NOVELTY - A holding sealing material (4) comprises fiber assembly of material containing alumina-silica-type fibers (6) which are aggregated in mat form. The holding sealing material is provided at gap of a supporting catalyst (2) and metal shells (3), and covers the outer periphery of supporting catalyst. The crystallization rate of surface-side portion (S1) of holding sealing material is different from the crystallization rate of surface-side portion (S2).    USE - Holding sealing material is used for catalytic converter (claimed) for fuel cell modifier, diesel particulate filter, and internal combustion engine used for motor vehicle.    ADVANTAGE - The holding sealing material having excellent supporting-catalyst retainability is easily, reliably and economically manufactured. The catalytic converter comprising the holding sealing material has excellent sealing characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalytic converter.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the catalytic converter.    Supporting catalyst (2)    Metal shell (3)    Holding sealing material (4)    Alumina-silica-type fiber (6)    Surface-side portions (S1,S2)
NOVELTY - The apparatus has light source unit (1) which emits laser beam, and light receiving unit (3) that receives Raman-amplified laser beam in measurement atmosphere (2), as measurement light and outputs the light reception signal according to measurement light. A gas detection unit (4) calculates gas concentration of detection object gas contained in measurement atmosphere based on ratio of fundamental wave signal of wavelength modulation frequency and harmonic signal detected from light reception signal.    USE - Gas detection apparatus for detecting gas such as methane, oxygen, carbon dioxide, acetylene and ammonia in remote place such as sea-bottom and pit.    ADVANTAGE - The gas existed in remote place can be detected with high precision by suppressing stimulated Brillouin scattering.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of gas detection apparatus. (Drawing includes non-English language text)    Light source unit (1)    Measurement atmosphere (2)    Light receiving unit (3)    Gas detection unit (4)    Light output unit (12)
NOVELTY - The cell has a gas supply flow path (30ci) formed in a side that touches a gas diffusion layer at a gas flow path formation part. A downstream end obstructed in gas supply flow path and an upper end obstructed in a gas discharge flow path (30co) of an isolation structure are arranged along a perpendicular direction by turns on both sides of a closed part. The gas supply flow path is formed, so that a middle part of an upper end side turns into a lowest part with respect to the perpendicular direction among the flow paths from the upper end to the downstream end.    USE - Fuel cell i.e. solid polymer electrolyte type fuel cell, for generating electric power.    ADVANTAGE - The cell ensures that volume of gas flowing through a bending part increases and extrudes to the gas discharge flow path, and the gas is easy to discharge through a gas diffusion layer or a catalyst electrode layer, thus suppressing retention of water and suppressing fall of electric power generation performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a gas flow path formed in a separator of a cathode side from a gas diffusion layer side.'(Drawing includes non-English language text)'    Gas flow path (30c)    Gas supply flow path (30ci)    Gas discharge flow path (30co)    Gas supply manifold (40i)    Gas discharge manifold (40o)
NOVELTY - The method involves preparing (S1) carbon that carries a catalyst, and a polymer electrolyte. A solvent is stirred (S4) to the carbon and the polymer electrolyte by applying shearing force. A carbon fiber is added and stirred (S6) into mixture of the stirred carbon, the polymer electrolyte and the solvent, where the carbon, the polymer electrolyte and the solvent mixture are grinded (S3) before stirring the solvent to the carbon and the polymer electrolyte.    USE - Method for manufacturing paste utilized for an electrode catalyst layer of a fuel cell i.e. polymer electrolyte fuel cell, to generate electric power in a motor vehicle.    ADVANTAGE - The polymer electrolyte is uniformly dispersed by stirring the mixture of the carbon, the polymer electrolyte and the solvent by applying the shearing force, so that the polymer electrolyte can be effectively fixed for the catalyst, and adhesion of the polymer electrolyte to the carbon fiber by addition of subsequent carbon fiber and stirring can be suppressed, thus increasing electric power generation performance of a fuel cell while restraining usage-amount of an expensive catalyst. The carbon is finely grinded for increasing a surface area of the carbon by grinding the carbon mixture, the polymer electrolyte and the solvent before stirring the mixture, so that utilization factor of the catalyst carried by the carbon can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing paste for electrode catalyst.'(Drawing includes non-English language text)'    Carbon and polymer electrolyte preparing step (S1)    Carbon, polymer electrolyte and solvent mixture grinding step (S3)    Solvent stirring step (S4)    Catalyst and polymer electrolyte mixture obtaining step (S5)    Carbon fiber adding and stirring step (S6)
NOVELTY - Method for removing calcium containing foreign substance (W2), involves throwing organic waste (W1) in a separation tank (1), utilizing difference of solubilization time of the organic substance in the organic waste and calcium containing foreign substances, storing the organic waste in the separation tank for predetermined time, stimulating solubilization of the organic substance, and selectively removing the calcium containing foreign substances remained in unsolubilized state.    USE - The method is useful for removing calcium containing foreign substances which is used in methane fermentation system.    ADVANTAGE - The method is simple, cost-effective, and environmentally-friendly, and consumes less energy. The method simultaneously performs solubilization of organic waste and removal of foreign substances.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) unit for removing calcium containing foreign substances (A) comprising a separation tank which stimulates solubilization of the organic substance in the organic waste while providing the bottom portion of down substantially cone form, unit for stirring (2) the organic waste in the separation tank, and unit for discharging foreign substances (3); and    (2) methane fermentation preprocessing system comprising the above-cited unit.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic figure of Vertical cross sectional view of calcium containing foreign substances removal unit.    Separation tank (1)    Stirring unit (2)    Foreign substances discharge unit (3)    Liquid supply unit (32,33)    Opening and closing unit (34)    Calcium containing foreign substances removal unit (A)    Organic waste (W1)    Calcium containing foreign substances (W2)
NOVELTY - The furnace has a vaporizing furnace barrel (1) whose bottom part is provided with air intake pipes (2). An end of one of the air intake pipes is connected with a fan (14), where another end of the air intake pipe is connected with a secondary oxygen supply pipe (13), an ash discharge plug (5) and a gas pipe (8). The secondary oxygen supply pipe is provided with a secondary oxygen supply switch (6). The bottom part of the barrel is provided with an ash discharging lighting port (4). The air intake pipes are parallely arranged on a bottom part of the barrel.    USE - Horizontal organic matter vaporizing furnace for treating crop straw, organic house refuse and medical rubbish to provide large fuel for a company and a house.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a horizontal organic matter vaporizing furnace.    Vaporizing furnace barrel (1)    Air intake pipes (2)    Ash discharging lighting port (4)    Ash discharge plug (5)    Secondary oxygen supply switch (6)    Gas pipe (8)    Secondary oxygen supply pipe (13)    Fan (14)
NOVELTY - The device has a hopper-shaped discharge bucket (2) arranged under a furnace body (1). A discharge port (3) is positioned on bottom part of the hopper-shaped discharge bucket. A furnace door (4) is hinged on exterior of the discharge port. A locking mechanism (5) i.e. hinge latch, is positioned between the furnace door and the hopper-shaped discharge bucket.    USE - Deslagging device for an energy-saving gasification furnace.    ADVANTAGE - The device ensures gas tightness of an energy-saving gasification furnace, and increases air output of the furnace so as to save consumption of raw material. The device can easily discharge the slag, is inexpensive, ensures high air output, has simple and rational structure, and realizes better use effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a deslagging device.    Furnace body (1)    Hopper-shaped discharge bucket (2)    Discharge port (3)    Furnace door (4)    Locking mechanism (5)
NOVELTY - The combustor has a combustion chamber connected to a feeding pipe and an air discharging pipe, where an axial internal wall of the feeding pipe is tangentially arranged with an internal wall of a transversal section of the combustion chamber. The air discharging pipe is transversally arranged in a center part of the combustion chamber. A left end of the air discharging pipe is inserted into an internal end of the combustion chamber. A right end of the air discharging pipe is stretched out from the combustion chamber.    USE - Cyclone dust removing biomass gasification combustor.    ADVANTAGE - The combustor allows air to enter into the combustion chamber with biomass material from the feeding pipe to form cyclone so as to promote the combustion of the biomass material. The combustor can separate ash slag under the action of the centrifuging force of cyclone, so that the biomass gas is maintained in clean manner. The combustor has better dust removing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a cyclone dust removing biomass gasification combustor.
NOVELTY - The device has a fluidized gasification reactor arranged in a biomass gasification reacting system. A fuel gas pipeline is connected to the fluidized gasification reactor. A water container is located on a top part of a shell. A bottom part of a draw bar is connected to a top part of a bell jar and passed through a through-hole on the top part of the shell. Another bell jar is connected to the draw bar and covered on a top end of a pipeline unit of the water container, where bottom of the latter bell jar is located below a water surface in the water container.    USE - Biomass combustible gas water-seal device for a biomass gasification reacting system (Claimed).    ADVANTAGE - The device prevents explosions and leakage problems in the biomass gasification reacting system and avoids unstable air pressure and unstable gas production rate in a biomass combustible gas well, so that the device can operate the biomass gasification reacting system with better safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification reacting system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass combustible gas water-seal device.
NOVELTY - The furnace has a gasification furnace chamber provided with a drying region, an oxidizing region, a reducing region i.e. stomach-shaped cavity, and an ash removing region from top to bottom in series. A drying region chamber is in the form of an inclined surface cavity. An oxidizing region cavity is in the form of a cylindrical cavity. The reducing region is big on a middle part and small on two ends. A dust removing region is in form of a tapered surface cavity that is big on an upper part and small on a lower part.    USE - Lower suction type gasification furnace.    ADVANTAGE - The furnace has high temperature fuel gas that is blocked by a baffle plate of the furnace, and the heat is transferred to the drying region for reinforcing drying of the material, and part impurities such as vapor ash, can be separated from the fuel gas by blocking, thus realizing primary filtering function. The furnace has a draining hole that is sealed by a choke cover in the operating process, so that the furnace is convenient to open for cleaning accumulated dirty water when the furnace is stopped. The furnace has fuel gas filter function.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a lower suction type gasification furnace. '(Drawing includes non-English language text)'
NOVELTY - The device has an automatic feeding device installed between a fuel box and a gasification furnace. A feeding hole of the automatic feeding device is formed with the fuel box. A discharging hole is formed with a feeding hole of the gasification furnace. The feeding hole is formed on an upper end of a shell. The discharging hole is installed on a lower end the shell. A loading core is divided into three equal parts. A material is fed and discharged rotatably in the shell under driving of a driving mechanism. A protection valve is installed on a gas reflux channel.    USE - Automatic-feeding updraught gasification device.    ADVANTAGE - The device quantitatively feeds the material, does not cause incomplete gasification, does not waste fuel, and ensures gas quality and efficiency. The device refluxes the tar, so that the gas is environment-friendly. The device has reduced investment, simple operation, easy management and no pollution, and achieves gasification at any time, and does not need the gas storage device and transport. The economic performance of the device is better than that of a biomass biogas central gas supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an automatic-feeding updraught gasification device.
NOVELTY - The device has a level upper baffle (2) assembled in an upper part of an inner chamber of a fuel collecting tank (1). A lower baffle (3) is provided in a lower part of the inner chamber of the fuel collecting tank. The upper baffle and the lower baffle divide the inner chamber of the fuel collecting tank up and down into an exhaust buffer chamber (1-1), a fuel finishing chamber (1-2) and an intake buffer chamber (1-3). A tar collector (10) is arranged under the fuel collecting tank and connected to the fuel collecting tank through a guide pipe (9) that is provided with a valve (11).    USE - Air-cooling biomass tar processing device.    ADVANTAGE - The device can conveniently process water-cooling tar without utilization of large amount of water and cooling system with complex pipe connection.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an air-cooling biomass tar processing device in partial section.    Fuel collecting tank (1)    Exhaust buffer chamber (1-1)    Fuel finishing chamber (1-2)    Intake buffer chamber (1-3)    Level upper baffle (2)    Lower baffle (3)    Guide pipe (9)    Tar collector (10)    Valve (11)
NOVELTY - The purifier has a shell (3) whose lower part is formed with an impurity discharging port (2). An air inlet (5) is arranged at an upper part of a side of the shell. An air outlet (6) is arranged at a lower part of another side of the shell. The shell is provided with a purifying device that is formed by crossing and arrangement of two upper purifying sheets (1) connected with an upper wall in the shell. Two lower purifying sheets (4) are connected with a lower wall in the shell. An ambulatory-shaped upper passage and an ambulatory-shaped lower passage are formed in the shell.    USE - Straw gasification furnace fuel gas purifier.    ADVANTAGE - The purifier effectively removes impurities such as water content and dust powder, in fuel gas by using gravity settling and baffle separation theories. The impurities in the straw fuel gas are avoided to block an outlet of the purifier, thus ensuring normal utilization of the gasification furnace, and saving gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace fuel gas purifier.    Upper purifying sheets (1)    Impurity discharging port (2)    Shell (3)    Lower purifying sheets (4)    Air inlet (5)    Air outlet (6)
NOVELTY - The method involves determining a settling location of nitrifying bacteria. Samples of settled waste solids are obtained. The samples are tested using genus-specific analysis to determine settling characteristics and concentrations of bacteria in a clarifier. An inlet port is placed in the clarifier to collect recycling bacteria at a settling location of the recycling bacteria, where the recycling bacteria is nitrifying bacteria or Anammox bacteria. The recycling bacteria are returned to a wastewater basin to remove nitrogen contaminants from the wastewater.    USE - Method for enhancing nitrification or anaerobic ammonium oxidation in wastewater such as domestic or municipal wastewater.    ADVANTAGE - The method enables allowing an aeration basin to be efficiently utilized when solids retention time (SRT) is uncoupled, so that overall hydraulic residence time is reduced in cost effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an activated sludge system.
NOVELTY - A process for the production of biodiesel, is disclosed. Particularly, a process for the production of biodiesel from high free fatty acid content raw material, is disclosed. Image 0/0
NOVELTY - The system has a hydrogen reactor (12) comprising an interior chamber (14) and a set of electrode plates (16) arranged in a predetermined stacked array within the chamber. The electrode plates include a set of positively charged and negatively charged plates placed in a predetermined spaced position relative to one another to define the predetermined stacked array. An electrolyte source directs a jet of electrolyte between the electrode plates. A hydrogen reactor produces hydrogen gas through electrolytic decomposition of water (17).    USE - System for producing hydrogen gas utilized in powering an internal combustion engine of a motor vehicle.    ADVANTAGE - The system comprises the operative components associated with installed type of vehicles as an after market product, thus increasing the fuel efficiency during operation of the vehicle under various driving conditions based on reduction in the consumption of the fossil fuel intended to be used in the powering the motor vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial cutaway view of the portion of the structural and operative features of the system.    Hydrogen reactor (12)    Interior chamber (14)    Electrode plates (16)    Water (17)    Splash guard (23)
NOVELTY - Producing alcohol or hydrogen gas comprises culturing alcohol producing microorganisms in a waste fermented solution produced during the bioethanol production process.    USE - The method is useful for producing alcohol (butanol, 1,3-propanediol or ethanol) or hydrogen gas (claimed), which is used as biofuel.    ADVANTAGE - The method: is economically efficient and environmental friendly by lowering the high concentration of organic matter of the waste fermented solution; and provides ethanol waste fermented solution distillate or filtrate may as a alcohol-producing medium without any pretreatment.
NOVELTY - A yield efficiency of methane in anaerobic process of organic waste is increased by adding powders with not less than 15% free trivalent iron oxide into an anaerobic biochemical system for producing methane from organic waste to be uniformly mixed. The organic waste is an organic matter that can be biologically degraded. The dosage of the powders is 0.5-5% of the mass of the organic waste counting based on the amount of the iron oxide.    USE - Method for increasing yield efficiency of methane in anaerobic process of organic waste (claimed).    ADVANTAGE - The iron ions released when the free trivalent iron oxide is reduced by microbe are capable of prompting the activity of the anaerobe, e.g. methane bacteria to increase the speed and yield of producing the methane from organic waste. The method increases yield and production speed of methane in methane energy source utilization system, e.g. municipal domestic waste, processed agricultural product waste, residual sludge of municipal sewage plant, and excrement of intensification farm, and increases the utilization efficiency of recyclable energy sources of organic waste.
NOVELTY - One type of coal or a mixture of coal is ground as raw material to less than 180 mesh. A coal tar adhesive agent is added, agitated and mixed uniformly using an agitation apparatus, and extruded and molded using a molding machine. Air is removed from a carbonizing furnace, and the molded product is carbonized and cooled to obtain a carbonaceous bio-carrier.    USE - Preparation of low-density carbonaceous bio-carrier for use in sewage treatment.    ADVANTAGE - The method enables preparation of carbonaceous bio-carrier having low density, which reduces power consumption when fluidizing in a biological fluidized bed. Since bump among the particles is reduced, the usage time is improved.
NOVELTY - A material shell (1) is provided at the upper end with a feeding port (1-1), and at the lower end with a discharging port (1-2). A material-filling roller (2) is equally divided into at least three material-filling hoppers (2-1) to rotatably feed and discharge in order in the material shell as a driving shaft (3) is driven.    USE - Automatic feeding device for converting low biomass into combustible gas.    ADVANTAGE - Realizes material supply without causing incomplete gasification and without causing fuel waste. Quality of gasification and production efficiency is guaranteed. Low in investment, simple in operation, and easy to manage.    DESCRIPTION OF DRAWING(S) - The drawing shows a front schematic view of the automatic feeding device.    Material shell (1)    Feeding port (1-1)    Discharging port (1-2)    Material-filling roller (2)    Material-filling hopper (2-1)    Driving shaft (3)
NOVELTY - The generator has a gas conduit that is penetrated through material outlet of guiding device. The gas inlet of gas conduit is arranged on upper end inside the material containing vessel. The recycling mouth is arranged on guiding device between material inlet and material outlet or on pipeline interconnected with guiding device, such that the recycling mouth is higher than material outlet. The recycling vessel is arranged below the recycling mouth.    USE - Biogas generator.    ADVANTAGE - The generator is featured with good sealing property and good safety performance. The feeding and discharging of material can be regulated automatically due to biogas pressure, so that the biogas can be produced stably even during cold weather.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas generator.
NOVELTY - The combustor has a hollow cylindrical combustion chamber connected with a feeding pipe and an air outlet pipe. A left end of the air outlet pipe is arranged in the combustion chamber and provided with an internal end. A right end of the air outlet pipe is extended out of the combustion chamber and provided with an extended end. A wind chamber is arranged between a cavity body and the combustion chamber and connected with a wind pipe. The air outlet pipe is formed with air outlet holes. The wind chamber is formed with the other air outlet holes.    USE - High-energy biomass gasification combustor.    ADVANTAGE - The air outlet pipe is formed with the air outlet holes and the wind chamber is connected with the other air outlet holes so as to supply oxygen to clean biomass fuel gases before entering into a boiler, obtain high energy, combust biomass fuel gases in a boiler completely and produce high combustion energy of the boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high-energy biomass gasification combustor in partial section.
NOVELTY - The gasifier has an air distributing chamber (2) provided at a lower part of a furnace body (1). A furnace top (3) is provided at an upper part of the furnace body. A coiled heat exchanger (5) is provided inside a furnace top, where one end of the coiled heat exchanger is welded and connected with an inlet pipe (4) and another end of the coiled heat exchanger is welded and connected with an exhaust pipe (6). An end of the exhaust pipe is connected with the air distributing chamber.    USE - Biomass gasifier for a fluidized bed.    ADVANTAGE - The gasifier is simple and compact in structure, convenient to manufacture and environment friendly and energy-saving, and utilizes biomass to generate combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasifier.    Furnace body (1)    Air distributing chamber (2)    Furnace top (3)    Inlet pipe (4)    Coiled heat exchanger (5)    Exhaust pipe (6)
NOVELTY - The methane tank has tank main portion (1) and current guide plate (3).A material pouring port (2) is mounted on upper portion of the tank main portion. The current guide plates are horizontally and uniformly distributed around inner wall and upper middle portion of tank main portion. The vertical lines of current guide plates are horizontally and uniformly distributed around an inner wall of tank main portion. The section of current guide plate is provided with curvature which is similar to that of special curve face of airscrew.    USE - Methane tank.    ADVANTAGE - The methane tank is simple in structure. The cracking liquid level incrustation can be performed through disturbance of special curve face of current guide plate when methane liquid level increases or decreases, so that normal fermentation methane generation can be guaranteed. The material from tank can be released effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of methane tank.    Tank main portion (1)    Material pouring port (3)
NOVELTY - Combined anaerobic pre-treatment of domestic sewage and organic waste comprises acid generating reactor (anaerobic sequencing batch reactor ASBR type), regulating pond, methane generating reactor (ASBR type), wastewater delivering system, reactor temperature control system, and methane measuring device    USE - Combined anaerobic pre-treatment of domestic sewage and organic waste in village beside lake.    ADVANTAGE - Both acid generating reactor and methane generating reactor (ASBR type) has simple structure, low investment, good flocculating and solid/liquid separating effect, strong reacting propelling force and low operation cost. They are capable of forming granular sludge taking Sarcina methanica as superior bacteria. They are specifically suitable for low-investment and low-scale sewage processing especially in village.
NOVELTY - A high-efficiency domestic sewage processing device comprises a sewage pond (1), a ground source heat pump (2) beside the sewage pond, and an outlet pipeline (21) of the ground source heat pump connected with an inlet pipeline (22) of the ground source heat pump through a heat exchanger (3) in the sewage pond. A middle segment of the inlet pipeline of the ground source heat pump having a heat absorbing segment (23) deeply embedded in the ground.    USE - A high-efficiency domestic sewage processing device.    ADVANTAGE - The sewage pond may be heated by the ground source heat pump and the heat exchanger, to accelerate metastasis and improve sewage treatment efficiency. The device is simple and convenient to maintain.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the domestic sewage processing device.    Sewage pond (1)    Ground source heat pump (2)    Heat exchanger (3)    Outlet pipeline (21)    Inlet pipeline (22)    Heat absorbing segment (23)
NOVELTY - The furnace has a main portion that is provided with steam generation block and moisture adjustment spray nozzle. The smoke flue is provided with atomizing dust removing chamber, humidifying dust removing chamber, air guide pipe and atomizing coke collecting chamber sequentially. The air guide pipe is provided with steam pipe. The atomizing coke collecting chamber is provided with high pressure spray nozzle and coke collecting pool. The coke collecting pool of coke collecting chamber is provided with high pressure spray nozzle and siphon water discharge pipe.    USE - Self-combustion type pollution-free carbonization furnace for use in manufacturing of charcoal.    ADVANTAGE - The accumulation of atmospheric pressure in the self-combustion type pollution-free carbonization furnace is eliminated. The safety to the user is improved, as the carbonization furnace provides automated earthing installation. The charcoal is manufactured effectively by performing biomass transfer of agricultural straws and residuals.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the self-combustion type pollution-free carbonization furnace.
NOVELTY - A high-efficiency anaerobic biological tower reactor comprises a tank body (1), a water circulation part (2), a reaction part (3) and a three-phase separator. The inner side of tank body is provided with the reaction part and the water circulation part. The reaction part is provided with a three-phase separator; and the bottom in the tank body is provided with a rotary water distribution part (5). The reaction part is communicated with a biogas collecting part (4).    USE - High-efficiency anaerobic biological tower reactor.    ADVANTAGE - The tower reactor functions in large-resistance rotating water distribution, uniformly water distribution, and stirring. It has stable working and simple operation. Water intake along water loss is far less than partial water loss. Service area of every water outlet is basically the same, so that water distribution is uniform without dead zone. The unit area water intake quantity is basically the same; the intake water can be sufficiently contacted with the mud; anaerobic mud is at swelling state on vertical direction; and the anaerobic microorganism is sufficiently contacted with the matrix to reach good mass transfer effect. The reactor realizes rotary water distribution by arranging different installation angles of the water outtake pipe, so that the anaerobic mud rotates on the horizontal direction, so as to further avoid happening of the dead zone. The reactor avoids outtake water from backflowing to cause guanite crystallizing and blocking problem, and high-effectively removes organic pollutant. It has low power consumption and high gas producing rate, and benefits for energy recycling.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the high-efficiency anaerobic biological tower reactor.    Tank body (1)    Water circulation part (2)    Reaction part (3)    Biogas collecting part (4)    Rotary water distribution part (5)
NOVELTY - A special soil modifier comprises (pts.wt.) extract residues (40-60), livestock and poultry manure (20-30), furnace slag (10-20), full-value nutrient element (0.2-0.5), and composite fermentation fungicide and mycorrhizal fungi fungicide (0.01-0.05). The composite fermentation fungicide comprises Saccharomycetes, Actinomycetes, phosphorus-degrading bacteria and potassium-degrading bacteria. The mycorrhizal fungi fungicide is mixture of Glomus mosseae and Gluomus etunicatum fungicide.    USE - A special soil modifier (claimed).    ADVANTAGE - The soil modifier enhances organic substance content in the soil, increases soil permeability, and prevents the salt from rising, thus ensuring cultivation sustainability. The use of the extract residues reduces environmental pollutant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the special soil modifier comprising uniformly mixing extract residues, livestock and poultry manure, furnace slag, full-value nutrient element, composite fermentation fungicide and water, allowing the mixture to ferment, adding mycorrhizal fungi fungicide to the fermentation product, mixing uniformly, and air-drying resulting product.
NOVELTY - Anaerobic treatment device for treating commercial pulp papermaking waste water comprises a hydrolyzing and pre-acidifying reactor, a feeding tank and an anaerobic reactor. The liquid level of the feeding tank is lower than the hydrolyzing and pre-acidifying reactor. The feeding tank is connected with the anaerobic reactor by a lifting water pump and a flow meter.    USE - The anaerobic treatment device is useful for treating commercial pulp papermaking waste water.    ADVANTAGE - The device: drastically reduces the amount of sludge, secondary sludge pollution into the environment and the power consumption; produces biomass energy and biogas; and reduces the operation cost.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the anaerobic treatment device for treating commercial pulp papermaking waste water.
NOVELTY - A large-scale sealed straw gasifying system comprises carbonizing chamber connected to tar settling chamber, spray tower, solid purifier, cooling purifying device, blower fan, rotary purifier, water purifier and solid purifier. The output end of solid purifier is connected to a large-scale gas storage tank, the gas storage tank is connected to the user through gas transmission tube net. The tar settling chamber, spray tower, solid purifier, cooling purifying device, rotary purifier, water purifier and solid purifier are connected to a tar recycling pool through tubes.    USE - A large-scale sealed straw gasifying system for producing carbon.    ADVANTAGE - The device adopts thermal cracking technique in producing combustible gas without using gasifying agent, where the combustible gas has high heat value. The combustible materials that cannot be gasified are used for producing good charcoal, thus increasing usage rate of raw materials.
NOVELTY - The filler includes raw material containing 50-80 parts of sludge, 10-30 parts of straw, 10-15 parts of clay and 25-50 parts of water. A hollow convex hemisphere (1) and hollow concave hemisphere (2) with equal outer diameters are provided. A lug boss structure (3) of the hollow convex hemisphere is embedded in a recess structure (4) of the hollow concave hemisphere. The convex and concave hemispheres are opened with round, triangle and rectangle shaped multiple through holes (5).    USE - Hollow spherical porous filler for use in constructed wetland.    ADVANTAGE - The water quality of constructed wetland is improved such that biochemical oxygen demand (BOD) index can be reduced by 10-50% and suspended solid (SS) demands are reduced by 50%. The cost of the raw material and processing cost of the hollow filler are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the hollow spherical porous filler.    Hollow convex hemisphere (1)    Hollow convex hemisphere (2)    Lug boss structure (3)    Recess structure (4)    Through hole (5)
NOVELTY - The manufacturing device has a spiral conveying machine through which a material feeding machine, a wire drawing machine, a mixing pulping machine, a separator and a liquid storing tank are communicated with each other. A squeezing shaping machine is located by the side of the wire drawing machine, mixing pulping machine and separator. The separator is internally provided with a 50 micrometers filtering net and a 30 micrometers filtering net which is arranged below the 50 micrometers filtering net.    USE - Single/multiple component biomass solid and liquid fuel manufacturing device.    ADVANTAGE - The breakage rate of the single/multiple component biomass solid and liquid fuel manufacturing device can be improved at high production rate. The shaping of components is simplified during the squeezing process. The unnecessary repeated squeezing process can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the single/multiple component biomass solid and liquid fuel manufacturing device.
NOVELTY - Processing ethanol waste water of sweet potato fuel, comprises processing sequencing batch type anaerobic sludge bed (ASB) anaerobic reaction, two-stage sequencing batch bio-film reactor (SBBR) aerobic reaction and flocculation sedimentation.    USE - The method is useful for processing ethanol waste water of sweet potato fuel.    ADVANTAGE - The method: has high organic load of the anaerobic reaction, short hydraulic retention time, high removal rate of organic matter and high rate of methane productivity; solves the problem of operating high concentrations of in-fluent SS high-rate anaerobic reactors; has high removal rate of aerobic organic matter; has good denitrification effect; has chromaticity of the flocculation sedimentation and total phosphorus removal rate of more than 95%; and has COD removal rate of 70%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for processing ethanol waste water of sweet potato fuel.
NOVELTY - The digester has a rotary shaft installed perpendicularly at the center of annular bearing, and a cylinder pipe in which lower end is welded between surfaces of digestion tank. The digestion tank is installed in outside of shaft provided between propeller blades at predetermined angle. A circular hole is formed in central portion of bottom of sleeve having biogas anti leakage seal (A). Several bending lines and flat portions are formed in the edge of metal plate. A virtual vertical plane board is provided in lower portion of shaft at an angle of 15 degrees .    USE - Mechanical stirred type anaerobic digester for biogas production.    ADVANTAGE - The anaerobic digester increases the yield of biogas and prevents the leakage of biogas in the shaft of the mixer. The biogas can be manufactured from high concentration organic liquid waste in the mixing unit of the digestive fluid within the digestion tank and the bearing, the mixing effect is optimized and the anaerobic fermentation is accelerated. The efficiency of biogas production can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the anaerobic digester.    Warm water inlet pipe (3)    Warm water drain (4)    Biogas exhaust pipe (6)    Reduction motor (7)    Biogas anti leakage seal (A)
NOVELTY - The controller has an electric valve whose control circuit is provided with a TLP521 type optical isolation chip and a relay. A control circuit of a blower fan includes another optical isolation chip and a controllable silicone. The control circuit of the electric valve, the latter optical isolation chip, a temperature sensor and a LCD display module are connected with a single chip computer. The electric valve is connected between the relay and a gasification furnace. The blower fan is connected between the controllable silicone and the gasification furnace.    USE - Automatic controller for a biomass gasification furnace that is utilized for baking tobacco leaves.    ADVANTAGE - The controller is simple in structure, convenient to operate. The controller accurately and timely controls the temperature, reduces labor intensity, and effectively improving quality of baking tobacco leaves.    DETAILED DESCRIPTION - The single chip computer adopts a microcontroller Upd78F0537A of 78K0 Kx2 series. The electric valve is adopted with an O-shaped ball valve. The temperature sensor is adopted with a digital temperature sensor DS18B20 of a single bus type.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an automatic controller. '(Drawing includes non-English language text)'
NOVELTY - The equipment (100) has a central control unit (40) that controls number of rotation of driving unit (30). The driving unit is connected to the mixing screw (20) positioned in the bottom portion of fermentation annihilation reaction bath (10). A sensor is connected to the fermentation annihilation reaction bath and central control unit. A gas trap portion (60) is connected to the upper end of the fermentation annihilation reaction bath for collecting the bio gas from the waste food (85).    USE - Biofuel equipment used in apartment house.    ADVANTAGE - Excellent fermentation annihilation reaction can be ensured with reduced external energy. The environmental contamination of the equipment can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biofuel equipment. (Drawing includes non-English language text)    Fermentation annihilation reaction bath (10)    Mixing screw (20)    Driving unit (30)    Central control unit (40)    Gas trap portion (60)    Waste food (85)    Biofuel equipment (100)
NOVELTY - Comprehensive use of plant lignocellulose, involves (1) crushing the biomass raw material, and steam blasting the obtained product, (2) preparing the obtained material based on solid and liquid ratio and uniformly stirring the obtained product, (3) performing enzymolysis by adding xylanase to obtained product to obtain crude sugar liquid containing oligosaccharide, and (4) separating residue from liquid after enzymolysis, and obtaining sugar liquid and sugar residue.    USE - The plant lignocellulose is useful for preparing oligosaccharide and ethanol.    ADVANTAGE - The plant lignocellulose is obtained by consuming less energy and does not require material for preprocessing including acid, alkali solution, and catalyst, reduces discharge of pollutant, and thus is environmentally-friendly, and improves the mass production of oligosaccharide and ethanol with high yield by gas explosion technology.    DETAILED DESCRIPTION - Comprehensive use of plant lignocellulose, involves (1) crushing the biomass raw material to mesh size of 10 or less, and steam blasting the obtained product at 1.5-3.5 Mpa for 30-120 seconds, (2) preparing the obtained material based on solid and liquid ratio of 1:5-8, adjusting pH value of the obtained product to 3-7, and uniformly stirring the obtained product, (3) performing enzymolysis by adding 10-20 IU/g of xylanase to obtained product at 30-70 degrees C for 4-20 hours to obtain crude sugar liquid containing 80% or more of oligosaccharide, and (4) separating residue from liquid after enzymolysis, and obtaining sugar liquid and sugar residue. The total content sugar solid in the sugar liquid is 2-8%. The sugar residue comprises 60-80% of water.
NOVELTY - The device has a spiral conveyor arranged at the lower side of a material hopper, partially arranged in the inner cavity of a rotary reactor and partially arranged out of the rotary reactor. Part of spiral conveyor in the rotary reactor is supported by a slide bearing. The external sleeve of a slide bearing is fixed on the rotary reactor. The internal sleeve of the slide bearing is fixed on the spiral conveyor. Part of spiral conveyor located out of the rotary reactor is supported by a bearing element. The rotary reactor is interconnected with a gas phase product discharging channel.    USE - Gas and solid phase continuous discharging device for pyrolytic product of organic solid waste.    ADVANTAGE - Gas and solid of solid waste in the reactor are continuously discharged in separated phase under the normal operation state of reactor; therefore, the whole process is automatically controlled, the environment is not polluted via sealed discharge, and safety is high.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the gas and solid phase continuous discharging device for pyrolytic product of organic solid waste.
NOVELTY - The separation device has a shunt (5) set on the top of B section of a main input pipe (6). One side of shunt is connected with the straight side of a tee fitting (3). A standpipe (7) extends vertically to a separation kettle (9) and connects to another side of shunt with the end away from the tee fitting of B section of the main input pipe in turn. The bottom, middle and upper parts of separation kettle are arranged with first liquid outlet (12), second liquid outlet (15) and third liquid outlet (13), respectively.    USE - Separation device for producing liquids from biomass pyrolysis.    ADVANTAGE - Separation device separates and purifies liquid by controlling the rate and velocity of liquid flowing into separation kettle. Separation device has rational structure and convenient use and popularization.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the separating device for producing liquids from biomass.    Tee fitting (3)    Shunt (5)    Main input pipe (6)    Standpipe (7)    Separation kettle (9)    First liquid outlet (12)    Third liquid outlet (13)    Second liquid outlet (15)
NOVELTY - The downdraft-type biomass gasifier has a reactive part (200) with a top end portion (210), in which a slope (110) is provided. A profile (221) is formed at a low end (220), where another profile (211) is also provided. A cross section edge of the top end portion is provided in concavo-convex regions.    USE - Downdraft-type biomass gasifier.    ADVANTAGE - The downdraft-type biomass gasifier has a reactive part with a top end portion, in which a slope is provided, where a profile is formed at a low end, and hence ensures simple and improved downdraft-type biomass gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a downdraft-type biomass gasifier.    Slope (110)    Reactive part (200)    Top end portion (210)    Profiles (211,221)    Low end (220)
NOVELTY - The power device has a solar battery (1) arranged on an adjustable support (2) and which produces current which is input into a brine electrolysis hydrogen manufacturing device (4) through a conductive wire (3) to generate hydrogen which is input in a workshop (6) for producing a hydrogen fuel storage container through a hydrogen transmission pipe (5). A hydrogen fuel storage container (7) conveyed from the workshop to be installed on the paddy planter. Hydrogen fuel is input in a hydrogen fuel battery (9) from the hydrogen fuel storage container through a hydrogen fuel transmission pipe (8).    USE - Power device for applying new solar hydrogen energy to a paddy planter.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the power device and paddy planter.    Solar battery (1)    Adjustable support (2)    Conductive wire (3)    Brine electrolysis hydrogen manufacturing device (4)    Hydrogen transmission pipe (5)    Workshop (6)    Hydrogen fuel storage container (7)    Hydrogen fuel transmission pipe (8)    Hydrogen fuel battery (9)
NOVELTY - The apparatus has a continuously perforated belt (120) that is arranged in a frame (100) using idle rollers (110a,110b). Compressive rollers (130,140,150) and a feeder roller (210) are interlinked by a roller driving unit (200). The feeder roller is arranged at the front side of the compressive roller (130). The supporting roller supports the lower side of the belt. The compressive rollers pressurize the upper side of the belt.    USE - Apparatus for recycling waste of beef cattle of stockbreeding farmhouse.    ADVANTAGE - The excretion of cattle is recycled and used as fertilizer without any bad odor. The cost burden on farmhouse for piling up the excrement is reduced by recycling the excrement. The fermentation is performed shortly with reduced energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for recycling waste of cattle.    Frame (100)    Idle rollers (110a,110b)    Belt (120)    Compressive rollers (130,140,150)    Roller driving unit (200)    Feeder roller (210)
NOVELTY - The biomass pyrolysis gas separating and condensing device has a liquid outlet which is connected with a chilling condenser (4) through a pump and a pipeline. The other liquid outlet is connected with a fractionator (8). The fractionator is provided with wood vinegar outlet (13) and a tar outlet (14) that are reserved on the fractionator. A gas outlet on the liquid storage tank (5) is connected with the condenser through a pipeline. The condenser is provided with a condensed water inlet, a condensed water outlet, a gas inlet and a gas outlet.    USE - Biomass pyrolysis gas separating and condensing device.    ADVANTAGE - Improves dust removal. Exhibits simple process and improves energy conservation.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass pyrolysis gas separating and condensing device.    Chilling condenser (4)    Liquid storage tank (5)    Fractionator (8)    Wood vinegar outlet (13)    Tar outlet (14)
NOVELTY - The device has a reaction kettle connected to a synthesized gas condensing device by a synthesized gas cooling device and a synthesized gas distributing device. The synthesized gas condensing device is connected to a thermal cracking liquid collecting box. The synthesized gas condensing device is connected to the synthesized gas condensing device by the synthesized gas pipe device and the synthesized gas burning device.    USE - Plant thermal cracking device used in agroforestry plant treating technology.    ADVANTAGE - Device has no need of using extra energy and special operation technology or knowledge. Energy needed by the system can be self-supplied except a little kindling material for lighting the fire. System is safe, automatic and has low bias and can produce the obvious downstream product with high value without precise monitoring. The activity of waste treatment is generally recognized as a production procedure.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the plant thermal cracking device in agroforestry.
NOVELTY - The apparatus has a fuel cell main body, which produces electric power with fuel by which steam reforming is carried out. A control unit controls water vapor/steam supply amount supplied by a water vapor/steam supply unit, and fuel supply amount supplied by a fuel-supply unit, where supply of the water vapor/steam and the fuel are stopped in a state in which taking-out of the electric power by an electric power extraction part is stopped when continuation time of abnormality exceeds predetermined time and the fuel supply amount does not reset to a normal state.    USE - Fuel cell apparatus i.e. solid oxide fuel cell (SOFC), for producing electric power to carry out steam reforming.    ADVANTAGE - The apparatus enables electric power generation by a fuel cell stack to be stopped by temporary fluctuation/variation of water vapor volume in the modifier so as to prevent a situation where decline in electric power generation efficiency is prevented and function lowering of the fuel cell main body even in a case where fuel supply amount is abnormal.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating abnormal countermeasure control of fuel supply amount in fuel cell apparatus . '(Drawing includes non-English language text)'
NOVELTY - Method for producing ethanol, involves mixing transformed yeast capable of expressing formate dehydrogenase with saccharification biomass and culturing the biomass.    USE - The method is useful for producing ethanol used as alternative fuel.    ADVANTAGE - The method prevents global warming in atmosphere and food problem as it utilizes lignocellulosic biomass e.g. rice straw and wheat straw, and waste material as raw materials.
NOVELTY - Manufacture of tungsten oxide-alumina catalyst, involves pre-processing alumina at predetermined temperature, mixing 5-30 parts weight of tungstic acid with 100 parts weight of alumina, adding aqueous solution of ammonium hydroxide and nitric acid to the mixture, stirring the mixture, filtering and drying the mixture, and plasticizing the mixture.    USE - Manufacture of tungsten oxide-alumina catalyst useful for removing free fatty acid from waste edible oil (both claimed) for producing raw material for biodiesel fuel.    ADVANTAGE - The tungsten oxide-alumina catalyst has strong acid strength, can be manufactured simply and cost-effectively, and is suitable for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) tungsten oxide alumina catalyst manufactured by the above-mentioned method; and    (2) method of removing free fatty acid from waste edible oil, involves mixing alcohol with waste edible oil in the ratio of 1:1-1:12, adding tungsten oxide alumina catalyst (1-30 g with respect to 100 ml of waste edible oil), stirring and esterifying the mixture at 100-1200 revolutions per minute (rpm) and 60-250 degrees C for 2-12 hours, isolating the catalyst from the waste edible oil using centrifuge, and isolating triglceride which is main component of ester from the waste edible oil.
NOVELTY - Producing pyrolysis oil comprises providing a reactor containing multiple catalysts; fluidizing the catalysts; entraining a biomass fluidized catalysts, so that the biomass is pyrolyzed; and collecting the resultant pyrolysis oil.    USE - The processes are useful for producing pyrolysis oil; and for producing fuel (all claimed).    ADVANTAGE - The invention provides methods for fractional catalytic pyrolysis which allow for conversion of biomass into a slate of desired products without the need for post-pyrolysis separation. Biomass is added to the catalytic bed, preferably while entrained in a non-reactive gas such as nitrogen, causing the biomass to become pyrolyzed and forming the desired products in vapor and gas forms, allowing the desired products to be easily separated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process for producing fuel comprising providing a reactor containing multiple catalysts; fluidizing the catalysts; entraining a biomass fluidized catalysts, so that the biomass is pyrolyzed to produce pyrolysis oil; and cracking the pyrolysis oil; or a process for producing fuel comprising producing pyrolysis oil; blending the pyrolysis oil with gas oil to produce an oil blend; and cracking the oil blend.
NOVELTY - A method comprises transforming algae to express cellulase and/or hemicellulase; allowing the algae to secrete the cellulase and/or hemicellulase into a culture medium; and recovering the culture medium to obtain cellulase and/or hemicellulase.    USE - The method is used for producing cellulase and/or hemicellulase (claimed).    ADVANTAGE - The present invention provides methods for inexpensive production of cellulases and hemicellulases which can be used to hydrolyze cellulose and hemicellulose. It provides a method for co-producing both algae-based biofuels and lignocellulosic material biofuels. It also provides a biorefinery capable of producing both algae-based and lignocellulosic material based biofuels. The present invention provides multiple types of biofuels and/or other valuable products in the same biorefinery using shared resources.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a cellulase or hemicellulase that is obtained from an algal biofuel feedstock that has been transformed to express the cellulase or hemicellulase;    (2) a biofuel that is obtained from cellulosic biomass that has been hydrolyzed by a cellulase or hemicellulase derived from an algal biofuels feedstock that has been transformed to express the cellulase or hemicellulase; or a biofuel that is obtained from an algal biofuel feedstock that has been transformed to express the cellulase or hemicellulase; and    (3) a recombinant product other than cellulase or hemicellulase that is obtained from an algal biofuels feedstock that has been transformed to express both the recombinant product and the cellulase or hemicellulase.
NOVELTY - Conversion of biomass comprises charging a feed comprising a biomass and a synthetic thermoplastic polymer based material to a reactor (106) for contact with a catalyst and conversion to a product comprising liquid hydrocarbons, where the weight ratio of the biomass to the synthetic thermoplastic polymer based material is greater than 1:4.    USE - The process is useful for the conversion of biomass.    ADVANTAGE - The process improves the quality of fuel by reducing the oxygen content of liquid hydrocarbon product.    DETAILED DESCRIPTION - Conversion of biomass comprises: either charging a feed comprising a biomass and a synthetic thermoplastic polymer based material to a reactor (106) for contact with a catalyst and conversion to a product comprising liquid hydrocarbons, where the weight ratio of the biomass to the synthetic thermoplastic polymer based material is greater than 1:4; or charging a feed comprising a biomass and/or a biomass and a synthetic polymer based material to a first reactor for contact with a heat carrier material and conversion to a product comprising oxygenated hydrocarbons, charging at least a portion of the product to a second reactor along with a synthetic thermoplastic polymer based material for contact with a second reactor catalyst and conversion of the synthetic thermoplastic polymer based material to liquid hydrocarbons, and removing a second reactor bio-oil from the second reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for the conversion of biomass.    Biomass charging conduit (102)    Reactor (106)    Catalyst charging conduit (108)    Heating zone (114)    Pretreatment section. (118)
NOVELTY - A hydrogen generating system (1) comprises electrolyzer (10) comprising photocatalyst arranged to generate hydrogen from electrolyte (e.g. water) on illumination with solar radiation (3); photovoltaic cell (6) arranged to generate bias voltage on illumination with solar radiation; mechanism for applying bias voltage to electrolyzer; and at least one solar concentrator arranged to concentrate incident solar radiation onto electrolyzer and photovoltaic cell.    USE - System for generating hydrogen.    ADVANTAGE - The system allows solar radiation from relatively wide area to be focused onto reduced area of higher light intensity in which photovoltaic cells and electrolyzer are located, thus enabling fewer cells or smaller area of cells to be used in order to produce same amount of hydrogen. It reduces overall cost which is typically dominated by cost of photovoltaic cells and electrolyzer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating hydrogen generating system.    Hydrogen generating system (1)    Solar radiation (3)    Photovoltaic cell (6)    Electrolyzer (10)    Converter (12)
NOVELTY - An enhanced biodiesel fuel composition (C1) comprises: (a) an ester-based biodiesel component; and (b) a functionalized ester component comprising a functionalized ester (I). The functionalized ester (I) amounts to at least 0.1 wt.% of the biodiesel fuel.    USE - As an enhanced biodiesel fuel composition (claimed) useful for improving the low temperature properties of biodiesel.    ADVANTAGE - The enhanced biodiesel fuel composition extends the utility of the ester-based biodiesel fuels to colder climates (geographically and seasonally).    DETAILED DESCRIPTION - An enhanced biodiesel fuel composition (C1) comprises: (a) an ester-based biodiesel component; and (b) a functionalized ester component comprising a functionalized ester of formula C(R3)(R5)-CH(OC(O)R4)-R2-C(O)OR1 (I). The functionalized ester (I) amounts to at least 0.1 wt.% of the biodiesel fuel.    R1=1-3C alkyl;    R2 and R3=1-10C alkyl, or 1-10C alkenyl;    R4=2-20C alkyl or 2-20C alkenyl;    R5=H, hydroxyl, or 2-20C ester-forming carboxylate functional moiety.
NOVELTY - The method involves creating basic operation plan in which fuel cell (1) is operated within permissible operation time and a number of startup by basic operation plan creation unit (2). The special operation plan is drawn in which fuel cell is operated within range of other permissible operation time longer than a permissible operation time. The basic operation plan and special operation plan are selected by operation plan selection unit (4). The fuel cell is operated based on operating plan selected at operation plan selection process by fuel cell driving unit (5).    USE - Method for operating fuel cell system (claimed).    ADVANTAGE - The fuel cell system can be operated according to user's request. The occurrence of damage in the fuel cell system can be prevented. The lifetime of the fuel cell system can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Basic operation plan creation unit (2)    Special operation plan creation unit (3)    Operation plan selection unit (4)    Fuel cell driving unit (5)
NOVELTY - A hydrogen storage material comprises a porous material containing cluster containing metal ion and oxygen ion or metal ion and organic compound, and lithium supported on the inner surface of the porous material.    USE - Hydrogen storage material is used for manufacturing hydrogen for fuel cell used as power supply for electric vehicle.    ADVANTAGE - The hydrogen storage material has excellent hydrogen storage capability.
NOVELTY - Composition comprises polypeptide (P1) comprising a first amino acid sequence exhibiting at least 70% homology to amino acid sequence of Caldicellulosiruptor saccharolyticus glycoside hydrolase family 5 (GH5). The first amino acid sequence has thermostable or thermophilic cellobiohydrolase (CBH) or exoglucanase activity.    USE - The composition is useful for binding and hydrolyzing carbohydrate, preferably cellulose present in solution containing pretreated biomass chosen from pretreated cellulose biomass, pretreated hemicellulose biomass, pretreated lignocellulose biomass and their mixtures (all claimed), which is useful for producing sugars, specifically glucose, producing biofuel and processing other biomaterial, and for recycling paper and processing pulp for manufacturing paper.    ADVANTAGE - The composition comprising CBH is compatible with the ionic liquid treatment and it substantially improves the yield of saccharide products in a rapid and cost-effective manner compared to other commercially available enzymes. The formation of unwanted byproducts during the hydrolysis is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for hydrolyzing cellulose, which involves (a) preparing a composition comprising solution of an ionic liquid (IL) and cellulose, and (b) introducing the polypeptide (P1) such that the cellulose is hydrolyzed by the polypeptide.
NOVELTY - Growing an algal culture having a fatty acid content of at least 5x 10-12 g comprises: adding an algal culture to a growth medium comprising water, alkaline buffer solution, phosphate and nitrogen; and exposing the algal culture to a light condition greater than 60 mu E/m2/second, where the light schedule comprises at least 6 hours of light followed by at least 6 hours of darkness.    USE - The method is useful for growing an algal culture having a fatty acid content of at least 5x 10-12 g (claimed), where the algae is useful in production of biofuels.    ADVANTAGE - The method provides growth of large biomass of algae with high lipid content at low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a growth medium for an alga comprising: water; alkaline buffer solution; trace metal ion solution; vitamin solution; phosphate; and nitrogen;    (2) a method (II) of selectively generating an algal culture having identification property comprising: obtaining a first algal culture having an identification property containing a first value; isolating the first algal culture in a first growth medium; incubating the first algal culture in the first growth medium to provide a second algal culture; and sorting the second algal culture to select algal cells having the identification property containing a second value to provide a sorted portion of the second algal culture;    (3) a fatty acid mixture obtained from an alga comprising: 14C (14-25 wt.% of the total content); 16C (17-26 wt.% of the total lipid content); 18C (29-57 wt.% of the total lipid content); and greater than or equal to 20C (9-30 wt.% of the total lipid content); and    (4) an algal culture comprising many algal cells having an average fatty acid content of at least 5x 10-12 g/cell, where the algal culture is capable of surviving in fresh water.
NOVELTY - Preparing valganciclovir and its salt involves partially hydrolyzing in an alcohol solvent, protected ganciclovir bis(L-valinate) to corresponding protected ganciclovir mono-L-valinate.    USE - For preparing valganciclovir and its salt (preferably valganciclovir hydrochloride salt) (claimed) used for the treatment of cytomegalovirus (CMV) retinitis in patients with acquired immunodeficiency syndrome (AIDS) in adults and prevention of CMV disease in kidney, heart, and kidney-pancreas transplant patients at high risk in adults, and for prevention of CMV disease in kidney and heart transplant patients at high risk in pediatric patients.    ADVANTAGE - The process provides improved process for preparing valganciclovir and its salt, which is simple, cost-effective, commercially viable, sustainable, environmentally friendly, and avoids multiple protection-deprotection steps.    DETAILED DESCRIPTION - Preparing valganciclovir and its salt involves partially hydrolyzing in an alcohol solvent protected ganciclovir bis(L-valinate) of formula (VII) to corresponding ganciclovir mono-L-valinate of formula (VIII).    P1=amine-protecting group.
NOVELTY - The apparatus (10) has a frequency detection unit (20) to detect the system frequency of alternating current of converter (70). The active power output from the converter to alternating current system (80) is reduced and the grid connection point voltage of converter is raised, when the detected system frequency is greater than the frequency threshold value.    USE - Apparatus for controlling converter connected to electric power grid used for generating power using fuel cell, wind and secondary battery.    ADVANTAGE - The frequency control of electric power grid is performed efficiently, by reducing the active power output from converter to alternating current system and by raising the grid connection point voltage of converter, when detected system frequency is greater than the frequency threshold value.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the converter control apparatus. (Drawing includes non-English language text)    Converter control apparatus (10)    Frequency detection unit (20)    Phase detecting unit (40)    Converter (70)    Alternating current system (80)
NOVELTY - The system (S) has water supply apparatus (30) that performs water level maintenance control to maintain water level in anode humidifying water storage portion (13) and cathode humidifying water storage portion (14) at predetermined range. A control unit (Z) sets generating mode of fuel cell (12) while performing wastewater treatment at the time of abnormality generated from humidifying water storage portions when state of water level in anode and cathode humidifying water storage portion is detected as more than upper limit water level of predetermined range.    USE - Fuel cell system.    ADVANTAGE - Since the generating mode of fuel cell is set while performing wastewater treatment at the time of abnormality generated from the humidifying water storage portion, the water level in the storage portion can be reduced and permeation of water level from the storage portion for anode and cathode can be avoided even if the abnormality state in the water level is produced. Since the ion exchange treatment of the water stored by the water retention portion for replenishment is performed continuously or intermittently, the water supplied to the humidifying water storage portion for anodes and cathodes can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (12)    Anode humidifying water storage portion (13)    Cathode humidifying water storage portion (14)    Water supply apparatus (30)    Fuel cell system (S)    Control unit (Z)
NOVELTY - The fuel cell (10) has a fuel electrode (102) formed in a surface of an electrolytic membrane (101), which includes solid oxide. An air electrode (103) is formed in another surface of the electrolytic membrane. A renewable hydrogen-producing material (105) supplies produced hydrogen by reaction with water generated by electric power generation to the fuel electrode. The air electrode is supplied during the electric power generation, and a cooling unit (130) cools excess gas that is discharged.    USE - Fuel cell e.g. polymer electrolyte fuel cell (PEFC) and solid oxide fuel cell (SOFC), for a portable electronic device.    ADVANTAGE - The fuel cell is provided with the cooling unit that cools the excess gas that is discharged, so that the temperature of the gas discharged from the fuel cell and influence of the heat to surroundings of the fuel cell are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a structure of a fuel cell. '(Drawing includes non-English language text)'    Fuel cell (10)    Electrolytic membrane (101)    Fuel electrode (102)    Air electrode (103)    Renewable hydrogen-producing material (105)    Cooling unit (130)
NOVELTY - The method involves forming a negative electrode precursor containing apatite type silicic-acid lanthanum. A solid electrolyte thin film is formed by thermally spraying the apatite type silicic-acid lanthanum on a surface of the negative electrode precursor. A positive electrode is formed on the solid electrolyte thin film. Nickel oxide is restored to nickel in the negative electrode precursor by using the negative electrode precursor as a negative electrode by heat-processing the negative electrode precursor in a restoration state.    USE - Method for manufacturing a solid oxide fuel cell (SOFC) i.e. medium-temperature degree type SOFC.    ADVANTAGE - The method enables utilizing the apatite type silicic-acid lanthanum as the negative electrode by heat-processing the negative electrode precursor in the restoration state, thus providing precise cell with less thickness, and hence reducing manufacturing cost of the solid oxide fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a solid oxide fuel cell manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - A hydrogen gas is manufactured by connecting first conductor (21) containing iron, zinc, magnesium or aluminum and second conductor (22) containing platinum, palladium, nickel, titanium, gold, silver, copper or graphite, immersing in alkali-fusion salt, and reducing water and generating hydrogen gas by supplying water vapor in alkali-fusion salt (8).    USE - Manufacture of hydrogen gas used in energy field.    ADVANTAGE - The method has high hydrogen production rate.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the chemical reaction.    Alkali-fusion salt (8)    First conductor (21)    Second conductor (22)    Electric wire (23)
NOVELTY - Mixture of solution is obtained by fermenting organic substance containing thermophilic microorganism capable of regulating mucous membrane immune system genes and genes related to metabolism in the liver and intestine when administered to animal at 50-90 degrees C. The thermophilic microorganism is Bacillus, Oceanobacillus, Paenibacillus, Anoxybacillus, Lysinibacillus, Methanopyrus, Geogemma, Pyrolobus, Pyrodictium, Geobacillus, Thermomyces, or Clostridium.    USE - The mixture of solution is useful in pharmaceuticals for regulating expression of mucosal immune system gene and metabolic gene of intestine and liver in animal (claimed) and human.    DETAILED DESCRIPTION - Mixture of solution is obtained by fermenting organic substance containing thermophilic microorganism capable of regulating mucous membrane immune system genes and genes related to metabolism in the liver and intestine when administered to animal at 50-90 degrees C. The thermophilic microorganism is chosen from Bacillus, Oceanobacillus, Paenibacillus, Anoxybacillus, Lysinibacillus, Methanopyrus, Geogemma, Pyrolobus, Pyrodictium, Hyperthermus, Pyrococcus, Pyrobaculum, Thermococcus, Aeropyrum, Aquifex, Thermotoga, Thermodesulfobacterium, Thermus, Geobacillus, Thermomyces, and Clostridium.
NOVELTY - Producing renewable multipurpose biomaterial, involves dissociating biomass waste by anaerobic reaction to obtain hydrocarbon and alcohol, dissociating hydrocarbon and alcohol to generate carbon and hydrogen, harvesting carbon dioxide emitted from industrial process, reacting harvested carbon dioxide with hydrogen to generate hydrogen-dense fuel, and dissolving hazardous contaminant in hydrogen-dense fuel utilized as solvent to generate liquid mixture which isolates hazardous contaminant from environment.    USE - The method is useful for producing renewable multipurpose biomaterial used for isolating hazardous contaminant e.g. carbon donor and hydrogen donor from environment and storing energy (claimed). The biomaterial is fuel.    ADVANTAGE - The biomaterial is portable and can be easily stored.    DETAILED DESCRIPTION - Method (M1) of producing a renewable multi-purpose biomaterial, involves dissociating biomass waste by anaerobic reaction to obtain at least one of hydrocarbon and alcohol from waste heat recovered from an external heat source, dissociating at least one of hydrocarbon and alcohol to generate carbon and hydrogen, harvesting carbon dioxide emitted from an industrial process, reacting the harvested carbon dioxide with the hydrogen to generate the hydrogen-dense fuel, and dissolving a hazardous contaminant in the hydrogen-dense fuel utilized as a solvent to generate a liquid mixture which isolates the hazardous contaminant from the environment, where the hazardous contaminant comprises at least one of carbon donor, nitrogen donor and hydrogen donor. An INDEPENDENT CLAIM is included for energy-dense liquid mixture that reduces vapor pressure or availability of vapor pressure of hazardous contaminant, and the liquid mixture.
NOVELTY - Converting plant biomass to a biomass slurry comprises: (a) collecting plant biomass, where overall plant biomass comprises a moisture content between about 70% to about 95%; (b) chopping the plant biomass to produce a chopped plant biomass where the chopping comprises chopping the biomass to a theoretical cut length of less than 1.3 centimeters; (c) inoculating the chopped plant biomass with a ethanol-producing biocatalyst microbe to produce an inoculated chopped plant biomass; (d) placing the inoculated plant biomass into a chamber for at least 12 hours; and (e) providing a biomass slurry.    USE - The method is useful for converting plant biomass to biomass slurry (claimed). Preferably, it can be used for converting bulky lignocellulosic biomass to high density biomass products, including biofuels.    ADVANTAGE - The invention provides improved method for converting biomass to biofuels and/or high density biofuel feedstocks. The method can reduce biomass storage and transport issues, and does not require the use of large amounts of externally provided water.    DETAILED DESCRIPTION - Converting plant biomass to a biomass slurry comprises: (a) collecting plant biomass, where the overall plant biomass comprises a moisture content between about 70% to about 95%; (b) chopping the plant biomass to produce a chopped plant biomass where the chopping comprises chopping the biomass to a theoretical cut length of less than 1.3 centimeters; (c) inoculating the chopped plant biomass with a ethanol-producing biocatalyst microbe to produce an inoculated chopped plant biomass; (d) placing the inoculated plant biomass into a chamber for at least 12 hours, where the inoculated plant biomass maintains a pH of greater than 3.5; and (e) providing a biomass slurry.
NOVELTY - Producing low oxygen biomass-derived pyrolysis oil from carbonaceous biomass feedstock, comprises: pyrolyzing (20) biomass feedstock to produce char and pyrolysis gases comprising oxygenated hydrocarbons and steam, in presence of a steam reforming (30) catalyst to form carbon monoxide, carbon dioxide, and hydrogen gas and to convert a portion of oxygenated hydrocarbons into hydrocarbons by steam reforming, the hydrogen gas at least partially deoxygenating (40) a residual portion of oxygenated hydrocarbons; and condensing (100) a condensable portion of the pyrolysis gases.    USE - The method is useful in producing low oxygen biomass derived pyrolysis oil from carbonaceous biomass feedstock and reducing an oxygen level in condensable pyrolysis gases comprising oxygenated hydrocarbons and steam (all claimed), where the low oxygen biomass derived pyrolysis oil is useful as a biofuel.    ADVANTAGE - The method: provides low oxygen biomass-derived pyrolysis oil having substantially improved energy density, lower corrosivity, and higher thermal stability than conventional biomass-derived pyrolysis oil; provides the low oxygen biomass derived pyrolysis oils which are fully hydrocarbon products making them more suitable for processing into biofuels and chemicals; and potentially eliminates or substantially reduces the severity of secondary upgrading of the oils.    DESCRIPTION OF DRAWING(S) - The figure illustrates a flow chart of method for producing low oxygen biomass-derived pyrolysis oils.    Pyrolyzing carbonaceous biomass feedstock (20)    Steam reforming portion of oxygenated hydrocarbons in the presence of a steam reforming catalyst (30)    Deoxygenating residual portion of the oxygenated hydrocarbons (40)    Producing additional hydrogen gas using a low temperature water-gas shift catalyst (60)    Condensing condensable portion of the pyrolysis gases into low oxygen biomass derived pyrolysis oil (100)
NOVELTY - Household sewage purifying tank comprises quadrate tank body; water inlet provided at the left upper part of the tank body; and water outlet provided at the right lower part of the tank body. The tank body has two partitions, which divide the tank body into three water purifying units, where water flowing holes are provided on each partition, and cobblestones, activated carbon, and filtering ring are filled in the second water purifying unit. Water bamboos are planted on the cobblestones, activated carbon, and filtering ring.    USE - Household sewage purifying tank.    ADVANTAGE - The purifying tank has simple structure and low cost; and beautifies the environment.
NOVELTY - Improving an ecological habitat at the bottom of a surface water comprises directly installing a microorganism carrier and an aeration oxygen-filling device in the water. The aeration oxygen-filling device is a bottom horizontal flow fluidizing and oxygenating device, and the carrier is paved at the bottom. An artificial microorganism preparation or a composite biological enzyme preparation is directly added to the surface water.    USE - Method for improving an ecological habitat at the bottom of a surface water (claimed) for benthic shell organism, e.g. spiral shell and freshwater mussel.    ADVANTAGE - The method oxidizes bottom sludge of the surface water, reduces inner pollution load, and quickly decomposes organic substance deposited at the bottom.
NOVELTY - A system comprises a hydrolysis acidification pond; a lime settling pond connected with a lime dosing device; an anaerobic reactor for removing a majority of chemical oxygen demand (COD) in a wastewater, and drains of generated methane; and an aerobic pond.    USE - A system for treating terramycin wastewater (claimed).    ADVANTAGE - The system allows a stable process and is inexpensive, has small occupying area, and has low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating terramycin wastewater, comprising:    (A) adjusting pH value of the wastewater to adjust pH value of inflowing water to 6.5-7.5, entering a hydrolysis acidification pond, where the wastewater stays for 8-9 hours, utilizing hydrolysis acidification pond to conduct hydrolysis reaction and acidification reaction to degrade macromolecular organic matters such as terramycin in the wastewater to be low molecular organic acid;    (B) transmitting the wastewater to a lime settling pond, where terramycin and calcium ion bond together to form settlement to lower residual of the terramycin and reduce prevention and poison effects on anaerobism, where COD in the wastewater is lowered to 5000-6000 mg/L;    (C) entering an anaerobic reactor, where water is at 35-38 degrees C and at a pH of 6.0-7.5, adding 30-35 g/L high efficiency strains to the anaerobic reactor, removing the COD in the wastewater, and ensuring COD content in the wastewater flowing out from the anaerobic reactor smaller than 1500 mg/L; and    (D) entering an aerobic pond, where organic matters and ammonia nitrogen in the wastewater are further lowered.
NOVELTY - The method involves feeding a solid fuel from top end of pyrolysis reactor of reverse-flow down bed. The fuel is passed through pyrolysis reactor of reverse-flow down bed from up and down. The fuel in fluidifying gas reverse flow is entered from bottom of pyrolysis reactor of reverse-flow down bed and is operated from down to up. The pyrolytic reaction of solid fuel is completed. The fuel is coal, biomass or pyroshale. The radiative transfer and heat convection of fluidifying gas on wall surface of reactor supplies heat required for pyrolytic reaction of solid fuel.    USE - Low-temperature pyrolysis method for solid fuel in pyrolysis reactor of reverse-flow down bed.    ADVANTAGE - The design height of the pyrolysis reactor of the reverse-flow down bed is reduced. The pyrolysis reactor of reverse-flow down bed has low semicoke sulfur content. The tar yield is high. The heat of the pyrolytic gas is increased and the pyrolysis reactor of reverse-flow down bed is operated stably and continuously.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the low-temperature pyrolysis process. (Drawing includes non-English language text)
NOVELTY - The device includes a transmission mechanism. The mechanism comprises a motor arranged on an outer side of the upper portion of a storage bin. A small flywheel which is installed on the same shaft with output end of motor is linked with a big flywheel. A horizontal obliquity of the pneumatic feed pipe alpha is 40-60 degrees. A blade is arranged on the same shaft with the feeding screw rod whose upper end is installed on the same shaft with big fly wheel. The lower end of the rod extends into a pneumatic feed pipe through a cone-shaped outlet of the storage bin.    USE - Biomass precise feeding device for fluid bed.    ADVANTAGE - Precision feeding for biomass is performed with stable feeding process. The feeding process is performed through pneumatic transmission while avoiding advance coking process. The operation condition and the production rate of device are improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass precise feeding device.
NOVELTY - Preparation of methane comprises crushing crop straw to be of any length from 1 mm to 10 mm; mixing the crushed straw with silt of sewage treatment plant; executing heating pre-treatment on the mixture; executing solid and liquid separation on the mixture; and executing anaerobic fermentation on separated liquid.    USE - Method for preparing methane.    ADVANTAGE - The method solves the problem of carbon/nitrogen unbalance during the anaerobic fermentation process; and the anaerobic fermentation speed is largely improved.
NOVELTY - The fermentation device has a net cage conveying device that moves a net cage inside and outside a corridor that is arranged on the corridor. Two pipelines are arranged at the output end of an air guiding tube. One pipe line is connected with a methane collection device while the other one is connected with a methane compression pump. A net cage is correspondingly placed under each one of the gas nozzles that are spaced on an air return tube. A heating tube which is arranged on the upper portion or inner portion inside the corridor receives the hot circulating water.    USE - Net cage plug flow-type fermentation device used in fermentation process of excrement and straw.    ADVANTAGE - The net cage plug flow-type fermentation device is featured with convenience operation, low energy consumption and high gas production rate and is provided with the ability to effectively avoid the blocking and jamming of the corridor and to provide a good anaerobic environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of net cage plug flow-type fermentation device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the net cage plug flow-type fermentation device.
NOVELTY - The system has an upper absorbing type gasifying boiler comprising an auger charging system, a gasifying boiler and a rotary dusting system. The auger charging system and the rotary dusting system are connected with the gasifying boiler through a flange. The auger charging system is located at a charging port of an upper part of the gasifying boiler. The rotary dusting system is located on a bottom part of the gasifying boiler. A high temperature transmitting pipe system is connected with a gas generating port and a fuel spraying port of the boiler through the flange.    USE - Biomass gasifying reburning system for a coal fired boiler.    ADVANTAGE - The system can stably and continuously process the biomass material, and can output the gasified gas for acting as the fuel of the boiler for reburning. The system has low density and scattered distribution of the biomass source in the Country so as to improve the utilization ratio of the biomass, synchronously reduce the emission of the oxynitride, and to avoid the transformation in large scale to the existing device. The system does not damage the utilization of the biomass ash and the coal ash.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass gasifying reburning system.
NOVELTY - The furnace has a valve arranged on a smoke discharging pipe, and a fuel gas purifying box whose gas outlet port is connected with a stove. Purifying cylinders are arranged in the fuel gas purifying box. Lower parts and upper parts of the purifying cylinders are connected in series. A sewage discharging pipe is arranged on a lower end of each purifying cylinder. A sewage discharging valve is installed on a lower end of the sewage discharging pipe. The fuel gas purifying box is filled with cooling water. A water inlet pipe and a water outlet pipe are arranged on the fuel gas purifying box.    USE - Cone type anaerobic gasification furnace.    ADVANTAGE - The upper part of an internal wall of the gasification furnace is small and the lower part is large, so that the firewood is burned without the fault space. The fuel gas purifying box ideally purifies the fuel gas produced by the furnace. The wind emitted by a semi-spherical blowing head is blown in all direction, so that an anaerobic gasification of the firewood is balanced. The furnace feeds the material, and removes ash without stopping the stove.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cone type anaerobic gasification furnace.
NOVELTY - A biomass compact shaping particle fuel is prepared by taking the waste reproducible straw, rice hull, and maize cob as raw materials, pulverizing, mixing, drying, compressing, cooling, sieving, and packaging.    USE - A biomass compact shaping particle fuel.    ADVANTAGE - The biomass compact shaping particle fuel is columnar particles with diameter of 8 mm and length of 10-50 mm. The finished product particle can be obtained after cooling by cooler, sieving, and packaging.
NOVELTY - Preparation of biological oil comprises drying aquatic plant; controlling the water content to less than 15%; conveying the aquatic plant to a microwave reactor; microwave cracking; and separating the product as gas, liquid, and solid.    USE - Preparation of biological oil (claimed) for use as fuel.    ADVANTAGE - The method realizes fast cracking of aquatic plant; produces gas, which is micromolecule substance (hydrogen, carbon monoxide, and methane) and has less short carbon chain hydrocarbon and has good flammability for combustion power supply system; and produces solid, which is used as inorganic fertilizer. Thus, the method utilizes biological substance, which is harmless; and turns waste into valuable products.
NOVELTY - An urban domestic sewage algae treatment padding bed comprises a bed body internally provided with three galleries in its length direction by two separating plates; a water inlet at a bottom part of the first gallery; and a water outlet at an upper part of the third gallery. The three galleries are filled with radial elastic polyethylene padding, where the volume of the padding is 2/3 of the total volume of the bed body.    USE - An urban domestic sewage algae treatment padding bed.    ADVANTAGE - The padding bed uses the radial elastic polyethylene padding which is harmless to algae cells and distributed according to a certain density, makes the alga easily attached, and has good effect of removing nitrogen and phosphor in the urban domestic sewage. The algae are easily harvested.
NOVELTY - Fermentation reactor comprises a gas discharging pipe (1), an adsorbing filler tube (2) and a movable cover (3) fixed together to form the movable cover body, a fermentation warehouse (4) whose bottom end is provided with a gas inlet or gas inlet pipe, and a rotary shaft (5) which penetrates through the middle part of the fermentation warehouse in parallel manner. The two ends of the rotary shaft are connected with a triangular support.    USE - The reactor is useful for composting the domestic waste and in research process studies.    ADVANTAGE - The reactor: can be utilized as the mobile sanitation facility; realizes several compost models of aerobic, anaerobic, static or dynamic; and removes the odor produced in the fermentation process by using the adsorbing filler tube.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the fermentation reactor.    Gas discharging pipe (1)    Adsorbing filler tube (2)    Movable cover (3)    Fermentation warehouse (4)    Rotary shaft (5)
NOVELTY - Biomass bio-gas purifying system comprises a gas collecting kettle connected with a desulfurizing tower, which is connected with a decarbonization adsorption device. The tail end of a gas outlet pipe of decarbonization adsorption device is connected with a methane collector. A siloxane removing device, a halogenated hydrocarbon remover, a drying tower and a nitrogen and oxygen remover are connected in parallel on the gas outlet pipe between decarbonization adsorption device and the methane collector. The pipe of the halogenated hydrocarbon remover is connected with a gas compressing device.    USE - Used as a biomass bio-gas purifying system.    ADVANTAGE - The system: has methane with high concentration after gas processing; can work continuously with high purification efficiency; and utilizes removal agent that can be easily obtained and has low cost. The device: has simple structure that can be operated easily; can be removed by stages and utilized in modularization; and has good flexibility and adaptability.    DETAILED DESCRIPTION - Biomass bio-gas purifying system comprises a gas collecting kettle connected with a desulfurizing tower, which is connected with a decarbonization adsorption device. The tail end of a gas outlet pipe of the decarbonization adsorption device is connected with a methane collector. A siloxane removing device, a halogenated hydrocarbon remover, a drying tower and a nitrogen and oxygen remover are connected in parallel on the gas outlet pipe between the decarbonization adsorption device and the methane collector. The pipe of the halogenated hydrocarbon remover is connected with a gas compressing device in series, and the pipes among the devices in parallel are respectively provided with a control valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass bio-gas purifying system.
NOVELTY - The system has an integrated treating device of anaerobe and aerobe, which is made of reinforced steel cement. A septic tank group, a grid, a water collecting well, the integrated treating device, an ecological wetland system and a plant ecological system are connected with each other through a pipeline.    USE - Ecological treating system for treating domestic sewage.    ADVANTAGE - The ecological treating system is capable of efficiently treating the sewage discharged from the residential places, and improving the comprehensive usage of treated water. The whole sewage treating system is environmental-friendly with low carbon emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of ecological treating system. (Drawing includes non-English language text)
NOVELTY - The multifunctional fluidized bed type biomass pyrolysis conversion device has a lower section at a right side which is provided with a circulation water inlet while an upper section at the right side is provided with a circulation water outlet. A gas outlet at the upper section of the left side is connected with a gas storage tank. The gas storage tank is configured for storing the non-condensed gas obtained after rinsing and decoking of the rinsing decoking device. The inlet of the gas storage tank is connected with the gas outlet of the rinsing decoking device.    USE - Multifunctional fluidized bed type biomass pyrolysis conversion device for use as biomass recycling and energy equipment.    ADVANTAGE - Performs segmental temperature control to fluidized bed reactor to realize pyrolysis carbonization, liquefaction or gasification of biomass. Improves quality of pyrolysis product and suppresses pollution of biomass conversion to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional fluidized bed type biomass pyrolysis conversion device.
NOVELTY - A biomass reducing agent comprises (mass%) biomass charcoal (7-40) dry-distilled at 500 degrees C, biomass charcoal (20-25) dry-distilled at 600 degrees C, biomass charcoal (15-25) dry-distilled at 700 degrees C, biomass charcoal (10-23)l dry-distilled at 850 degrees C, biomass charcoal (10-20) dry-distilled at 900 degrees C, and binder (5-8).    USE - A biomass reducing agent.    ADVANTAGE - The agent overcomes relay of two industries on charcoal and coke; enlarges utilization ratio of regenerative resources; utilizes agricultural thus reducing pollution; has little sulfur, nitrogen and dust; does not increase carbon dioxide in the atmosphere; releases the worse greenhouse effect; reduces the fossil fuel consumption; and protects the human living environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass reducing agent comprising mixing biomass charcoal materials, shaping the mixture, and drying.
NOVELTY - An ethoxymethoxyl methane is used as methanol gasoline solubilizer.    USE - Ethoxymethoxyl methane is used as methanol gasoline solubilizer (claimed).    ADVANTAGE - The ethoxymethoxyl methane has good solubilizing effect for methanol gasoline and does not influence use of gasoline. The methanol gasoline added with ethoxymethoxyl methane solubilizer can be used in any natural environment in which the gasoline can be used.
NOVELTY - The increasing device has condensing pots which are connected with the vent of reaction kettle through an exhaust pipeline. The condensing pot is provided with a control valve, condensing liquid outlet, air outlet, and condensing jacket. A cryogenic freezer is arranged out of the condensing pot.    USE - Increasing device for productivity and cooling speed of reaction kettle.    ADVANTAGE - Increases the biological oil liquefaction rate and cooling speed of biological materials during the process of liquefaction under subcritical/supercritical condition in reaction kettle at high temperature and high pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an increasing device for productivity and cooling speed of reaction kettle.
NOVELTY - The device has a fluidized bed reactor whose upper portion is connected with an inlet end of a gas-solid separator. The gas outlet end of gas-solid separator is connected with the inlet end of a condenser. The gas outlet end of condenser is connected with the inlet end of a cyclone hydraulic separator whose gas outlet end at upper portion is connected with inlet end of an electrostatic dust collector. The outlet end of dust collector is connected with a gas distributor through a fan. A cold air pipeline of a heat exchanger is connected with condenser in parallel.    USE - Device for preparing biological oil through thermo-chemical conversion of waste artificial board.    ADVANTAGE - 70-80% of the nitrogen-included compound generated by pyrolyzation of artificial board can be effectively removed. The side effect of the rapid pyrolyzation product of artificial board is greatly reduced. The device is featured with compact structure, high efficiency and low biological oil manufacture cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing biological oil through thermo-chemical conversion of waste artificial board. (Drawing includes non-English language text)
NOVELTY - The feeder has jacket, and a chamber for putting molten salt pyrolysis biomass reaction device which is installed in the jacket. A stirring shaft is installed in the chamber, and connected with the output shaft of motor. The motor is installed on the jacket, and a stirring blade is installed on the stirring shaft. The stirring blades are installed on the stirring shaft, and a baffle is sleeved on the stirring shaft between the stirring blades.    USE - Feeder for molten salt pyrolysis biomass reaction device.    ADVANTAGE - Provides feeder which is easy and uniform to feed material, effectively reduces the heating during feeding, and satisfies the oxygen-free or oxygen-lack condition.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a feeder for molten salt pyrolysis biomass reaction device.
NOVELTY - The method involves fermenting vegetable, fruit and garden waste, adding the vegetable, fruit and the garden waste with partially fermented waste, and composting the mixture of the fermented waste and compost.    USE - Method for treating organic and biodegradable waste such as vegetable, fruit and garden waste e.g. plants, flowers, wood, leaves and grass from a food industry, a catering industry and an industrial scale greenhouse. Uses include but are not limited to kitchen waste, leftovers from meals, coffee grounds, paper, cardboard and egg shells, garden waste, animal faces and animal derived waste such as meat and animal fat.    ADVANTAGE - The method avoids the formation of biogas, methane and carbon dioxide during the fermentation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of the method for treating organic and biodegradable waste.    Fermentor (2)    Composting unit (3)    Storage unit (8)    Upgrading unit (13)    Supply unit (33)
NOVELTY - A methanol gasoline denaturing agent comprises methanol gasoline phase separation inhibitor, methanol gasoline corrosion inhibitor, methanol gasoline vapor pressure regulator, formic acid, methyl aldehyde and methyl alcohol complete combustion improver. The methanol gasoline corrosion inhibitor is 1-10 wt.% and comprises mixture of ester compound, nitrogenous compounds and poly oleic acid.    USE - A methanol gasoline denaturing agent.    ADVANTAGE - The denaturing agent has long-term storage and provides normal use of methanol gasoline.    DETAILED DESCRIPTION - Methanol gasoline denaturing agent comprises methanol gasoline phase separation inhibitor, methanol gasoline corrosion inhibitor, methanol gasoline vapor pressure regulator, formic acid, methyl aldehyde and methyl alcohol complete combustion improver. The methanol gasoline corrosion inhibitor is 1-10 wt.% and comprises ester compound, nitrogenous compounds and poly oleic acid. The ester compound is dioctyl phthalate, dibutyl phthalate, epoxy oleic acid and epoxy butyl oleate. The nitrogenous compound is benzotriazole, triethanolamine and oleic acid triol amine salt. The poly oleic acid is dimerization oleic acid or trimerization oleic acid. The complete combustion improver is 8-18C amine, butyl caproate and propyl valerate. An INDEPENDENT CLAIM is included for preparation of methanol gasoline denaturing agent, comprising adding each component in reaction tank; and at 70-80 degrees C, sealing, stirring and reacting for 1-3 hours.
NOVELTY - A (4R)-4-methyl-2-carbonyl valeric ester derivative of formula (I), is new.    USE - Compound (I) for synthesizing (2S)-2-methyl-1-propionaldehyde compound (claimed).    ADVANTAGE - The compound has simple preparation method, requires less usage of steroid sapogenin as raw materials, and reduces pollution.    DETAILED DESCRIPTION - A (4R)-4-methyl-2-carbonyl valeric ester derivative of formula (I), is new.    R1=O-benzyl, O-p-methyl-benzyl, O-2-nitrobenzyl, O-p-nitrobenzyl, O-2,4,6-trimethylbenzyl, O-2,4-dimethoxy benzyl or O-3, 4-dimethoxy benzyl;and    R2=1-3C alkyl.    INDEPENDENT CLAIMS are included for:    (1) preparation of (I); and    (2) use of (4R)-4-methyl-2-carbonyl valeric ester in synthesis of (2S)-2-methyl-1-propionaldehyde compound comprising mixing non-protonic solvent A and organic alkali, adding compound (I) and carbonyl protecting agent, reacting at 0 degrees C to room temperature for 1-5 hours, adding ozone, reacting in the presence of non-protonic solvent A and/or alcohol solvent and organic alkali to obtain blue solution of formula (IV), adding dimethyl sulfide, reacting at room temperature for 1-2 hours, stirring for 3-6 hours.    R3=O-trimethyl silica, O-triethyl silica or O-dimethyl tertiary butyl silica.
NOVELTY - Preparing geraniin, by immersing fresh meadow cranesbill stems and leaves in water, squeezing material, filtering obtained product, allowing activated carbon column to adsorb, eluting column, collecting eluent, recycling ethanol, condensing eluent, allowing absorption resin column to adsorb condensate, eluting column, collecting eluent, recycling ethanol, condensing eluent, adding methanol crystal to eluent, separating crystal, washing crystal, and drying crystal to obtain the final product.    USE - The method is useful for preparing geraniin.    ADVANTAGE - The method is simple and environmentally-friendly, and consumes less energy. The geraniin has high purity, and is easy to realize and suitable for industrial production.    DETAILED DESCRIPTION - Method for preparing geraniin, involves immersing fresh meadow cranesbill stems and leaves in water (8-12 times) for 18-36 hours, squeezing the material, filtering the obtained product, allowing activated carbon column to adsorb, eluting the column using 75-85% ethanol, collecting eluent (3-8 times with respect to mass of the column), recycling the ethanol, condensing the eluent, allowing absorption resin column having large holes to adsorb the condensate, eluting the column using 50-70% ethanol, collecting the eluent (3-8 times with respect to mass of the column), recycling the ethanol, condensing the eluent, adding methanol crystal to the eluent, separating the crystal, washing the crystal, and drying the crystal to obtain the final product.
NOVELTY - Recycling carbon to produce a renewable fuel, comprises (a) harvesting carbon dioxide (110) emitted from an industrial process, (b) dissociating a biomass waste under an anaerobic reaction to produce hydrogen, and (c) reacting the harvested carbon dioxide with the biomass waste produced hydrogen under pressure and heat to generate a renewable fuel.    USE - The method is useful for producing a renewable fuel (claimed) including methanol fuel.    ADVANTAGE - The method is simple and reduces fuel production cost by avoiding the equipment and energy expenses required to produce and store water-free fuels.    DETAILED DESCRIPTION - Recycling carbon to produce a renewable fuel, comprises: either (a) harvesting carbon dioxide (110) emitted from an industrial process, (b) dissociating a biomass waste under an anaerobic reaction to produce hydrogen, and (c) reacting the harvested carbon dioxide with the biomass waste produced hydrogen under pressure and heat to generate a renewable fuel; or step (a) as above per se, (b1) dissociating a biomass waste under an anaerobic process to produce carbon monoxide, one or more carbon donors and hydrogen, (c1) generating thermochemically shifted carbon monoxide and additional hydrogen by reacting the harvested carbon dioxide with the biomass waste produced carbon donors, and (d1) reacting the produced carbon monoxide (130) and the thermochemically shifted carbon monoxide with the produced hydrogen and the additional hydrogen under pressure and heat to generate a renewable fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a process flow diagram of a method for reinvesting, repurposing or recycling carbon dioxide.    Harvesting a carbon dioxide (110)    Harvesting hydrogen from biomass waste dissociation (120)    Reacting carbon dioxide with biomass produced hydrogen (130)    Adding catalyst to the reaction to enhance hydrogen-dense fuel mixture. (140)
NOVELTY - Obtaining transesterified lipids/fatty acid alkyl or methyl esters from biological material comprises: reacting the biological material with an alcohol and an acid; and incubating the mixture, where the steps result in the formation of at least two phases, in which the first phase comprises transesterified lipids/fatty acid alkyl or methyl esters and the second phase comprises an acidified alcohol solution.    USE - The method is useful for obtaining transesterified lipids/fatty acid alkyl or methyl esters from biological material. The transesterified lipids are useful to produce: a fuel-grade biodiesel product; a product of an omega fatty acid, a carotenoid, a sterol or a wax; a co-product, which is a protein-rich animal feed, a feedstock for aerobic or anaerobic fermentation, a food additive, or a bio-based material or composite (all claimed), where the transesterified lipids are useful as biodiesel and nutritional products, including polyunsaturated fatty acids such as omega-3 or -6 fatty acids.    ADVANTAGE - The process provides the transesterified lipid products as high purity lipids, without further solvent extraction or distillation. The process is cost effective through the reduction in equipment size and the high throughput.
NOVELTY - The method involves injecting and boiling molded separator for fuel cells into the pure wash water stored in the chamber of pressure cooker apparatus, in the state more than direct pressure. Heat powder molding of separator is carried out at the board of planar rectangle with the molding material containing powdered electro-conductive material and thermoplastic resin.    USE - Method for processing fuel cell separator.    ADVANTAGE - Since fuel cell separator is injected and boiled into the pure wash water of pressure cooker apparatus in the state more than direct pressure, ionic substance and impurity can be removed effectively from the fuel cell separator and the electro-conductivity of the fuel cell separator can be improved.
NOVELTY - The product has biological enzymes having main constituents such as amylase, cellulose, beta-glucanase, glucose oxidase, lipase, maltase, mannose, pectinase, phytase, protease, xylanase and galactomannan enzyme. The biological enzymes and proteins are provided with unique biodegradation and function of promoting beneficial germ propagation. Optimal reaction process dissolves organic matter waste product into methane, water, carbon dioxide and energy. Fetor pollution generated from rubbish and excrement is controlled radically.    USE - Biological complex enzyme deodorizing product. Uses include but are not limited to a sewage treatment plant, a city excrement treatment plant, a house refuse treatment plant, a livestock farm, an animal husbandry and a public toilet.    ADVANTAGE - The product deodorizes city environment, and is environmental-friendly.
NOVELTY - An animal waste solar medium-temperature methane gas generating thermoelectric and cogeneration device comprises a spot source-surface source animal waste gathering and pre-treating system, an anaerobic digestion system, a solar heat gathering system, a medium-temperature methane gas generating system, an aerobic water processing system, a methane gas purifying system device, a purified methane gas generating system, and a methane liquid and methane slag recycling organic fertilizer generating system.    USE - An animal waste solar medium-temperature methane gas generating thermoelectric and cogeneration device.    ADVANTAGE - The device improves methane gas generating rate, and improves efficiency of the system integration.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the device.    Ditch (1)    Grid sediment pool (2)    Natural composting system (3)    Regulating pool (4)    Stirrer (5)
NOVELTY - Separated lipase comprising fully defined 325 amino acids (SEQ ID NO: 4) as given in the specification, is new.    USE - The lipase is useful for: converting plant oil into bio-diesel; the catalytic synthesis of ester, where the esterification reaction is catalyzed in water-free or less-water system; carrying out catalytic chiral resolution (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a nucleic acid molecule coding the lipase;    (2) a vector comprising the nucleic acid;    (3) a cell comprising a vector or a gene integrated with the nucleic acid;    (4) a composition comprising the lipase and the vector; and    (5) producing the lipase.
NOVELTY - The fuel-cell wind mill has a hydrogen generator whose outlet is connected with the air inlet of the fuel cell stack trough an air duct. The electrode of the fuel cell stack is connected with the input electrode of motor through a conductor. The fuel stack is composed of membrane electrode assembly having proton exchange membrane made of perfluorinated sulfuric acid resin.    USE - Fuel-cell windmill.    ADVANTAGE - The fuel-cell windmill can be designed in simple structure and the windmill can be operated easily. The working principle of the fuel cell can be demonstrated efficiently, and the windmill can be used as high-tech toy effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the fuel-cell windmill.
NOVELTY - Poly L-aspartic acid (PASP) high-efficiency environment-friendly urea prepared by adding polyaspartic acid and other microelements into normal urea in specific proportion, is claimed.    USE - Used as poly L-aspartic acid high-efficiency environment-friendly urea.    ADVANTAGE - The urea: solidifies sand, conserves water, promotes the development of root system of crops, improves the effect of fertilizer, is simple and environment-friendly, and has high fertilizer utilization ratio and does not loss soil and water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the PASP high-efficiency environment-friendly urea, comprising: (i) adding aspartic acid into a polymerizing kettle and polymerizing into an amber polyaspartic acid by solid phase reaction under the presence of a catalyst and the absence of a solvent; (ii) dehydrating the amber polyaspartic acid by a centrifuging machine and hydrolyzing to obtain a polyaspartic acid solution; (iii) adding polyaspartic acid solution, solid zinc chloride, ferrous sulfate, potassium sulfate and boric acid into a mixing tank, and stirring by a steam bubbling to fully mix; and (iv) pumping the mixed material into a urine pumping port by a high-pressure metering pump, and pumping into a pelleting tower sprayer to form a fog form mixture to obtain the product in particle form.
NOVELTY - Organic nutrient solution is prepared using (in parts weight): biogas (70-85), low-rank coal (10-20), stalk (0-5) and Bacillus culture liquid (5-10). The biogas is a liquid having solid content of 1% or less. The biogas is produced during anaerobic fermentation of dairy manure, pig manure or mixed dairy manure and pig manure.    USE - The organic nutrient solution is useful as growth regulator for promoting the development of root systems and stimulating the growth of plants.    ADVANTAGE - The prepared solution is environmentally-friendly, portable and highly nutritious, has excellent storage stability, and promotes photosynthesis. The method is simple.    DETAILED DESCRIPTION - Organic nutrient solution is prepared using (in parts weight): biogas (70-85), low-rank coal (10-20), stalk (0-5) and Bacillus culture liquid (5-10). The biogas is a liquid having solid content of 1% or less. The biogas is produced during anaerobic fermentation of dairy manure, pig manure or mixed dairy manure and pig manure. The Bacillus culture liquid is prepared by inoculating Bacillus strain into a kettle by existing method, culturing the strain for 12-24 hours, and inoculating the strain into a fermentation container for performing fermentation for 12-24 hours, where concentration of the bacteria is 1-2x 108 colony forming units/ml. An INDEPENDENT CLAIM is included for method for preparing the above-cited solution, which involves mixing biogas, low rank coal or humic acid and stalk, adding the mixture in a fermentation pond, inoculating Bacillus culture liquid, stirring the mixture uniformly, and fermenting the mixture at 25-28 degrees C to obtain the product.
NOVELTY - Fish protein organic fertilizer comprises (in parts by weight) abyssal fishes (300), Saccharomyces cerevisiae (5), copper sulfate (50), zinc sulfate (50), ferrous sulfate (30), manganese sulfate (30), molybdenum salt (24), ethylenediaminetetraacetic acid (2), bio fulvic acid (80), magnesium chloride (36) and water (900).    USE - Used as a fish protein organic fertilizer.    ADVANTAGE - The fertilizer: is rich in various kinds of microelements; improves soil and soil-water permeability; promotes the aggregation and prevents hardening of the soil, and thus the fertilizer is suitable for vegetables, fruit trees and field crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fish protein organic fertilizer, comprising (i) preparing the abyssal fishes into a slurry, adding into a fermenting tank, adding water, stirring, sterilizing for 30 minutes at 103-110 degrees C, lowering the temperature to 35 plus minus 5 degrees C, adding Saccharomyces cerevisiae at 35 plus minus 5 degrees C, performing oxygen-enriched fermentation for 8-12 hours and reserving; (ii) adding copper sulfate, zinc sulfate, ferrous sulfate, manganese sulfate, ethylenediaminetetraacetic acid and molybdenum salt into the fermenting tank of the step (i), stirring for 1.5-3 hours for reacting at 55-60 degrees C; (iii) adding bio fulvic acid into the fermenting tank of the step (ii), stirring for 1.5-3 hours at 55-60 degrees C; and (iv) centrifugally separating, collecting the filtrate and filling to obtain the product.
NOVELTY - Multifunctional biological organic fertilizer (C1) comprises (%) animal hoof and horn (15-50), tobacco straw (45-80), bone powder (2-5), and trace element (0.1-1). The fineness of fermented tobacco straw is 60-80 mesh; and the fineness of bone powder is 60-80 mesh.    USE - Fertilizer (C1) with stress resistance and parasite expelling property (claimed).    ADVANTAGE - The fertilizer (C1) has stable and long-lasting performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer (C1) comprising:    (A) preparing the amino acid raw liquor by crushing dry and clean animal hoof and horn; adding an amount of acid and water; adjusting pH at 5.5-6; completely hydrolyzing at 60-140 degrees C and 0.40-3.9 kg/cm2 for 24-48 hours; and obtaining animal hoof and horn hydrolysate; and    (B) cooling the completely hydrolyzed raw material at 0-40 degrees C; concentrating under vacuum environment; concentrating into 1.0-2.0 times the animal hoof and horn hydrolysate; neutralizing, settling, filtering, and obtaining amino acid raw liquor; crushing tobacco straw; mixing with fermentation strain, which is the beneficial bacterium for accelerating the growth of plant; fermenting; drying; grinding the tobacco straw until the fineness of 60-80 mesh; mixing amino acid raw liquor with tobacco straw; adding bone powder and trace element while mixing; and drying to obtain fertilizer (C1).
NOVELTY - Production of a fatty acid methyl ester (biodiesel) comprises adding absolute alcohol liquid and acid catalyst to a pre-processed kitchen waste oil and fat, heating, stewing, and layering; separating fatty acid methyl ester and oil and fat mixture, adding base metal carbonate solution, washing and separating, and dewatering at 105 plus minus 5 degrees C; and adding absolute alcohol liquid and a base catalyst to the washed fatty acid methyl ester, oil and fat and few acid catalyst mixture, reacting, stewing and separating the catalyst, and decompressing and distilling.    USE - Method for the production of fatty acid methyl ester (claimed).    DETAILED DESCRIPTION - Production of a fatty acid methyl ester (biodiesel) comprises:    (A) adding absolute alcohol liquid and acid catalyst to a pre-processed kitchen waste oil and fat, heating, stirring and back flowing, stewing, and layering, where the lower layer is the glycerin alcohol mixture and the upper layer is the intermediate product, that is fatty acid methyl ester, oil and fat, and few acid catalyst mixture;    (B) separating the fatty acid methyl ester and the oil and fat mixture, adding base metal carbonate solution, washing and separating, and dewatering at 105 plus minus 5 degrees C; and    (C) adding absolute alcohol liquid and a base catalyst to the washed fatty acid methyl ester, oil and fat and few acid catalyst mixture, reacting, stewing and separating the catalyst, where the lower layer is the glycerin alcohol mixture and the upper layer is the fatty acid methyl ester, and decompressing and distilling.
NOVELTY - Ibuprofen is synthesized by using 1-bromo-4-isobutyl benzene and acetate salt derivative as raw material, and performing palladium catalysis decarboxylation coupling reaction, methylation reaction, and hydrolysis reaction.    USE - Method for synthesizing ibuprofen (claimed).    ADVANTAGE - The synthesizing method is simple and easy to operate. The raw material source is wide and its cost is low. In the synthesis production, only inorganic salt and carbon dioxide are produced. The method is safe and environment-friendly, and meets green chemical requirement.    DETAILED DESCRIPTION - Synthesis of ibuprofen involves dissolving 1-bromo-4-isobutyl benzene and compound of formula NC-CH(Me)-COOM (I) in a solvent, generating decarboxylation coupling reaction to obtain a compound of formula (II) under catalysis of palladium catalytic agent and organophosphorus ligand, and hydrolyzing compound (II) to generate ibuprofen.    M=alkali metal or alkaline-earth metal.
NOVELTY - Sealed and safe connector is for arch cover of biogas pool, where the biogas pool includes a tee pipe fitting, a locking cover and a pressure relief sealing cover, and one end of the tee pipe fitting is provided with a projection, and the end is connected with gas outlet of arch cover and thread connected with the locking cover.    USE - The sealed and safe connector is useful for arch cover of biogas pool (claimed).    ADVANTAGE - If the connector is used, there will be good sealed connecting performance between the connector and the arch cover. Moreover, opening the sealed and safe connector can balance the gas pressure between the pool and external air, which is beneficial to discharge residual methane in the pool and facilitates the operator to enter into the pool from feed inlet or discharge outlet in order to clean the pool even if the arch cover had never been opened.    DETAILED DESCRIPTION - Sealed and safe connector is for arch cover of biogas pool, where the biogas pool includes a tee pipe fitting, a locking cover and a pressure relief sealing cover, and one end of the tee pipe fitting is provided with a projection, and the end is connected with gas outlet of arch cover and thread connected with the locking cover; a sealing gasket located in inner wall of the arch cover is mounted between the locking cover and the projection; another end of the tee pipe fitting is connected with the pressure relief sealing cover; the third end of the tee pipe fitting is connected with the pipe of gas-consuming device; and the internal of the locking cover is hollow.
NOVELTY - Catalytic nanoparticles (30) comprise porous palladium, palladium-metal or platinum-metal core (32), and atomic thin layer (34) of platinum atoms on core. The metal is chosen from gold, iridium, osmium, palladium, rhenium, rhodium and ruthenium.    USE - Catalytic nanoparticles are used as electrocatalyst for fuel cell for producing electrical energy.    ADVANTAGE - The catalytic nanoparticles are economical, and provide fuel cell with excellent workability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for forming catalytic structure.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of catalytic nanoparticles.    Catalytic nanoparticles (30)    Core (32)    Platinum monolayer (34)
NOVELTY - Catalytic nanoparticles (30) comprise a porous, hollow palladium, palladium-M or platinum-M core, where M is gold, iridium, osmium, palladium, rhenium, rhodium and ruthenium, and an atomically thin layer of platinum atoms on the core.    USE - Catalytic nanoparticles for use as an electrocatalyst in a hydrogen fuel cell to produce electrical energy.    ADVANTAGE - The catalytic nanoparticles improve fuel cell performance when the surface area of platinum nanoparticles is increased by increasing the loading of platinum. The core-shell structure of nanoparticles improves the durability of the catalytic nanoparticles. The core-shell structure of catalytic nanoparticles reduces costs because the high cost platinum is limited to the surface of catalytic nanoparticles while core is formed from less expensive palladium or palladium-M.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for forming a catalytic structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of catalytic nanoparticles.    Catalytic nanoparticles (30)    Hollow core (32)    Platinum atoms (34)
NOVELTY - The energy processing system has feeding device, bag crushing and massive separating device, screening device, magnetic separating device, winnowing device, refuse derived fuel raw material pre-treating device, hot extrusion forming device and anaerobic fermentation processing system which are orderly connected via conveying device. The anaerobic fermentation processing system is connected with the screening device via the conveying device.    USE - Energy processing system for processing municipal solid waste and domestic garbage.    ADVANTAGE - The treatment of municipal solid waste can be transformed into engineering and scale integral treatment so as to improve the energy processing utilization rate of the municipal solid waste, and reduce the operation cost. Hence, the comprehensive benefit can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of energy processing system.
NOVELTY - A compound (C) containing silicon hydride groups is contacted with phosphorus-type catalyst (I) or polymer-supported catalyst (II), in presence of base in water as solvent to obtain hydrogen and byproduct (C1).    USE - Manufacture of hydrogen used as fuel for vehicles.    ADVANTAGE - The method economically provides hydrogen with excellent safety.    DETAILED DESCRIPTION - A compound (C) containing one or more silicon hydride groups is contacted with phosphorus-type catalyst of formula: X1X2X3P(=O) (I) or polymer-supported catalyst of formula: RaRb(P=O)- (II), in presence of base in water as solvent to obtain hydrogen and byproduct (C1).    X1,X2=1-6C alkyl, 1-6C alkoxy, NRaRb, 6-10C aryl, aralkyl or 5-7 membered heteroaryl, in which alkyl or aryl are optionally substituted by 1-3 Rc;    or X1+X2+P=3-10 membered heterocycloalkyl optionally substituted by Rd;    X3=1-6C alkyl, 1-6C alkoxy, NRaRb, 6-10C aryl, aralkyl, 5-7 membered heteroaryl or -L-P(=O)X1X2;    L=1-6C alkylene or 6-10C arylene;    Ra,Rb= 1-6C alkyl or 6-10C aryl;    or Ra+Rb+P=heterocyclyl optionally substituted by 1-3 Re;and    Rc,Rd,Re=Cl, Br, I, F, OH, 1-6C alkyl, 1-6C alkoxy, NO2, NH2, CN or COOH.    INDEPENDENT CLAIMS are included for the following:    (1) composition, which contains compound (C), phosphorus-type catalyst, base and water; and    (2) device for manufacturing hydrogen, which has reaction chamber containing reaction mixture inlet, hydrogen outlet and byproduct collector. The surface of the device is contacted with the mixture, and coated with polymer supported catalyst.
NOVELTY - Producing a biobased gamma-butyrolactone (GBL) product comprises (a) combining a genetically engineered biomass comprising poly-4-hydroxybutyrate and a catalyst; and (b) heating the biomass with the catalyst to convert the poly 4-hydroxybutyrate to a GBL product.    USE - The method is used for producing a biobased GBL product (claimed).    ADVANTAGE - The present invention provides new GBL manufacturing processes that address not only improvements in the yield, purity, and cost of the product but also use sustainable starting materials that have a more positive impact on the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a biobased GBL product produced by the process above; and    (2) a poly-4-hydroxybutyrate biomass produced from renewable resources which is suitable as a feedstock for producing GBL product, where the level of poly-4-hydroxybutyrate in the biomass is greater than 50% by weight of the biomass.
NOVELTY - The method involves acquiring a key and an amount of electrical energy. A digital signature is generated based on the amount of electrical energy and the key. A certificate comprising the digital signature and the amount of electrical energy is generated. The electrical energy is generated from renewable energy or environmentally friendly resources.    USE - Method for authenticating characteristics of green electrical energy for home power network. Can also be used in wind energy generation, geothermal energy generation, hydro energy generation, atomic energy generation, biomass energy generation, natural gas generation and fuel cell generation.    ADVANTAGE - By using the certificate of electric-generation, the electric-generation capacity generated by green electric energy generation can be increased and electricity can be sold at green energy price when selling electricity along with green certificate. Thus when green certificate changes the trading price, the green certificate can be provided with high monetary value and green certificate can be treated as marketable security. The value of green generation can be widespread to the electric energy consumers and electric energy generation can be replaced by fossil fuels. Thus the green energy generation hinders the decline of the global environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for green power generation apparatus for authenticating characteristics of green electrical energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the green power generation apparatus.    Certificate authority (4)    Green power generation apparatus (11)    Photovoltaic panel (111)    Electric-generation capacity measurement unit (112)    Communication unit (115)
NOVELTY - A cathode for hydrogen evolution with a catalyst layer formed on the cathode substrate, comprises (mol.%): at least, three elements of platinum (5-90), cerium (5-55) and palladium (5-65), as essential element, in a state of metal, metal oxide, or hydroxide.    USE - As cathode for hydrogen evolution with a catalyst layer formed on the cathode substrate (claimed), used in industrial electrolysis, including chlor-alkali electrolysis.    ADVANTAGE - The activated hydrogen evolving cathode for chlor-alkali electrolysis is superior in electrolysis properties, enabling a long-time stable operation with hydrogen overvoltage maintained at less than or equal to 90 mV when operated at a current density of 5 kA/m2, keeping a high remaining rate of the catalyst element after a cease of operation for a short-circuiting and after an electrolysis operation at a high current density, restricting catalyst loss, and having a strong resistance to contamination by electrolytic impurity elements. If the catalyst layer comprises at least two layers having an under catalytic coating layer formed on the cathode substrate surface and a top catalytic coating layer formed on the under catalytic coating layer, and almost all quantity of palladium element is impregnated in the top catalytic coating layer, the catalyst remaining rate after the short-circuiting shut-down test increases, and the property of shut-down resistance can be enhanced.
NOVELTY - Composition comprises (a) culture supernatant of microbial cell capable of expressing at least one of xynR gene and fatty acid elongase (fae) gene, or (b) protein comprising one of 7 (225-379) amino acid sequences (SEQ ID NOs: 8-14) all fully defined in the specification. The composition is capable of stimulating saccharification process of biomass using cellulase.    USE - The composition is useful for stimulating saccharification of biomass which is useful for producing chemical product raw material chosen from fuel alcohol, preferably ethanol and organic acid.    ADVANTAGE - The method is environmentally-friendly, and does not required large amount of enzyme.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) saccharification processing agent comprising the above-mentioned composition and cellulase; and    (2) method of saccharifying biomass, involves processing the biomass using the above-mentioned agent.
NOVELTY - A compost raw material is fermented using a fermenter having an upper portion with an insertion opening (11) and an exhaust port (13) of composed raw material, and lower air supply portion (21,24,25) to obtain compost. The ventilation from top air supply portion (12) is provided On the upper portion of fermenter.    USE - Manufacture of compost from compost raw material e.g. home garbage, industrial vegetable waste, marine product waste, agricultural product refuse, and sludge generated by dehydration of sewage, human waste treatment plant and farm village colony wastewater treatment.    ADVANTAGE - The method enables efficient manufacture of compost under aerobic atmosphere, by preventing dew condensation inside the manufacturing apparatus. The moisture content of compost raw material is reduced, and fermentation heat cycle is maintained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (100) for manufacturing compost.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the apparatus for manufacturing compost.    Insertion opening (11)    Top air supply portion (12)    Exhaust port (13)    Lower air supply portions (21,24,25)    Apparatus for manufacturing compost (100)
NOVELTY - The gasifier a gas storage barrel (2) connected with a combustion furnace (1) and a gas using end part (3) via pipelines, respectively. A fan (4) is connected with the furnace. A pipeline of the furnace is utilized for connecting with the gas using end part. A furnace is provided with a charging hopper (11). The charging hopper is arranged with a sealed device i.e. valve (12). Area of the valve is greater than area of an inlet of the charging hopper. The valve is provided with a handle (13). A lower part of the gas storage barrel is provided with a water discharging pipe (21).    USE - Straw gasifier.    ADVANTAGE - The gasifier improves flowing speed of the gas in each pipeline via function of the fan. The gas using end part of the gasifier has strong gas activity function. The gasifier improves the flowing speed of the gas in the pipeline. The valve of the gasifier can stop discharge of polluted smoke and dust generated by a burning process. The gasifier is simple in structure, utilized in various occasions and wide in application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw gasifier.    Combustion furnace (1)    Gas storage barrel (2)    Gas using end part (3)    Fan (4)    Charging hopper (11)    Valve (12)    Handle (13)    Water discharging pipe (21)
NOVELTY - The system has a feed unit (1) with helical feeding devices (11,32) and an air transporting system (33), a pyrolytic reaction unit (2) with a pyrolytic reaction section (21), a discharge unit (3) and a pyrolytic reaction control system (4). The helical blade of the feeding device changes in density. A helical propulsion device (22) and an air supply device (23) are arranged in the pyrolytic reaction section.    USE - System for preparing biomass gas and biomass charcoal.    ADVANTAGE - The system accurately controls and integrates the material height, material propulsive speed, temperature and intensity of pyrolytic reaction and improves the pyrolytic efficiency. The biomass gas and biomass charcoal prepared by the system are good and stable in quality. The system is capable of processing wide biomass and organic waste and high automatic level.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for preparing biomass gas and biomass charcoal.    Feed unit (1)    Pyrolytic reaction unit (2)    Discharge unit (3)    Pyrolytic reaction control system (4)    Helical feeding devices (11,32)    Pyrolytic reaction section (21)    Helical propulsion device (22)    Air supply device (23)    Transporting system (33)
NOVELTY - The pond has a pond main portion (1), feed port (2) and discharging port (3) which is arranged on pond main portion. The sealing belt (11) which is provided with L- type cross section is provided in the inner side surface of pond main portion. The outer surface of lower portion of pond cover (4) is matched with sealing belt.    USE - Floating cover type methane fermenting pond for recycling organic waste.    ADVANTAGE - The sealing effect of pond can be improved. The storage capacity of pond can be controlled effectively. The residue can be removed easily while ensuring the safety of operator. The power consumption of pond can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of floating cover type methane fermenting pond for recycling organic waste.    Pond main portion (1)    Feed port (2)    Discharge port (3)    Pond cover (4)    Sealing belt (11)
NOVELTY - A heat pump has heat and cold sources which are in thermal contact with working fluids used for air conditioning, bathing, heating, dehumidifying, ice-making and refrigerating processes. A bioreactor is provided to generate biomass fuel and heat energy. The heat regulation of bioreactor is performed by working fluids. A burner is provided to burn biomass fuel to over-heat working fluid, so that over-heated fluid is converted to high-temperature vapor. A thermoelectric generating set has cold end that is in thermal contact with heat reservoir to generate electric power.    USE - Energy regeneration system.    ADVANTAGE - The bioreactor can be filled with organic matters which are converted to biomass fuel under the action of micro-organism. The chemical energy of the biomass fuel can be converted efficiently to heat energy for driving the thermoelectric generating set to generate electric energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the energy regeneration system. (Drawing includes non-English language text)
NOVELTY - The present invention is about a continuous system for mass anaerobic bio-hydrogen production and the use thereof. The system comprises a glycosylation tank including a stirrer for mixing organic substances; a hydrogen fermenting tank for co-culturing anaerobic organisms and the organic substances the obtained from the glycosylation tank to produce gas and wastewater; an gas-liquid separator for separating the gas and the wastewater produced from the hydrogen fermenting tank; and a gas collecting and treating unit for collecting and treating the gas from the gas-liquid separator to obtain hydrogen gas. The bio-hydrogen production volume of the system can reach more than 6. 0m3 per day.
NOVELTY - A manufacturing apparatus (1) of hydrogen ion water and hydroxide-hydrogen dihydroxide ion water has an upper tank (4) and a lower tank (8) arranged in two stages, a partition portion (6) provided between upper and lower tanks, and tourmaline contact tank (7) accommodating tourmaline (9) in contacting state with water in lower tank. Water is supplied to lower tank from upper tank through filter formed in partition portion.    USE - Apparatus for manufacturing hydrogen ion water and hydroxide-hydrogen dihydroxide ion water.    ADVANTAGE - The apparatus lengthens electrolysis contact time of tourmaline, and has improved sustainability.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing apparatus of hydrogen ion water and hydroxide-hydrogen dihydroxide ion water.    Manufacturing apparatus (1)    Lid (2)    Opening portion (3)    Upper tank (4)    Partition portion (6)    Tourmaline contact tank (7)    Lower tank (8)    Tourmaline (9)
NOVELTY - The furnace has an air exhaust port (21) arranged on the fuel tank (18). The two ends of a clean fuel transmission pipe (22) are connected respectively with the air exhaust port and the fuel pipe (34) to interconnect the fuel tank with the fuel pipe. The side wall of the drum (8) is provided with a pore plate. A through-hole is provided on the side wall of the housing (7) at the place of the external side part of the pore plate. A repairing door is mounted on the external wall face of the housing for sealing the through-hole.    USE - Biomass multifunctional carbonizing furnace.    ADVANTAGE - Furnace is simple in structure, low in cost, multiple in functions, light in environmental pollution, low in power consumption, high in carbon yield rate, reliable in operation and low in error rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the biomass multifunctional carbonizing furnace.    Housing (7)    Drum (8)    Fuel tank (18)    Air exhaust port (21)    Clean fuel transmission pipe (22)    Fuel pipe (34)
NOVELTY - The fuel cell apparatus has fuel battery whose cathode air flow output end is connected to reactor. The metal hydride covered by permeable airtight film is arranged in reactor to provide cathode air flow of battery, to react with hydride to generate hydrogen gas. Permeable airtight film and carbon paper are fixed by adhesive such as silica gel, and film is formed by alkaline polymer electrolyte film or acid polymer electrolyte film. Metal hydride is adhered to the carbon paper, and formed as lithium aluminum-hydride (LiAlH4).    USE - Fuel cell apparatus.    ADVANTAGE - Since the fuel cell apparatus collects the water steam in the air flow of the fuel battery cathode, the cathode air flow of battery is reacted with the hydride in the reactor to obtain the hydrogen gas required for fuel battery so as to realize circuiting of apparatus without depending on the environment humidity. The simple structured fuel cell apparatus is designed easily so that the circulation of air flow is regulated according to the using state of the fuel battery.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the fuel cell apparatus. (Drawing includes non-English language text)
NOVELTY - Floating cover type methane tank comprises a methane tank body and a floating cover. The methane tank body has an open concrete structure. The tank body is fixed with a guide rail wheel and a feeding inlet. The feeding inlet is connected to the toilet. The floating cover is fixed with a floating cover guide rail, a gas guide tube and a pair of symmetric balance bodies.    USE - The tank is useful for producing methane.    ADVANTAGE - The tank: occupies less space; has short working period and low sealing requirement; easy to maintain and feed; is simple and safe to operate; promotes methane production; and conveniently discharges the product by utilizing easily separable floating cover from the methane tank while discharging.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the floating cover type methane tank.
NOVELTY - Organic solid ignition material comprises (in wt.%) sawdust carbon powder (20-40), vegetable oil (30-40), stearic acid (20-30) and spice (0.2). The organic solid ignition material is prepared by heating the above raw materials, cooling and solidifying.    USE - Used as an organic solid ignition material.    ADVANTAGE - The organic solid ignition material: is made of natural organic materials, so cinders in the grate and other solid fuels can be ignited conveniently; has long burning time in comparison with other fuels with similar functions; does not contain any petroleum source chemical products; and does not release toxic gases and harmful residual components after burning process, thus it is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic solid ignition material, comprising: (i) measuring the sawdust carbon powder, vegetable oil and stearic acid by using an automatic flow meter instrument and mixing; (ii) dissolving the mixed substances in a dibasic ester solvent, conveying into a reaction kettle and heating; (iii) conveying the heated substance into a heated container, adding the spice and mixing uniformly to prepare a viscous liquid; and (iv) conveying the viscous liquid into a molding machine and cooling to form a solid.
NOVELTY - An isolated lipase comprising an amino acid sequence comprising fully defined 318 amino acids (SEQ ID NO. 2) given in the specification, is new.    USE - The lipase is used for catalyzing or synthesis of ester, converting plant oil into biodiesel oil, and chiral splitting method (claimed).    ADVANTAGE - The lipase is a thermostable lipase.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a nucleic acid molecule encoding the lipase;    (2) a carrier comprising the polynucleotide;    (3) a cell comprising the carrier or the polynucleotide;    (4) a method for producing the lipase;    (5) a method for converting plant oil into biodiesel oil comprising treating the plant oil with lipase;    (6) a method for catalyzing synthesis of ester comprising catalyzing the esterification reaction using the lipase in an anhydrous system or a system with a few amount of water; and    (7) a chiral splitting method, where the lipase is used for chiral splitting via catalysis.
NOVELTY - Pre-treatment of a fermentation broth for extracting a target product comprises: (i) filtering a fermentation broth obtained after fermentation through a mesh filter to obtain a suspension 1; (ii) using a micro-beam to separate particulate matters having high precipitation velocity in suspension 1 by a siphon or a water pump in a beam deposition unit to obtain an extraction liquid 2; and (iii) performing ultrafiltration to the extraction liquid 2 to remove residual particles and macromolecular substances, separating the supernatant to extract the target product using a membrane.    USE - The method is useful for pre-treatment of a fermentation broth for extracting a target product.    ADVANTAGE - The method: removes granular substances in the fermentation broth without the requirement of filtration (e.g. microfiltration), centrifugation and flocculation; reduces blockage of membrane in subsequent membrane treatment, thus reducing the washing frequency of the membrane, and prolonging the service life of the membrane; and is economical, simple, safe, and suitable for large-scale industrial production.
NOVELTY - A Chlorella sp. YL-2 (CGMCC No: 4305), is new.    USE - The Chlorella sp. YL-2 is useful for treating sewage for removing nitrogen and/or phosphorus in sewage, and preparing biodiesel (all claimed).    ADVANTAGE - The Chlorella sp. removes nitrogen and phosphorus in the sewage simultaneously, is rich in oil content, and has wide application prospect with respect to biodiesel transferring system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) seed culture medium for culturing Chlorella sp., comprising (in g): annexin-5 and cobalt (A5+Co) solution (1 ml), starch (2), peptone (1.5), sodium nitrate (1.5), dipotassium hydrogen trihydrate (0.04), magnesium sulfate heptahydrate (0.075), calcium chloride dihydrate (0.036), citric acid (0.006), ferric ammonium citrate (0.006), EDTA disodium salt (0.001) and sodium bicarbonate (0.02) with respect to water (1 l), where the A5+Co solution is obtained using boric acid (2.86 g/l), manganese chloride monohydrate (1.81 g/l), zinc sulphate heptahydrate (0.222 g/l), copper (II) sulfate pentahydrate (0.079 g/l), sodium molybdate dihydrate (0.390 g/l), and cobaltous nitrate hexahydrate (0.049 g/l) with respect to water (1 l); (2) method (M1) of preparing seed liquid of Chlorella sp., involves culturing the Chlorella sp. in the culture medium; and (3) method (M2) of preparing biodiesel, involves extracting oil from the Chlorella sp. as raw material.
NOVELTY - A quercetin is prepared by dissolving rutin in alcohol solution, adding into catalyst, and reflux heating for 2-6 hours; recycling part of solvent, filtering, and recycling filtered catalyst, precipitating filtrate, filtering to obtain quercetin, and adding activated carbon into filtrate to decolor; filtering while hot, recycling activated carbon, concentrating filtrate, crystallizing, drying, and obtaining mixture of rhamnose and glucose; adding methanol, and insoluble substance glucose; and filtering to obtain glucose, then concentrating filtrate, and crystallizing to obtain rhamnose.    USE - Method for preparation of quercetin (claimed).    ADVANTAGE - The method is low-cost and environment-friendly. It has wide material sources, simple reaction condition, and easy operation. The catalyst replaces acid in the initial technique, and no acidic waste solution is generated. None of product hydrolyzed by rutin is flown away, thus satisfying requirements of energy-saving, environment-friendly and atom economy. The property of the catalyst is not reduced after recycling for 10 times.
NOVELTY - A low temperature aniline- degrading bacterial strain A1 belonging to new seeds of Pseudomonas (CGMCC 5011), is new. The preservation date is first day in December of 2010. The bacteria is Gram-positive aerobic bacteria, rod-shaped with length of 3 microns and width of 0.8 microns. The white colony of bacteria is formed on beef extract-peptone culture medium, where the colony is round, semi-transparent, smooth on the surface and wave shaped at the edge and difficult to stir up.    USE - The low temperature aniline- degrading bacteria is useful in biological processing of waste water.    ADVANTAGE - The aniline-degrading rate is 100%. The bacteria does not causes secondary pollution. The waste water can be processed cost-effectively.
NOVELTY - Organic acid/alcohol is produced by adding anaerobic bacteria capable of producing organic acid/alcohol by metabolizing carbon monoxide (CO), hydrogen (H2) and carbon dioxide (CO2) into reactor filled with inert particles as carriers; filling synthesis gas containing CO, H2 and CO2 in container, thus the carriers are up to fluidized state and keeping this state, and mixing and fermenting bacteria and carriers; and adding liquid culture medium in container, rushing suspended anaerobic bacteria out of container, and forming biological film by microorganism adhering to carrier surface.    USE - Method for producing organic acid or alcohol (claimed).    ADVANTAGE - The method realizes highly efficient conversion from synthesis gas to organic acid or alcohol by fully utilizing characteristic of high mass transfer efficiency of solid-liquid internal circulation fluidized bed and assisting with gas external circulation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for organic acid/alcohol production, which is a 3-phase anaerobic fluidized bed of solid-liquid internal circulation and gas external circulation.
NOVELTY - Microbial wax removing and preventing system is prepared by preparing culture liquor of Rhodococcus ruber Z25 strain; mixing with wax removing and preventing nutrient agent to obtain wax removing and preventing viscosity reducer; and infusing into recovery well barrel to remove and prevent wax.    USE - Microbial wax removing and preventing system.    ADVANTAGE - The system uses hydrocarbon-degrading strain with high activity, which can degrade the paraffin in raw oil, reduce the viscosity of raw oil, improve the flow property, and remove the paraffin attached on the well barrel, and has prolonged wax removal activity in the oil well. The wax removing and preventing nutrient agent of the system has low cost and simple preparation method and convenient application. It is suitable for application to the oil well with high wax content in large scale, improving the economical benefit of the oil field.
NOVELTY - The system has aeration biological filtering tank for filtering the sewage. The quick-filtering tank and artificial wetland are connected with each other.    USE - Combined sewage deep treatment system.    ADVANTAGE - Various types of pollutants contained in the sewage can be removed efficiently. The water standard quality can be improved. The service life of the artificial wetland can be improved. The possibility of preventing the artificial wetland from being blocked can be performed. The aeration amount of the water can be adjusted easily.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sewage deep treatment system.
NOVELTY - The apparatus has a gas sensor and signal processing circuit (1) whose signal output end is connected with a signal input end of a controller (2). An alarm and control signal output end of the controller is connected with an alarm and control signal input end of an alarm and relay circuit (3). The gas sensor and signal processing circuit is a natural gas sensor and signal processing circuit, a coal gas sensor and signal processing circuit, an ammonia gas sensor and signal processing circuit and a hydrogen sulfide gas sensor and signal processing circuit.    USE - Combustible gas detecting apparatus for use in a chemical laboratory.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a combustible gas detecting apparatus.'(Drawing includes non-English language text)'    Gas sensor and signal processing circuit (1)    Controller (2)    Alarm and relay circuit (3)    Display and remote control circuit (4)    Measuring signal output circuit (5)
NOVELTY - Biodiesel preparing involves reacting grease and monobasic alcohol in presence of alkali catalyst to obtain a product. Glycerin phase and light oil phase are separated from the product in presence of the alkali catalyst. The light oil phase is reacted with monobasic alcohol in presence of alkali catalyst to obtain a material. The obtained material is processed to obtain biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method increases balance conversion rate of grease, reduces content of triglyceride and diglyceride in the product and ensures that the free glycerin and the total glycerin content in biodiesel product can reach the national standard requirement.
NOVELTY - Valerian production-increasing fertilizer comprises (in wt.%) dry duck manure (8-10), dry pig manure (14-18), dry cow manure (12-16), ammonium bicarbonate (12-16), nitrogen fertilizer (8-12), potash fertilizer (10-12), nitramine (6-8), calcium fertilizer (3-5), phenolic resin (4-6), freshwater shrimp powder (4-6), methamidophos (2-4) and paclobutrazol (1-3).    USE - Used as a valerian production-increasing fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing valerian production-increasing fertilizer, comprising mixing the powder agents according to the ratio, placing in an agitator and stirring for 90 minutes, taking and grinding to particles about 80 meshes in a grinder, then placing again in an agitator and stirring for 180 minutes, taking and pouring the contents into a fermenting tank, adding liquid manure in a ratio of 1: 1.5, mixing up and down for stacking, tamping and covering tightly by plastic cloth, and fermenting for 28 hours, performing a first time pile-turning, where the pile turning is performed from the upper layer to the lower layer, from the inner layer to the outer layer, from inside to outside, and from outside to inside, and then adding liquid manure in a ratio of 1:1.5, stirring uniformly and stacking, tamping and covering tightly by plastic cloth, and fermenting for 48 hours, then performing a second pile-turning, stacking, and fermenting for 72 hours, then placing the fermented production-increasing fertilizer into a mold, which is 35 cm in height, 25 cm in width and 45 cm in length, to produce fertilizer blocks to obtain the product.
NOVELTY - Acylhydrazone schiff base, preferably (E)-N'-((2-hydroxynaphthalen-1-yl)methylene)picolinohydrazide (I), is new.    USE - (I) is useful in preparing medicine for curing liver cancer, lung adenocarcinoma, breast cancer, prostrate cancer, colon cancer (claimed) and promyelocytic leukaemia.    ADVANTAGE - In comparison to platinum anti-cancer medicine, (I): has high anti-cancer activity and good lipid solubility; is economical, environment-friendly and simple to prepare; and provides the novel path for developing the anti-cancer medicine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - Azithromycin slow-release microsphere comprises (wt.%) azithromycin (30-70), wax lipid slow-release framework material (5-25), water insoluble framework material (5-45), and binding agent (0.1-25). The binding agent is water-dispersed coating liquid.    USE - Azithromycin slow-release microsphere used to prepare medicine for curing infection caused by sensitized bacteria, e.g. respiratory tract infection, urogenital infection, nasosinusitis, otitis media and skin tissue infection (claimed).    ADVANTAGE - The azithromycin slow-release microsphere overcomes defect of spray-congealing. It does not need large amount of organic solvent or coating. The preparation is simple, environment-friendly and non toxic.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of azithromycin slow-release microsphere by mixing azithromycin, wax lipid slow-release framework material, water insoluble framework material and binding agent; extruding mixture to prepare microsphere; extruding soft material into strips; preparing microsphere through rolling circle device with extruder screen pore diameter of 0.2-0.25 mm; drying to remove water; heating; arranging grains; and screening microsphere with grain diameter less than 250 mu m;and    (2) azithromycin for suspension comprising azithromycin slow-release microsphere, suspending agent, flow aid, flavoring agent and essence.
NOVELTY - Sand complex matrix formulation prepared by mixing sand, saw powder, cow dung and chicken manure in the volume ratio of 5:3:1:1, is claimed.    USE - The sand complex matrix formulation is useful for soilless culture of tomato.    ADVANTAGE - The complex matrix: reduces the manufacturing cost, saves resources, reduces environmental pollution and realizes ecological virtuous cycle; is comprehensive in nutrition, easy to obtain high yield and environmental friendly; and promotes the development of agricultural economy in sandy areas.
NOVELTY - Extraction of a purified cichoric acid from Echinacea purpura comprises crushing E. purpura, and immersing in a less acidic solution; adding ethanol to carry out ultrasonic extraction; filtering the extract solution by an ultra-filtration membrane; concentrating and drying to obtain a crude extract; extracting by supercritical carbon dioxide (CO2); adding disodium EDTA; filtering and adding anion exchanging resin; washing the impurities by deionized water; eluting, and adding the eluting solution in a cation exchanging resin; and concentrating, and drying.    USE - Method for the extraction of a purified cichoric acid from E. purpura (claimed).    ADVANTAGE - The method produces cichoric acid with high content by separation purifying methods such as ion exchanging separation. It does not use large amount of toxic organic solvent, is safe, environment-friendly, is inexpensive, and has high yield.    DETAILED DESCRIPTION - Extraction of a purified cichoric acid from E. purpura comprises crushing E. purpura, and immersing in a less acidic solution; adding ethanol to carry out ultrasonic extraction; filtering the extract solution by an ultra-filtration membrane, and decompressing and recycling solvent; concentrating and drying to obtain a crude extract of E. purpura; extracting by supercritical CO2 and its cosolvent to obtain cichoric acid; adding disodium EDTA to disperse the extract, and adjusting the pH value to 8-9 by alkali; filtering and adding anion exchanging resin, and uniformly agitating; loading the solution on a column, and washing the impurities by deionized water; eluting by an alkaline solution, and adding the eluting solution in a cation exchanging resin; and collecting the solution, concentrating, and drying.
NOVELTY - Additive composition comprises component (I) comprising aromatic amine antioxidant and/or phenol antioxidant, and component (II) comprising polyether amine.    USE - Additive composition used in diesel composition, e.g. biological diesel oil, petroleum diesel oil, Fischer-Tropsch synthesis diesel oil, hydro-cracking biological diesel, or oxygen-containing diesel oil blend (claimed).    ADVANTAGE - The additive composition improves oxidation stability of the diesel composition.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (A) a diesel composition comprising additive composition and base diesel oil comprising biological diesel oil, petroleum diesel oil, Fischer-Tropsch synthesis diesel oil, hydro-cracking biological diesel, or oxygen-containing diesel oil blend;and    (B) method for improving oxidation stability of biological diesel oil by adding additive composition in the base diesel oil.
NOVELTY - A suspending agent comprises triflumizole.    USE - Suspending agent (claimed) is used in agricultural field.    ADVANTAGE - The suspending agent is environmentally-friendly and is manufactured efficiently by using reduced amount of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of suspending agent. The raw material components are mixed, pH value of the mixture is adjusted to 3-5, sheared and milled, to obtain suspending agent having average grain diameter of 2-3 microns.
NOVELTY - Hydrogen cracking tail oil is enabled to enter a decompression distilling tower to execute decompression distilling, and hydrogen cracking tail oil heavy fraction and hydrogen cracking tail oil light fraction are distilled. Ethane is prepared by vapor-cracking using distilled hydrogen cracking tail oil light fraction. The hydrogen cracking tail oil heavy fraction is recycled to hydrogen cracking device to obtain hydrogen cracking reaction.    USE - Hydrogenation cracking used for manufacturing ethane.    ADVANTAGE - The method provides cracking with high yield, by a simple process.
NOVELTY - The system has a heating device connected with a reaction device. The reaction device is divided into two parts that are connected with an extracted residual oil cutting system by a high-pressure separating device, a stable tower system and an extracting system. Kerosene is extracted from a bottom part of the extracted residual oil cutting system by a pipeline, where the bottom part of the cutting system is connected with a third part or a fourth part of the reaction device. A lower part of a stable system is connected with an extracting system.    USE - Reinforcing system for naphtha productive aromatic hydrocarbon.    ADVANTAGE - The system has better processing ability, high liquid yield, high aromatic hydrocarbon yield and high hydrogen gas yield.    DETAILED DESCRIPTION - The bottom part of the extracting system is extracted with mixed aromatic hydrocarbon. An INDEPENDENT CLAIM is also included for a reinforcing method for naphtha productive aromatic hydrocarbon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reinforcing system.
NOVELTY - An environmentally friendly skin disinfectant comprises (wt.%): disinfectant (0.1-1) prepared from coconut oil as foundation raw material; menthol (0.1-0.5); Dryobalanops aromatica (0.1-0.5); complexing agent (0.05-0.5); solubilizer (0.2-1); cosolvent and penetrant (5-10); penetrant (0.5-2.5); and distilled water or deionized water (balance).    USE - Environmentally friendly skin disinfectant for fast killing pathogenic bacteria on skin surface, in pore and under skin via cooperated effect, sterilizing through penetrating the skin, dephlogisticating and easing pain.    ADVANTAGE - The disinfectant has high permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the skin disinfectant which comprises (A) putting menthol and D. aromatica in the stainless steel or glass container; (B) adding rilanit special (PEG-60) to container and mixing until crystal is completely dissolved to liquid; (C) adding ethanol and mixing until to completely smelting the liquid; adding 60% of distilled water or deionized water and mixing to completely smelt; (D) adding environment friendly skin disinfectant prepared by coconut oil as foundation raw material; (E) adding EDTA and EDTA tetrasodium salt and mixing to completely dissolve; and (F) adding azone and uniformly mixing; and supplying distilled water or deionized water to set quantity and stewing and filtering as standby after mixing.
NOVELTY - Biological organic fertilizer fermenting strains Brevibacterium sp. D1 deposited under CCTCC No. M2010250 and Bacillus amyloliquefaciens S4 deposited under CCTCC No. M2010249, are new.    USE - The biological organic fertilizer fermenting strains Brevibacterium sp. D1 and Bacillus amyloliquefaciens S4 are useful for preparing biological organic fertilizer of tobacco straw.    ADVANTAGE - In utilizing the biological organic fertilizer fermenting strains Brevibacterium sp. D1 and Bacillus amyloliquefaciens S4, the tobacco straw biological organic fertilizer can replace other fertilizers to produce the tobacco, which is capable of improving yield of the tobacco leaf, increasing production value of the tobacco leaf, and improving smoking quality of the tobacco leaf. Moreover, it removes pollution on the environment from the tobacco straw waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing the biological organic fertilizer fermenting strains.
NOVELTY - Propanetriol cyclic acetal(ketal) ether comprises propanetriol cyclic acetal(ketal) ether of formula (I) and propanetriol cyclic acetal(ketal) ether of formula (II).    USE - Propanetriol cyclic acetal(ketal) ether used as methanol gasoline additive (claimed).    ADVANTAGE - The propanetriol cyclic acetal(ketal) ether provides methanol gasoline with excellent low-temperature cold start-up performance, and solves the gas resistance produced by automobile engine under high-temperature environment .    DETAILED DESCRIPTION - Propanetriol cyclic acetal(ketal) ether comprises propanetriol cyclic acetal(ketal) ether of formula (I) and propanetriol cyclic acetal(ketal) ether of formula (II)    R1=CnH2n;    n=1-3;    R2=CmH2m+1;and    m=1-10, preferably 3-5.    INDEPENDENT CLAIMS are included for:    (A) preparation of methanol gasoline additive comprising preparing intermediate product propanetriol cyclic acetal(ketal) by reacting raw materials for 3-5 hours at 60-100 degrees C and 0.1-10 MPa with acidic catalyst, reacting, distilling and collecting fraction at 90-130 degrees C to propanetriol cyclic acetal(ketal); and preparing methanol gasoline additive propanetriol cyclic acetal(ketal) ether by reacting propanetriol cyclic acetal(ketal)and 1-10C halogenated hydrocarbon for 3-4 hours with alkaline catalyst, reacting, distilling and collecting fraction product of 80-180 degrees C to obtain methanol gasoline additive propanetriol cyclic acetal(ketal) ether;and    (B) methanol gasoline comprising (pts.wt.) propanetriol cyclic acetal(ketal) ether (0.5-5) and methanol gasoline (100).
NOVELTY - Production of a fertilizer comprises grinding magnesium reduction furnace slag to a powder of 100-200 meshes; reacting the milled furnace slag with diluted hydrochloric acid, and filtering; drying and grinding to powder; dividing the filtrate to part A and part B; performing complete reaction for the solution A and diluted sulfuric acid; evaporating and crystallizing mixed crystal comprising calcium sulfate and magnesium sulfate; evaporating and crystallizing solution B at 100-150 degrees C to obtain mixed crystal of calcium chloride and magnesium chloride; and mixing and granulating.    USE - Method for the production of a fertilizer (claimed).    ADVANTAGE - The method prevents environmental pollution caused by magnesium reduction furnace, is inexpensive, and has no secondary pollution.    DETAILED DESCRIPTION - Production of a fertilizer comprises:    (A) grinding magnesium reduction furnace slag to a powder of 100-200 meshes;    (B) performing complete reaction for the milled magnesium reduction furnace slag with diluted hydrochloric acid, and filtering slag to obtain silicon dioxide;    (C) drying and grinding to powder;    (D) dividing the filtrate to part A and part B at a ratio of 1:(1.7-2);    (E) performing complete reaction for the solution A and diluted sulfuric acid;    (F) evaporating and crystallizing mixed crystal comprising calcium sulfate and magnesium sulfate;    (G) directly evaporating and crystallizing the solution B at 100-150 degrees C to obtain mixed crystal comprising calcium chloride and magnesium chloride; and    (H) mixing and granulating the silicon dioxide, mixed crystal comprising calcium chloride and magnesium chloride, and mixed crystal of calcium sulfate and magnesium sulfate.
NOVELTY - Fixing agent is a mixture of calcium hydroxide and phosphoric acid solution, where the ratio of calcium hydroxide to phosphoric acid solution meets the condition that no precipitate is generated in the mixture and the mixture is clear.    USE - The agent is used for fixing nitrogen in composting process. It is used for controlling nitrogen loss in composting process. (all claimed)    ADVANTAGE - The method of using the fixing agent is simple and easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for controlling nitrogen loss in composting process comprising putting the fixing agent into the composting material and composting.
NOVELTY - A biodiesel is prepared by adding ionic liquor or mixture of ionic liquor and metal salt chloride, short-chain alcohol, and free fatty acid or high-acid-value oil in high-pressure agitated reactor at a molar ratio of 0.01:0.1:1-6.1. Alcoholization reaction is done at 60-150 degrees C for 30-300 minutes. The molar ratio of mixture of ionic liquor to metal salt chloride is 1:1-9. Fatty acid methyl ester product is separated from ionic liquor, vacuum distilled to recover short-chain alcohol, and washed with hot water (70-90 degrees C). The ionic liquor is dried. Biodiesel is obtained via vacuum distillation.    USE - Method for preparing biodiesel by ionic liquid catalyzing (claimed).    ADVANTAGE - The ionic liquor is easy to separate, recover, and reuse after reaction. The method is simple in activated system and simple in technique.
NOVELTY - Rabdosia rubescens Chinese herbal medicinal nutrient fertilizer comprises (g) dry pig manure (16000), dry sheep manure (16000), dry goose manure (16000), dry donkey manure (16000), dry human excrement (16000), wheat flour (20000), freshwater shrimp powder (16000), mung bean powder (10000), rice bran (30000), bean pulp powder (30000), rice powder (30000), grass powder (30000), methamidophos (20000), ammonium bicarbonate (16000), urea (10000), superphosphate (10000), paclobutrazol (50000), growth hormone (50000), and epoxy resin (15000).    USE - R. rubescens Chinese herbal medicinal nutrient fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of R. rubescens Chinese herbal medicinal nutrient fertilizer comprising combining the powdered materials together; placing in a mixer and agitating for 90 minutes; taking out and placing in a crusher; crushing into grains of 80 mesh; placing in an agitator and agitating for 150 minutes; taking out and pouring in a fermenting pool; adding human excrement and water at 1:1.5 ratio; uniformly agitating up and down and piling; tightly compacting; covering and tightly pressing with a plastic cloth; fermenting for 30 hours; turning the pile for the first time, where turning is performed from upper layer to lower layer, inner layer to outer layer, inside to outside, and outside to inside; after turning the pile, adding human excrement and water at 1:1.5 ratio; uniformly mixing and piling; tightly compacting; tightly pressing with a plastic cloth cover and fermenting for 50 hours; turning the pile for the second time in the same method with the first turning step; piling and fermenting for 80 hours; and placing the fermented nutrient fertilizer in a die having a height of 30 cm, a width of 25 cm, and a length of 40 cm to prepare into nutrient fertilizer blocks.
NOVELTY - Cinnamon Chinese medicine herb nutrient fertilizer comprises (g) dry human excrement (10000), dry chicken manure (10000), dry goose manure (10000), dry donkey manure (10000), soybean cake powder (10000), wheat powder (10000), broomcorn powder (20000), rice bran (20000), organic composite fertilizer (10000), growth hormone (1000), potassium sulfate (1000), Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate) (2000), and epoxy resin (4000).    USE - Cinnamon Chinese medicine herb nutrient fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cinnamon Chinese medicine herb nutrient fertilizer comprising combining all powdered materials together; placing in a blender and blending for 100 minutes; placing in a crusher, taking out, and crushing into granules of 80 mesh; placing in the blender and blending for 140 minutes; taking out and pouring in a fermenting pool; adding human excrement liquid at 1:1.5 ratio and uniformly blending upwards and downwards; compacting tightly; pressing with a plastic cloth cover; fermenting for 24 hours; overturning for the first time from the upper layer to the lower layer, from the inner layer to the outer layer, from the inner side to the outer side, and from the outer side to the inner side; adding human excrement liquid at 1:1.5 ratio and uniformly blending upwards and downwards; compacting tightly; pressing with plastic cloth cover; fermenting for 40 hours; overturning in the same method with the first overturning step; stacking; fermenting for 72 hours; and placing in a mold, which is 35 cm high, 25 cm wide, and 40 cm long to form into nutrient fertilizer block.
NOVELTY - Chinese mallow planting and culturing fertilizer comprises (wt.%) dry chicken manure (6-10), dry duck manure (24-28), corn powder (22-26), peanut cake powder (4-6), wheat straw powder (2-6), bran powder (3-5), tea seed powder (4-6), Coptis powder (2-6), pepper powder (4-8), Illicium simonsii powder (2-4), rhizoma alismatis powder (1-3), folium mori powder (1-3), lotus leaf powder (1-3), and Asparagus fern powder (4-6).    USE - Chinese mallow planting and culturing fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Chinese mallow planting and culturing fertilizer comprising mixing the materials; placing into a stirrer and stirring for 90 minutes; taking out; placing all the materials into a grinder and grinding into powder; taking out; pouring into a fermenting tank; stacking; tightly covering and pressing with plastic cloth; fermenting in sealing manner for 72 hours; turning the stack for the first time; adding manure liquid at 1:0.6 ratio in the turning step; splashing the manure liquid while turning the stack, where materials are turned from the lower material upward, from the inner side to the outer side outside, from the outer side to the inner side, and from the upper layer downward; uniformly splashing manure liquid; tightly covering and pressing with plastic cloth after the turning step; fermenting for 72 hours; keeping the fermenting temperature at greater than or equal to 80 degrees C; performing the stack turning process for every 72 hours; adding manure liquid at 1:0.6 ratio in each stack turning process; and performing the stack turning process for 7 times.
NOVELTY - Field-return summer corn straw is decomposed by crushing fresh corn straw in the field directly by a machine to obtain crushed segments with length of 3-5 cm and width of 0.5-2 cm, and uniformly and directly laying the crushed segments on field surface; preparing fertilizing material comprising (kg) decomposing agent (2-2.5), additive (3-5), water-retaining agent (0.5-1), and urea (6-8), and fertilizing the corn straw; and turning over or immediately performing rotary plowing of straw with fertilizing material and uniformly mixing, and covering with soil, where plowing depth is 15-20 cm.    USE - Method of decomposing field-return summer corn straw (claimed).    ADVANTAGE - The method can quickly decompose corn straw and improve soil. The corn straw is returned to be recycled directly after crushing. Winter wheat can grow regularly when soil nutrient is restored. Further, the rate of emergence is greatly improved, and field farming operation is executed easily and conveniently.
NOVELTY - An Ephedra sinica traditional Chinese medicinal nutrition fertilizer comprises (g) dry pig manure (18000), dry duck manure (18000), dry cow manure (18000), maize powder (18000), sorghum powder (5000), maize cob powder (30000), cotton seed cake powder (20000), urea (15000), zinc fertilizer (10000), calcium magnesium phosphate fertilizer (1000), Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate) (1000), glucose powder (3000), and epoxy resin (3000).    USE - Ephedra sinica traditional Chinese medicinal nutrition fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer, comprising:    (A) preparing components into powder, combining powders, stirring for 90 minutes, pulverizing into particles of 80 meshes and stirring for 140 minutes;    (B) pouring mixture to a fermenting pond, then adding human excrement liquid, and uniformly stirring up and down;    (C) stacking, compacting, compactly covering with plastic or cloth, fermenting for 30 hours, overturning the stack for the first time from upper layer to lower layer, then from inner layer to outer layer, from inside to outside, and from outside to inside;    (D) adding human excrement liquid again, uniformly stirring up and down, stacking, compacting, compactly covering with plastic or cloth, fermenting for 46 hours, overturning the stack for the second time, stacking, and fermenting for 68 hours; and    (E) putting the fermented nutrition fertilizer to a mold of 30 cm in height, 20 cm in width and 40 cm in length, and then making into nutrition fertilizer block.
NOVELTY - A Chinese herbal medicine fertilizer comprises (wt.%) dry human excrement (4-6), dry chicken manure (18-22), organic fertilizer (15-17), potash fertilizer (6-8), nitrogenous fertilizer (10-14), manganese fertilizer (1-3), wheat straw powder (10-12), bean cake powder (4-6), loach powder (1-3), beanstalk powder (8-10), calcium powder (3-5), Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate) (1-3), and epoxy resin (4-6).    USE - Chinese herbal medicine fertilizer used for gemma agrimoniae (claimed).    ADVANTAGE - The fertilizer can increase yield of gemma agrimoniae.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising:    (A) preparing components into powder except human excrement, mixing the powders, and stirring for 100 minutes;    (B) grinding mixture into particles of 80 meshes and stirring for 160 minutes;;    (C) putting into a fermenting pool, stacking, adding human excrement, then compacting with plastic or cloth, and fermenting for 30 hours;    (D) performing primary turning of stack from upper layer to lower layer, inner layer to outer layer, inward to outward, or from outward to inward;    (E) adding with human excrement again for stacking, compacting with plastic or cloth, and fermenting for 48 hours;    (F) performing secondary turning; and    (G) stacking, fermenting for 72 hours, and arranging fermented fertilizer in a die with height of 40 cm, width of 30 cm and length of 45 cm to prepare into fertilizer block.
NOVELTY - A biological organic fertilizer comprises 0.001-10% of stachyose.    USE - Biological organic fertilizer used for increasing disease resistance and stress resistance of crops, reducing toxin, or promoting growth of crops.    ADVANTAGE - The fertilizer has high bioactivity and stable soil fertilizing capability, prevents soil hardening caused by common fertilizer, increases water retaining ability, adjusts flora balance of soil microorganism, and can fix nitrogen, degrade phosphorus, improve crop yield and increase crop quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising:    (A) adding stachyose (0-10%) into plant material straw extracted with stachyose or powdered straw of crops, mixing with animal excrement, adding turf and phosphate fertilizer, and adjusting pH to 7-8;    (B) adding the mixture to composite microbial inoculum (0.02-1 wt.% of mixture), and adding water so that the water content of the mixture is 40-55%;    (C) adding mixture of composite microbial inoculum, then piling and fermenting, where the piling height is not greater than 1.1 m;    (D) when internal temperature of the piled fertilizer is 50-60 degrees C, and turning the pile;    (E) after piling for 10-15 days, cooling to 40-45 degrees C and finishing fermentation; and    (F) cooling the fermented mixture to normal temperature, then adding stachyose (0.001-10%) and uniformly mixing, granulating and drying to prepare the biological organic fertilizer.
NOVELTY - The method involves heating electrolyte liquid mixture at 30 to 90 degrees centigrade and passed through a membrane or a cationic membrane electrolytic cell. The cell voltage is then controlled at 1.9 to 3.2 volts, while holding the current intensity at 1000 to 4000 amperes per square meter to obtain chlorine and hydrogen. Continuous, multi-level electrolyzation is performed by supplying refined salt to the mixture until the pH level of the mixture is 3 to 5. After electrolysis, salt is supplied to the mixture until saturated, then placed into a separate membrane to produce chloralkali.    USE - Mixture liquid electrolyzing method for thin waste hydrochloric acid.    ADVANTAGE - Ensures low cell voltage and high current efficiency for preparing chlorine and hydrogen through electrolyzing mixture liquid, thus ensuring efficient recycling of waste hydrochloric acid.
NOVELTY - An aqueous emulsion contains (pts. wt.) novaluron (0.5-50), solvent (1-15), emulsifier (1-15), dispersant (0.1-10), cosurfactant or thickener (0.2-6), antifreezing agent (0.2-5), antifoaming agent (0.1-1), antimicrobial agent (0.1-3), pH regulator, and deionized water (to 100). The emulsion is prepared by respectively preparing each component into oil phase and water phase, and shearing and dispersing at high speed.    USE - Aqueous emulsion used for controlling injurious insects of agricultural and garden crops such as cottons, soybeans, corns, fruit trees, rice and vegetables, particularly cotton bollworm, soybean pod borer, leaf roller, Helicoverpa assulta, pine moth, aleyrodid, thrips, and snout moth's larva.    ADVANTAGE - The emulsion is environment friendly; does not use or utilizes little organic solvent; has low manufacturing cost and application cost; and reduces toxicity to operators, storage and transportation workers, and users during manufacture, storage, transportation and usage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of emulsion by adding novaluron, solvent, emulsifier and cosurfactant to a tank, and stirring to obtain uniform oil phase; adding water, antifreezing agent and antimicrobial agent to a tank, and stirring to obtain uniform water phase; and placing the oil phase (or water phase) in a tank with high-speed shearing machine, starting the shearing machine, adding the water phase (or oil phase), shearing at high speed, and dispersing.
NOVELTY - Recycling hot air generated by a compost comprises recycling heat generated by a composting process in ferment cabin unit A; and introducing the recycled heat to a ferment cabin B for the compost in the ferment cabin B, where the ferment cabin unit A comprises an independent ferment cabin different from the ferment cabin B.    USE - A method for recycling hot air generated by compost to prepare a fertilizer (claimed).    ADVANTAGE - The method has simple and easy operation, reduces resource waste, reduces processing cost for the heat energy, and reduces the cost for processing the domestic slag.
NOVELTY - Organic biological medicinal fertilizer comprises (pts.wt.) zeolite (8-25), amino acid (3-12), ammonium molybdate or sodium molybdate (0.2-1), manganese sulfate (3-10), fulvic acid (2-8), ammonium carbonate (2-8), zinc sulfate (0.2-2), EDTA (0.2-2), acetic acid (0.2-1), flavone (0.3-2), n-butanol (1-5), and low-sugar organic material (0.2-0.6).    USE - Organic biological medicinal fertilizer used for preventing and treating harmful bacteria.    ADVANTAGE - The fertilizer addresses both the symptoms and root causes of disease; and has complete nutrition, no toxicity, no harm, and no residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic biological medicinal fertilizer comprising taking plant waste containing 3-5% water or city refuse containing organic substance; adding 0-20 times water and fermenting enzyme; heating at 28-50 degrees C while stirring to hydrolyze; filtering the solution; reducing the pressure in vacuum; condensing to 35-40 wt.%; sterilizing and sealing to obtain low-sugar organic material; mixing zeolite, amino acid, ammonium molybdate or sodium molybdate, manganese sulfate, fulvic acid, ammonium carbonate, and zinc sulfate; dissolving with 3-10 times water and filtering; adding the low-sugar organic material to the filtrate; mixing; adding EDTA, acetic acid, flavone, and n-butanol; stirring; and regulating the pH at 3-8.
NOVELTY - Processing livestock waste comprises transporting livestock waste to anaerobic fermenting tank; transporting the sewage gas to the gas storage tank; transporting fermented sewage gas liquid to biologic leaching pond reactor; adding medicament and domestication microorganism inoculum; and introducing air; processing sewage gas liquid; compressing, filtering and dewatering the sewage; taking mud cake as organic fixed fertilizer; adding lime milk in filtrate, and regulating pH to 7 to 7.5; and obtaining clean available water via the processing of inverse penetration device.    USE - Method for processing livestock waste (claimed).    ADVANTAGE - The method is economic and environment-friendly, and has strong operability, and good sewage processing effect.    DETAILED DESCRIPTION - Processing livestock waste comprises taking livestock waste to transport to anaerobic fermenting tank for fermenting processing; transporting the sewage gas obtained by fermenting to the gas storage tank for storage; transporting fermented sewage gas liquid to biologic leaching pond reactor; adding medicament and domestication microorganism inoculum in biologic leaching pond reactor; and introducing air; making sewage gas liquid processed in biologic leaching pond reactor; compressing, filtering and dewatering the sewage which is biologic leaching processed; taking mud cake as organic fixed fertilizer; adding lime milk in filtrate, and regulating pH to 7 to 7.5 for micro-filtering film processing, and super-filtering film processing; and obtaining clean available water via the processing of inverse penetration device.
NOVELTY - Synthesis of 5,7-dihydroflavone comprises reacting active methylene compound ethyl acetoacetate with acylating agent benzoyl chloride in the presence of condensing agent; eliminating acetyl by selective hydrolysis of ammonium chloride solution to obtain ethyl benzoylacetate; mixing intermediate ethyl benzoylacetate with phloroglucinol to dissolve; heating; vacuumizing and reacting to obtain crude product, and refining crude product by dimethylformamide and ethanol to obtain 5,7-dihydroflavone product.    USE - Synthesis of 5,7-dihydroflavone for pharmaceutical industry.    ADVANTAGE - The method uses rich raw material sources, low cost, short reaction step, and simple operation thus optimizes reaction condition. It provides high yield and less environment pollution.    DETAILED DESCRIPTION - Synthesis of 5,7-dihydroflavone comprises reacting active methylene compound ethyl acetoacetate with acylating agent benzoyl chloride in the presence of condensing agent; controlling reaction temperature below 10 degrees C for more than 5 hours; performing normal-temperature hydrolytic reaction at pH greater than 11 for 2-24 hours using saturated ammonium chloride water solution to eliminate acetyl and obtain ethyl benzoylacetate; dissolving intermediate ethyl benzoylacetate with phloroglucinol at molar ratio of 1:1-2:1; heating at 152-156 degrees C and vacuumizing for 6 hour; finishing reaction to obtain crude product; and refining crude product with dimethylformamide and alcohol to obtain 5,7-dihydroflavone. The molar ratio of condensing agent to ethyl acetoacetate is 1:1-2:1. The condensing agent is sodium hydroxide, potassium hydroxide, and/or calcium hydroxide. The solvent comprises methanol, ethanol or water.
NOVELTY - The system (10) has a sulfur feed port that discharges the sulfur generated by the sulfur generating station (20), to the polyelectrolyte electrolytic bath (30). An electricity supply unit (50) supplies the electricity to the polyelectrolyte electrolytic bath made of polymer, in which the sulfuric acid is manufactured using sulfur. A sulfuric acid storage unit (70) stores the sulfuric acid produced in the electrolytic bath.    USE - Proton exchange membrane electrolysis technology based hydrogen generation system for fuel cell.    ADVANTAGE - The efficiency of manufacturing the sulfuric acid can be improved and need to perform sulfuric acid decomposition process at high temperature can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for optimization method of hydrogen generation system based on proton exchange membrane electrolysis technology.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generation system. (Drawing includes non-English language text)    Hydrogen generation system (10)    Sulfur generating station (20)    Polyelectrolyte electrolytic bath (30)    Electricity supply unit (50)    Sulfuric acid storage unit (70)
NOVELTY - The invention relates to an aerobic fermentation device for an organic matter comprising a fermentation processing machine, a heat exchanger, a culturing basin and a fuel cell. The heat exchanger can dissipate and condense organic gas produced by the fermentation processing machine to allow it becoming a high COD solution, gas and heat energy, thereby supplying nutrient and temperature required for microorganisms in the culturing basin. The residual gas absorbed by the microorganisms can be supplied to the fuel cell for generating electric power. Accordingly, the organic gas and heat energy produced in the fermentation processing machine can be effectively recovered and utilized.
NOVELTY - The system has a fuel anode supplied with hydrogen to produce a proton and an electron, and an air electrode supplied with oxygen to produce water. An electrolytic bath produces hydrogen and sodium hypochlorite from seawater, and a flash chamber separates the sodium hypochlorite, and supplies the separated hydrogen to a fuel delivery system unit. A sodium hypochlorite repository stores the hydrogen and separated sodium hypochlorite in the flash chamber, and a deionized water circulating pump transports deionized water stored in a pure water storage tank to a fuel cell.    USE - Polymer electrolyte fuel cell (PEFC) system. Uses include but are not limited to seawater electrolysis facility, waste treatment facility, iron mill, generating station, and oil refinery.    ADVANTAGE - The system has improved efficiency and stabilization and long service life, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a polymer electrolyte fuel cell system. '(Drawing includes non-English language text)'
NOVELTY - A plant oil-based cross-linked polymer obtained by cross-linking two meth(acrylate) groups contained in plant oil using cross-linking agent, is new.    USE - New plant oil-based cross-linked polymer useful as substitute for petroleum.    ADVANTAGE - The plant oil-based cross-linked polymer can be manufactured easily and has excellent biodegradability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the plant oil-based cross-linked polymer.
NOVELTY - A plant oil-based crosslinked polymer obtained by crosslinking two meth(acrylate) groups contained in plant oil using crosslinking agent, is new.    USE - The plant oil-based crosslinked polymer is used as substitute for petroleum.    ADVANTAGE - The plant oil-based crosslinked polymer has excellent biodegradability and can be manufactured easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing the above-cited plant oil-based crosslinked polymer.
NOVELTY - Solid fuel composition comprises (in wt.%): food waste (30-70), synthetic resin waste (20-60), wood powder (1-10), 10% dilute sodium silicate solution (3-7) and graphite powder or coal powder (5-10).    USE - Solid fuel composition.    ADVANTAGE - The waste resources can be recycled and regenerated.
NOVELTY - A biogas production system comprises a supply unit for supplying organic waste, a gas production unit which generates biogas by fermenting the organic waste supplied from the supply unit, a liquefied fertilizer reservoir for receiving the organic waste from the supply unit and the gas production unit and storing as a liquefied fertilizer, and a contaminated water processing unit for purifying contaminated water generated from the organic waste.    USE - Biogas production system (claimed).    ADVANTAGE - The contaminated water generated during biogas production using the system is recyclable.
NOVELTY - Apparatus for recharging a fuel cell comprises: (a) a housing having a fuel cell cartridge holder; (b) a water reservoir disposed in the housing and having water disposed in it; (c) an electrolysis chamber for converting water into hydrogen and oxygen; and (d) a vacuum pump in fluid communication with the fuel cell cartridge holder.    USE - The apparatus is used for recharging a fuel cell (claimed).    ADVANTAGE - The apparatus can be used in non-commercial environments such as in a consumer's home.    DETAILED DESCRIPTION - Apparatus for recharging a fuel cell comprises: (a) a housing having a fuel cell cartridge holder; (b) a water reservoir disposed in the housing and having water disposed in it; (c) an electrolysis chamber for converting water into hydrogen and oxygen, where the electrolysis chamber is in fluid communication with the water reservoir, where the electrolysis chamber includes a hydrogen passage for passing hydrogen from the electrolysis chamber to the fuel cell cartridge holder; and (d) a vacuum pump in fluid communication with the fuel cell cartridge holder, where the vacuum pump is configured to selectively vent residual hydrogen from a fuel cell cartridge disposed in the fuel cell cartridge holder. An INDEPENDENT CLAIM is included for a method for recharging a hydrogen fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the portable hydrogen fuel cell cartridge charger.    Controller (210)    Fan (215)    Cooler or condenser (220)    Water reservoir (223)    Water purifier (224)    Electrolysis chamber (225)    Filter (235)    Vacuum pump (242)    Fuel cartridge holder (255)
NOVELTY - A methane gas is produced by decomposing biodegradable resin in decomposition liquid containing biodegradable enzyme, buffering agent, organic solvent and water, and carrying out methane fermentation of decomposition liquid in which solubility parameter value of organic solvent is less than or equal to 8.5- greater than or equal to 11.5 and content rate of organic solvent in decomposition liquid is less than or equal to 15-1%.    USE - Production of methane gas for electric power generation.    ADVANTAGE - The method produces methane gas efficiently from biodegradable resin containing lactic acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the generated gas amount. (Drawing includes non-English language text).
NOVELTY - System for production of hydrogen energy utilizing silicon wastewater comprises ultrafiltration (UF) treatment bath where the silicon wastewater is treated through UF film filtration to separate UF treated water and a concentrated silicon waste solution; a line mixer connected to the UF treatment bath in order to admix the separated silicon waste solution with an alkaline material fed from the outside; and a hydrogen production bath connected to the line mixer, where the concentrated silicon waste solution in the mixture reacts with the alkaline material, in order to produce hydrogen gas.    USE - The system is useful for production of hydrogen energy utilizing silicon wastewater (claimed).    ADVANTAGE - The invention provides hydrogen energy production system utilizing silicon wastewater, including secondary treatment of the silicon wastewater to improve recovery to a desired level. Additionally, the hydrogen energy production system includes solidification of the residual waste remaining in the silicon wastewater, thus decreasing waste mass and efficiently reducing waste disposal costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for production of hydrogen energy utilizing silicon wastewater comprising treating the silicon wastewater through UF membrane filtration to separate UF treated water and a concentrated silicon waste solution; admixing the separated silicon waste solution with an alkaline material; reacting the concentrated silicon waste solution with the alkaline material in the mixture to produce hydrogen gas and alkaline water; and using an acidic material to neutralize the alkaline water, thus forming a supernatant and a precipitate.
NOVELTY - The device has an air suction device (4) connected with a purification groove (6) that is utilized for receiving discharged smoke by a reaction groove (3). The purification groove is provided with multiple passages (61). The passages of the purification groove are provided with a multilayer filtration unit (62) for filtering smoke to gas. A gas storage groove (7) is connected to the purification groove for receiving the filtered gas from the purification groove after being deposited and purified in the gas storage groove. The gas is conductively inflated to a collection bottle (8).    USE - Device for producing regenerated resource from waste materials.    ADVANTAGE - The waste material can be adopted to produce the regenerated energy gas as dynamic fuel, so as to achieve recycle environmentally friendly effect to replace the produced energy source with environmental waste materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of device for producing regenerated resource from waste materials.    Reaction groove (3)    Air suction device (4)    Purification groove (6)    Gas storage groove (7)    Collection bottle (8)    Passages (61)    Multilayer filtration unit (62)
NOVELTY - The device has a plasma spray gun (6) arranged at a rear end of a gasification hearth (13). A spray opening of the plasma spray gun appoints into the gasification hearth. A spiral material pusher is arranged in front of the gasification hearth. The spiral material pusher is provided with a spiral shell and a spiral shaft (19). A spiral material pushing head in front of the spiral shaft is fixed in the spiral shell. A discharge end of the spiral shell is stretched into the gasification hearth from a front end of the gasification hearth. A material bin is connected above the spiral shell.    USE - Device for producing hydrogen and coal gasification co-production gas by plasma pyrolysis water.    ADVANTAGE - The device realizes hydrogen production and coal gasification co-production gas made by plasma pyrolysis water to form complementation to achieve purpose of improving synthetic gas quality, saving coal loss and reducing greenhouse gas emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device for producing hydrogen and coal gasification co-production gas by plasma pyrolysis water.    Housing (2)    Heat-insulated layer (3)    Plasma spray gun (6)    Gasification hearth (13)    Spiral shaft (19)
NOVELTY - The combustor has a high-temperature cracking chamber (16) whose material inlet (25) is connected with a feeding device (24). An upper part of the cracking chamber is provided with a gasification combustor (21). A lower part of the cracking chamber is connected with a blower (8). The gasification combustor is interconnected with a counter-combustion chamber (22). A side of the counter-combustion chamber is provided with a combustion barrel (23). The material inlet of the cracking chamber is connected with the blower via a cooling pipe.    USE - Biomass gasification combustor for a heating supplying device.    ADVANTAGE - The combustor burns the biomass fuel, thus enhancing the energy utilization rate, reducing the smoke generated in the combustion process, and protecting the atmospheric environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification combustor.    Blower (8)    High-temperature cracking chamber (16)    Gasification combustor (21)    Counter-combustion chamber (22)    Combustion barrel (23)    Feeding device (24)    Material inlet (25)
NOVELTY - Sodium hydroxide (in parts weight) (90-10) is mixed with red clay (10-90) to obtain a mixed composition. The mixed composition is heated at 1100-1300 degrees C for 1-4 hours and melted to obtain a liquid melt. The liquid melt is cooled to obtain red clay processed material.    USE - Manufacture of red clay processed material used for composition for anti-corrosive agent and composition for disinfecting agent (both claimed). Can also be used in healthcare products, agricultural products, livestock products, food preservative, natural agricultural pesticide, fertilizer, paint, feed, construction material, cosmetic additive or marine products for preventing viral infectious diseases, and bacterial infection and inhibiting red tide.    ADVANTAGE - The red clay processed material and alkali ionized water are economically manufactured under mild reaction conditions. The red clay processed material and alkali ionized water are environmentally-friendly and non-toxic, and has excellent anti-corrosive property, and virus disinfecting activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alkali ionized water.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of processed material and alkali ionized water.
NOVELTY - A refuse-derived fuel is manufactured by using coagulation-sedimentation sludge of aqueous emulsion or latex containing aqueous solution, molding into organic waster after mixing and solidifying.    USE - Manufacture of refuse-derived fuel.    ADVANTAGE - The method is simple, has less environment impact and is excellent in economical efficiency.
NOVELTY - A supercritical carbon dioxide extraction procedure which is applied to produce Crassna seeds biodiesel material, especially for those use Crassna seeds as the raw materials and apply supercritical carbon dioxide extraction technique to provide high quality biodiesel.
NOVELTY - The apparatus has a hydrogen-production portion that generates hydrogen from electrolyte solution. An oxygen generation portion generates oxygen from electrolytic solution. The gas generation portions (7,8) are provided on back surface of photoelectric conversion element (2). The photoelectric conversion element is electrically connected to gas generation portions so that the electromotive force is generated when the received light from the photoelectric conversion element is supplied to the gas generation portions.    USE - Apparatus for production hydrogen by using sunlight as renewable energy source. Can also be used in hydraulic power, wind force, geothermal heat, tidal power, biomass, etc.    ADVANTAGE - The photoelectric conversion element is electrically connected to gas generation portions so that the electromotive force is generated when the received light from the photoelectric conversion element is supplied to the gas generation portions. Hence the hydrogen can be collected efficiently and the cost required for manufacturing the hydrogen production apparatus can be reduced. Since the hydrogen-production portion and oxygen generation portion are provided on the back surface of the photoelectric conversion element, the scattering of incident light by electrolyte solution can be prevented. The quantity of incident light to photoelectric conversion element can be increased so that the optical efficiency can be improved. The reduction in production rate of hydrogen by imbalance movement of proton concentration can be prevented even if the hydrogen production apparatus is enlarged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen production apparatus.    Photoelectric conversion element (2)    Gas generation portions (7,8)    Electro-conductive portion (9)    Insulation portion (11)    Top plate (14)
NOVELTY - Uricase inhibitor comprises one or more uricase inhibiting substances chosen from Eucalyptus, Eucalyptus extract, bamboo vinegar and corn steep liquor.    USE - The agent is used as uricase inhibitor for preparing compost (claimed).    ADVANTAGE - The uricase inhibitor prevents generation of ammonia from uric acid. The compost with high nitrogen content can be obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing compost, which involves adding the above-mentioned uricase inhibiting substance and composting excretion containing uric acid.
NOVELTY - Method for decomposing organic substance, involves preparing to-be-decomposed organic substance and treating the organic substance with mother-cell degradation enzyme produced through cell degradation accompanying sporulation of spore-forming aerobic bacterium.    USE - The method is useful for decomposing organic substance chosen from soybean curd residue, material comprising lignin and/or cellulose, fish scales, reishi mushroom, Agaricus blazei, caterpillar fungus, and Fuscoporia obliqua. The decomposition product of soybean curd residue is used as herbicide, decomposition product of material comprising lignin and/or cellulose is used as ethanol raw material, and decomposition product of fish scales is used as cosmetic liquid for activating innate immunity (all claimed). The material comprising lignin and/or cellulose is chosen from bamboo, timber and rice straw. The cosmetic liquid is also useful for stimulating phagocytosis of melanin in skin, preventing liver spots and sun burn, reducing lump of white acne, masking wrinkles, activating keratinocyte for improving skin metabolism, rejuvenating skin cell and promoting hair growth, and suppressing skin inflammation.    ADVANTAGE - The method enables rapid decomposition of organic substance.
NOVELTY - Preparing a bio-oil having a total acid number (TAN) of less than 10 from a solid biomass material, comprises: subjecting the solid biomass material to a catalytic pyrolysis process thus the bio-oil having a TAN of less than 60 and greater than 10 is produced; and subjecting the obtained bio-oil to an acid removal step.    USE - The process is useful for preparing a bio-oil having TAN of less than 10 or less than 5 from a solid biomass material (claimed), where the bio-oil is useful for fueling a boiler or turbine.    ADVANTAGE - The process provides bio-oil with a yield of greater than 30 wt.% with good quality and improved stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing a bio-oil having a TAN of less than 5 from a solid biomass material, comprising: (a) subjecting the biomass to a catalyst pre-treatment step; (b) subjecting the pretreated biomass material to a catalytic pyrolysis process thus the bio-oil having a TAN of less than 40 and greater than 5 is produced; and (c) subjecting the obtained bio-oil to an acid removal step.
NOVELTY - Pre-processing assembly for processing fuel feedstock for a fuel cell including oxygen and hydrocarbons having higher and lower hydrocarbon content, comprises: a deoxidizing unit for reducing the oxygen in the fuel feedstock; a propane processor unit for reducing the propylene in the fuel feedstock; and a pre-reforming unit for reducing the higher hydrocarbon content in the fuel feedstock.    USE - The pre-processing assembly is useful for processing fuel feedstock including natural gas, heavy duty-5% maximum allowable propylene content, and LPG to produce methane rich gas which is used in a high temperature fuel cell (all claimed).    ADVANTAGE - The pre-processing assembly: reduces or substantially eliminates the higher hydrocarbon and oxygen contents in the fuel feedstock; reduces the lower hydrocarbon content and increases the hydrogen content in the feedstock; has an extended life span; operates without an additional supply of hydrogen to the fuel feedstock; and utilizes a pre-reforming unit, which removes sulfur-containing compounds from the fuel feedstock, thus increasing the operating life of the reforming catalyst in the fuel cell assembly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the pre-processing assembly of the fuel cell system with a fuel delivery system.    Vessel (202)    Deoxidizer bed (204)    Pre-reforming bed (301) Propane processor bed (206)    Carbon resistant catalyst (305)
NOVELTY - The biogas plant (10) comprises a biogas reactor (12) such as a drying fermenter, which is aligned for producing biogas (21) and a fermentation residue (40) made of organic material, an engine such as gas turbine (14), which is connected with the biogas reactor, is aligned for combusting the biogases and has an exhaust gas system, and a fermentation residue-drying device, which is connected with the exhaust gas system for drying the fermentation residue with exhaust gases of the engine. The biogas plant has a hall, which surrounds the biogas reactor, a suction device and a storage device.    USE - Biogas plant for producing solid fuel.    ADVANTAGE - The biogas plant ensures economical and efficient production of the solid fuel with less operating personnel requirements.    DETAILED DESCRIPTION - The biogas plant (10) comprises a biogas reactor (12) such as a drying fermenter, which is aligned for producing biogas (21) and a fermentation residue (40) made of organic material, an engine such as gas turbine (14), which is connected with the biogas reactor, is aligned for combusting the biogases and has an exhaust gas system, and a fermentation residue-drying device, which is connected with the exhaust gas system for drying the fermentation residue with exhaust gases of the engine. The biogas plant has a hall, which surrounds the biogas reactor, a suction device, which is arranged to the gas turbine for sucking the combustion air from the hall, and a storage device for the fermentation residue, where the storage device is arranged in the hall. The suction device is arranged for sucking the combustion air from the biogas reactor and/or the storage device. An INDEPENDENT CLAIM is included for a method for producing a solid fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a biogas plant.    Biogas plant (10)    Biogas reactor (12)    Gas turbine (14)    Biogas (21)    Fermentation residue. (40)
NOVELTY - The method involves gasifying biomass to combustion gas in a fuel carburetor (3) with a gasification medium, where the combustion gas is converted into synthesis gas by gas processing. High temperature cleaning is performed by a centrifugal separator (5). A high temperature tar is reformed by a catalytic converter. High-temperature sulfur-and halogen are removed from sorbents by dry sorption process. The processing accomplished with gas temperature is of gaseous fuel between 700-900 degree Celsius. A high temperature fine electrostatic is precipitated in the gas processing.    USE - Method for producing synthesis gas from biomass in a fuel carburetor.    ADVANTAGE - The high temperature tar is reformed by the catalytic converter, and the high-temperature sulfur-and halogen are removed from sorbents by the dry sorption in the gas processing, so that additional cooling steps or heat extraction from the combustion gas before or during the gas processing of the combustion gas is not necessary, thus producing the synthesis gas from the biomass in economic and efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing synthesis gas from biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a method for producing synthesis gas from biomass in a fuel carburetor.    Fuel carburetor (3)    Free space region (4)    Centrifugal separator (5)    Tar reforming unit (6)    Fine dust sampler (7)
NOVELTY - The method involves controlling a valve-control part (8) to perform operations of supply of liquid e.g. activated-sludge treated water, to filling parts (21-23) of a gas-liquid contact part (2) at levels, and stop by turns while introducing a to-be-processed gas that contains an insoluble or slightly soluble odor component e.g. ester, in water other than a water soluble odor component e.g. lower fatty acid, from an inlet (11). The supply of the liquid to the filling part at a stage is stopped and supply of the liquid to the filling part at another stage is controlled by the valve-control part.    USE - Method for bio-deodorizing an odor component e.g. water insoluble or slightly soluble odor component such as ester and aromatic hydrocarbon type flavor elements, and water soluble odor component e.g. lower fatty acid, hydrogen sulfide and ammonia, generated from sewage, sludge, and industrial waste water in a to-be-processed gas i.e. process gas. Can also be used for biogas, pyrolysis gas, waste gas, and sewage gas generated by methane fermentation to micro-organisms.    ADVANTAGE - The supply of the liquid to the filling part at the stage is stopped, and supply of the liquid to the filling part at another stage is controlled by the valve-control part even when the odor component insoluble in water other than the water soluble odor component or slightly soluble is contained in the to-be-processed gas, thus ensuring effective deodorizing, and maintaining activity of microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bio-deodorizing apparatus comprising a filling part.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a bio-deodorizing apparatus. '(Drawing includes non-English language text)'    Gas-liquid contact column (1)    Gas-liquid contact part (2)    Valve-control part (8)    Inlet (11)    Filling parts (21-23)
NOVELTY - A light oil composition with density of 0.800-0.900 g/cm3 in 15 degrees C and cetane numbers of 44-70 comprises not greater than 10 mass ppm of sulfur, 3-37 vol.% of water and 2-16 vol.% of butanol.    USE - Light oil composition used as fuel for diesel engines.    ADVANTAGE - The light oil composition has favorable combustion efficiency, contributes to energy security or global warming prevention, and reduces particulate matter in exhaust gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of light oil composition involving mixing 65-95 vol.% of light oil base materials with initial boiling points of 150-205 degrees C and end points of 290-380 degrees C which contain less than or equal to 30 vol.% of aromatics part and 3-20 vol.% of water containing butanols on light oil composition standard, and mixing 2-32 vol.% of water on light oil composition standard and setting as emulsion after adding 0.3-5 mass% of surfactant and dissolving on light oil composition standard.
NOVELTY - The light source (1) has a modulation light output part (11) outputting a laser beam, where wavelength of the laser beam is modulated by predetermined wavelength interval. An optical fiber (12) propagates the laser beam. An excitation light output part (13) outputs excitation light for Raman-amplifying the laser beam propagating the optical fiber. A wavelength converter (14) i.e. second harmonic generation element, converts wavelength of the amplified laser beam into short wavelength according to nonlinear optical effect.    USE - Laser light source for a gas detection apparatus (claimed). Uses include but are not limited to detection of methane, oxygen, carbon dioxide, acetylene and ammonia.    ADVANTAGE - The wavelength converter converts the wavelength of the amplified laser beam into the short wavelength according to the nonlinear optical effect, thus detecting the detection object gas smaller than 1.2 micrometer at high precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas detection apparatus comprising a laser light source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a laser light source.'(Drawing includes non-English language text)'    Laser light source (1)    Modulation light output part (11)    Optical fiber (12)    Excitation light output part (13)    Wavelength converter (14)
NOVELTY - System for saccharifying and fermenting cellulose biomass as raw material, where the saccharifying and fermenting processes are performed by adding cellulose degradation enzyme and yeast for alcohol fermentation to biomass feedstock containing liquid, subjecting the obtained liquid to saccharification and fermentation simultaneously, subjecting the obtained product to alcohol isolation process to obtain residue, and saccharifying and fermenting all or portion of the residue.    USE - The system is useful for saccharifying and fermenting cellulose biomass for producing ethanol.    ADVANTAGE - The system enables cost-effective and rapid mass-production of ethanol.    DETAILED DESCRIPTION - System for saccharifying and fermenting cellulose biomass as raw material, where the saccharifying and fermenting processes are performed by (a) adding cellulose degradation enzyme and yeast for alcohol fermentation to biomass feedstock containing liquid, (b) subjecting the obtained liquid to saccharification and fermentation simultaneously, (c) subjecting the obtained product to alcohol isolation process to obtain residue containing various substances derived from cellulose degradation enzyme, yeast for alcohol fermentation and biomass feedstock, and (d) saccharifying and fermenting all or portion of the residue. The yeast for alcohol fermentation is Issatchenkia orientalis.
NOVELTY - A biological synergistic strain is used in sewage of petrochemical industry, where strain comprises BIO-TRET BA 1008CB or BIO-TRET BA ABR synergistic strain.    USE - Biological synergistic strain is used in sewage of petrochemical industry.    ADVANTAGE - The use of biological synergistic strain can solve problem that sewage in petrochemical industry is degraded difficultly in whole recycling process, improves treatment effect of petrochemical sewage, and recycles sewage.
NOVELTY - Biomass type coal comprises (in parts by wt.) coal mud (40-50), high-quality anthracite coal (20-30), biomass straw (10-20), peat soil (5) and lime (5).    USE - Used as a biomass type coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for processing biomass type coal, comprising grinding the biomass straw, sieving the smashed biomass straw, mixing coal mud, high-quality anthracite coal, biomass straw, peat soil and lime based on the above proportions, stirring the mixture completely, filling in a molding machine after stirring uniformly, then molding in high pressure condition, and drying to obtain the product, examining, packing and storing.
NOVELTY - A fermentation pot comprises pot body, top cover, clapboard, gas-guide pipe and feeding channel pipe, where pot body is cylindrical. The clapboard is fixedly arranged at middle upper part inside pot body. The discharge channel pipe is arranged at inner side of pot body to permeate through clapboard from upside of top cover to reach to bottom part of pot body. The gas-guide pipe permeates through clapboard from upside of top cover. The feeding channel pipe permeates clapboard from upside of clapboard to reach to upper part of pot body.    USE - Fermentation pot of methane fertilizer of greenhouse (claimed).    ADVANTAGE - The pot has strong pertinence, unique structure, rational design, and short fermentation and fertilizer production period. The wastes such as dry branches and fallen leaves and residual agricultural products during production process of greenhouse serve as organic material, thus pot satisfies need of the greenhouse planting to good-quality organic fertilizer and carbon dioxide gas fertilizer and can solve pollution problem of wastes during production.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a fermentation pot.
NOVELTY - A bacterium agent comprises a liquid bacterium agent comprising a functional bacterium agent and a characteristic bacterium agent mixed at a ratio of 2-4:1.    USE - A bacterium agent used for treating urban solid waste and animal manure, and for sludge reduction (claimed).    ADVANTAGE - The bacterium agent rapidly degrades the organic waste, has an enhanced stability, and has improved functionality. It improves the activity of the general microorganism system and lignocellulose degrading bacterium in a stack when applied to waste in a compost factory, refuse processing plant, or personal processing yard. The bacterium agent accelerates combined stacking of the vegetable, flower, and straw; and shortens rotting duration.
NOVELTY - Biomass adsorbent is made of punched corn cob or straw core, which is coated with microbial agent.    USE - Biomass adsorbent useful in waste gas treatment field.    ADVANTAGE - The adsorbent uses biomass corn cob or straw core that is easy to process as special gas adsorbing material for waste gas treatment, which can effectively purify the gas generated by the compost. It has low cost; fully uses the agricultural waste source, realizing recycled utilization of agricultural wastes; and is prepared using simple device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass adsorbent comprising punching a pore canal with a diameter of 0.5-1 cm at the center of corn cob or straw core using a punching machine; directly spraying microbial agent that can decompose the harmful compound of waste gas, into the punched corn cob or straw core; and sequentially stacking the punched corn cob or straw core with microbial agent on a waste gas adsorption pipeline.
NOVELTY - Preparation of adsorbent resin includes dissolving sodium alginate and yeast peptone dextrose (YPD) culture base in water; heating and dissolving; cooling to room temperature; adding kaolin, sodium bicarbonate, and polyethylene glycol; dropwise adding the mixture in calcium chloride solution to prepare hydrophilic gel grain; heating to prepare hydrophilic gel grain of porous structure; drying the porous gel grain; cooling and feeding to saccharomycete suspension liquid; culturing via shaking bed; and obtaining polymeric adsorbent loaded with microorganism.    USE - Preparation of adsorbent resin i.e. polymeric adsorbent used for absorbing organic waste gas (claimed).    ADVANTAGE - The adsorbent resin has dual function of absorbing oil and absorbing water; can be repeatedly used; saves running cost; and does not need to be regenerated. In treatment of organic waste gas, absorption and biological treatment are integrally combined.    DETAILED DESCRIPTION - Preparation of adsorbent resin comprises:    (A) preparation of hydrophilic gel grain by dissolving sodium alginate and YPD culture base in water; heating and dissolving; cooling to room temperature; adding kaolin, sodium bicarbonate, and polyethylene glycol; dropwise adding the mixture in calcium chloride solution; and preparing gel grain;    (B) preparation of hydrophilic gel grain of porous structure by heating the gel grain; and    (C) preparation of polymeric adsorbent loaded with microorganism: drying the porous gel grain for 15 minutes at 85 degrees C; cooling and feeding to saccharomycete suspension liquid; culturing for 24 hours via shaking bed; and obtaining polymeric adsorbent loaded with microorganism.    An INDEPENDENT CLAIM is included for polymeric adsorbent.
NOVELTY - A Paenibacillus elgii (CGMCC 4231), is new.    USE - The P.elgii is useful in organic fertilizer and for preventing soil-borne diseases and plant diseases caused by bacteria and fungi, accelerating plant growth by holding water and reducing moisture loss of plant root, improving soil and promoting drought resistance.    ADVANTAGE - The P.elgii is suitable for various crops in drought area and dry season.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial inoculants containing P.elgii (108 colony forming unit (cfu)/g); and (2) organic fertilizer is obtained by inoculating 20% of P.elgii in dairy manure and other poultry excrement during decomposition, fermenting the mixture and detecting spore content of mixture during fermentation to 108 cfu/g.
NOVELTY - Improving biomass and live-weight of Gluconobacter oxydans using fermentation medium containing an oxygen carrier, comprises inoculating G. oxydans into a seed culture medium of pH 7, culturing at a constant temperature in a shaker incubator at 20-30 degrees C, and 150-220 revolutions per minute (rpm) for 20-30 hours, inoculating the obtained seed culture liquid into a fermentation medium containing the oxygen carrier and a surfactant of pH 7, culturing at constant temperature in the shaker incubator at 20-30 degrees C and 150-220 rpm for 36-48 hours, and centrifuging.    USE - The method is useful for improving biomass live weight of G. oxydans.    ADVANTAGE - The method utilizes the oxygen carrier, which increases the concentration of dissolved oxygen in the culture medium without further addition of other substances and without additional energy consumption.
NOVELTY - The prevention device has hydrogenation tank (9) with a bottom outlet that is connected with a hydrogenation raw material gas pipe (17). The gas pipe is connected with an inlet of a conversion system (13). A conversion gas pipe (15) has an end connected with an outlet of the conversion system and the other end is through the pre-heater (7) and connected in a follow-up system (8). A driving branch pipe (11) with a driving valve (10) has an end connected with the operating mode gas pipe (2) and another end is connected with the hydrogenation raw material gas pipe.    USE - Prevention device for catalyst in methane conversion furnace from analyzing carbon during driving.    ADVANTAGE - Lowers the risk of the catalyst in the conversion system from analyzing the carbon during driving which ensures a smooth driving of methane conversion system, greatly shortens the original driving time, and create conditions for reducing the catalyst after replacing the catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic of the prevention device for catalyst in methane conversion furnace from analyzing carbon during driving.    Operating mode gas pipe (2)    Pre-heater (7)    Follow-up system (8)    Hydrogenation tank (9)    Driving valve (10)    Driving branch pipe (11)    Conversion system (13)    Conversion gas pipe (15)    Hydrogenation raw material gas pipe (17)
NOVELTY - Pellet is obtained by compressing fallen leaves powder, tropical timber, powder greasy material and wood powder at high pressure and high temperature.    USE - The pellet is useful as fuel.    ADVANTAGE - The pellet has high combustion property, high thermal property, excellent fragrance and improved quality, and is economical and environmentally-friendly.
NOVELTY - The device has an oxygen concentration detection sensing probe and a methane concentration detection sensing probe whose both signal output ends are respectively connected with a CPU by a signal processing circuit. The CPU is connected with a working power supply circuit, an alarm circuit and a digital tube display.    USE - Methane and oxygen detection alarm device.    ADVANTAGE - The device has compact structure and small volume. The digital tube display is utilized which is clearer than the LCD. The user can view strong or weak light rays from outer side.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methane and oxygen detection alarm device.
NOVELTY - Preparation of bio-oil by liquefying dilignification-preprocessed biomass comprises drying biomass; crushing; mixing with water; adding dilignification reagent; regulating the pH; reacting; obtaining biomass preprocessed by dilignification; washing; drying; mixing the preprocessed biomass with solvent; conducting liquefaction reaction; collecting the product; and obtaining bio-oil.    USE - Preparation of bio-oil (claimed).    ADVANTAGE - Compared with biomass liquefaction at the same condition, but without dilignification-preprocessing, the method achieves increased bio-oil yield.    DETAILED DESCRIPTION - Preparation of bio-oil by liquefying dilignification-preprocessed biomass comprises:    (A) drying biomass until moisture content is 5-15 wt.%; crushing into 20-80 mesh; mixing with water at 1:5-1:2 weight ratio; adding dilignification reagent; regulating the pH at 2-10; reacting for 30-120 minutes at 50-180 degrees C and 0-2 MPa; obtaining biomass preprocessed by dilignification; washing; and drying; and    (B) mixing the preprocessed biomass with solvent; conducting liquefaction reaction at 180-450 degrees C and 1-20 MPa for 0-40 minutes; collecting the product; and obtaining bio-oil, where weight ratio of biomass to solvent is 3-50:45-97.
NOVELTY - A forsythoside A is prepared by extraction, alcohol precipitation, separation, purification, and enrichment.    USE - Method for preparing forsythoside A (claimed).    ADVANTAGE - The method is simple and safe, and has no pollution and more convenient production operation, which is suitable for the batch production and satisfies the industrial requirements. It has reliable and stable process data, good repeatability, and strong technique process controllability, which meets the good manufacturing practice production requirement.
NOVELTY - An electricity is generated by pre-processing plasma gas household garbage and biomass, and continuously adding into plasma reactor; using multiple plasma torches in plasma reactor to produce plasma jet flow to heat material, and adding gasification agent and slag former; storing synthesis gas which comes out from plasma reactor, and enters cooling and purifying system; and supplying pure synthesis air to generator to generate electricity, and cooling tail gas with exhaust-heat boiler and recycling rest heat, and exhausting after removing off acid air and fly ash.    USE - Method for generating electricity.    DETAILED DESCRIPTION - Electricity is generated by:    (A) pre-processing plasma gas household garbage and biomass, and continuously adding into plasma reactor;    (B) using multiple plasma torches in plasma reactor to produce plasma jet flow to heat material, adding gasification agent which is of set percentage and is pre-heated to convert organic components into synthesis gas, and adding slag former which is of set percentage to convert inorganic components into vitreous body;    (C) storing synthesis gas which comes out from plasma reactor, and enters cooling and purifying system, and is cooled by gas-water heat exchanger and is removed off acids and dust, and is removed of mist into air storing tank; and    (D) supplying pure synthesis air to generator to generate electricity, and cooling tail gas with exhaust-heat boiler and recycling rest heat, and exhausting after removing off acid air and fly ash.    An INDEPENDENT CLAIM is included for an electricity generating device which comprises pre-processing system, synthesis gas cooling and purifying system and generating system. The pre-processing system comprises multiple plasma reactors which produce plasma jet flow to heat material and convert organic components in material into synthesis gas which is processed by synthesis gas cooling and purifying system and sent to generating system.
NOVELTY - Method for preprocessing hydrolysis of lignocellulosic biomass, involves soaking and expanding lignocellulosic biomass, wet triturating the expanded biomass, and popping the biomass, where the biomass is soaked in water such that the biomass is soaked and maintained until expansion. The wet triturating step is performed by pulverizing the soaked and expanded biomass and water by a milling device, and popping step is performed by processing the wet triturated biomass under pressure of 5-25 kgf/cm2 by a popping device.    USE - The method is useful for preprocessing hydrolysis of lignocellulosic biomass for producing bioethanol (claimed).    ADVANTAGE - The method consumes less energy and improved hydrolysis efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing bioethanol, which involves hydrolyzing the biomass, saccharifying the biomass, and fermenting the saccharified biomass.
NOVELTY - The burner has an air inlet (8) and a hot air outlet (9) that are formed at opposite ends of a shell body (1). A preheat nozzle (2), a catalyzed ring (5) and a hot air heat collector (7) are orderly arranged at the inner cavity of the shell body from the air inlet end. An electrode pair (4) is symmetrically arranged in a positive and negative manner at an inner wall between the preheat nozzle and catalyzed ring. The shell body has a water inlet that is connected to a preheat nozzle through the heat air heat collector, and to a catalyst in the catalyzed ring.    USE - Burner with water decomposing capability.    ADVANTAGE - The burner uses inexpensive water as raw material for resolving to generate hydrogen and oxygen. The consumption of primary energy is reduced by adding heat generated from burning into the heat engine. Discharge of greenhouse gases and pollutants is lowered since burning of hydrogen and oxygen generates water. Affecting the fuel burning caused by the traditional water gas reaction is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the burner.    Shell body (1)    Preheat nozzle (2)    Electrode pair (4)    Catalyzed ring (5)    Hot air heat collector (7)    Air inlet (8)    Hot air outlet (9)
NOVELTY - Production-increasing fertilizer prepared from radix Lindera Chinese herbal medicine, comprises (in wt.%): dry chicken manure (8-10), dry cow dung (15-23), dry goose dung (6-8), dry human excrement (8-12), sorghum flour (4-6), bran (1-3), corn cob flour (2-4), plant ash (2-4), an organic fertilizer (8-12), nitramine (10-12), potash fertilizer (6-8), glucose powder (3-5), dipterex (1-3), a nitrogenous fertilizer (2-4) and polyurethane (4-6).    USE - Used as a production-increasing fertilizer prepared from radix Lindera Chinese herbal medicine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the production-increasing fertilizer, comprising: combining the raw materials, placing in a stirrer, stirring for 90 minutes, taking out, placing in a crusher to crush into particles with 60 meshes, then placing in the stirrer, stirring for 160 minutes, taking out, completely pouring into a fermenting vat, adding the dry human excrement in to the fermenting vat in a ratio of 1:1.5, uniformly stirring and stacking, using a plastic cloth to cover and press to ferment for 30 hours, turning the stack for the first time from an upper layer to a lower layer, and from an inner layer to an outer layer, and turning from the inner part to the outer part, again adding the dry human excrement into the fermenting vat in a ratio of 1:1.5, uniformly stirring and stacking, using the plastic cloth to cover and press so as to ferment for 45 hours, then turning the stack for the second time via the same way as the first time, stacking, fermenting for 70 hours and molding the fermented production-increasing fertilizer by placing in a mold with a height of 30 cm, width of 25 cm and length of 40 cm to obtain the product.
NOVELTY - A mixed gas comprises (in weight%) alkane gas (94-96), methanol (0.6-1.8), n-butyl alcohol (1.6-2.9), ferrocene (0.09-0.6) and petroleum ether (0.4-2.1).    USE - Mixed gas is used for welding and cutting.    ADVANTAGE - The mixed gas has high temperature, combustion value, regular flame shape and control easily.
NOVELTY - Producing chlorine-based high phosphorus composite fertilizer by ammoniation method, involves directly filling ammonia gas to material layer of a granulator, granulating monoammonium phosphate with other powdered basic fertilizer containing nitrogen, phosphorus and potassium, drying obtained granules, cooling the dried granules, and sieving and encapsulating the granules to obtain nitrogen phosphorus potassium composite fertilizer.    USE - The method is useful for producing chlorine-based high phosphorus composite fertilizer.    ADVANTAGE - The method reduces moisture content of granulating material to reduce drying load, and saves large amount of energy consumption. The fertilizer has excellent solubility and high granulation rate without adding binder, hence investment cost is reduced.
NOVELTY - Method of producing microbial manure, involves (a) preparing solid bacterial agent by fermenting bacterium, and pulverizing the fermented bacterium, (b) guniting and prilling waste amino acid into grain amino acid organic granular formulation, and (c) adding the formulation and bacterial agent into a prilling machine, scattering the bacterial agent on the surface of the organic granular formulation, adding in spray state or adhering the waste amino acid on the surface of the formulation to obtain covered bacterial agent, and drying the composite manure by cold wind.    USE - The method is useful for producing microbial manure.    ADVANTAGE - The method improves value of commodity products.    DETAILED DESCRIPTION - Method of producing microbial manure, involves (a) preparing solid bacterial agent by fermenting bacterium using culture medium in a fermenting device, and pulverizing the fermented bacterium, where the total number of viable bacterium is 3x 108/g or more, (b) guniting and prilling waste amino acid into grain amino acid organic granular formulation, and (c) adding the formulation and bacterial agent into a prilling machine in a weight ratio of 5-15%, scattering the bacterial agent on the surface of the organic granular formulation, adding in spray state or adhering the waste amino acid on the surface of the formulation to obtain covered bacterial agent, and drying the composite manure by cold wind at 120-150 degrees C, where the material temperature in drying cylinder is 80 degrees C or less.
NOVELTY - Preparation of complete methane catalyst comprises forming catalyst precursor by hydrothermal chemical synthesis; filtering; washing; drying; forming complete methane catalyst after baking and reducing; raising temperature of product after drying; adding 2-4% graphite and 2-4% cellulose to obtained product; symmetrically grinding; forming; raising temperature; and reducing under hydrogen condition to form catalyst.    USE - Preparation of complete methane catalyst.    ADVANTAGE - The method provides convenient crystal deposition of catalyst material, simple process, and good repeatability. It guarantees to satisfy current clean energy requirement. It has irreplaceable important function for reinforcement of energy/resource safety.    DETAILED DESCRIPTION - Preparation of complete methane catalyst comprising (wt.%) active component nickel (10-75), high temperature resistant carrier (10-90), and rare earth auxiliaries (0.1-15), includes forming catalyst precursor by hydrothermal chemical synthesis; filtering; washing; drying; baking and shaping obtained catalyst precursor; forming complete methane catalyst after baking and reducing at 100-180 degrees C for 1-24 hours and at reaction pressure equal to saturated steam pressure of each component raw material solution needed for synthesizing catalyst, such that dosage of water-soluble slowly released alkali is 1-16 times of quantity of alkali needed by each component deposition in raw material mixing solution for synthesizing catalyst; raising temperature of product after drying to 500 degrees C at 1-2 degrees C for 2 hours; adding 2-4% graphite and 2-4% cellulose to obtained product; and symmetrically grinding; forming; raising temperature to 500-1000 degrees C for 2-4 hours; and reducing for 4 hours at 500 degrees C under hydrogen condition to form catalyst.
NOVELTY - The electrochemical device has an electrolytic cell having electrode which is connected with a car power generator via a control system. The electrolytic cell performs electrolytic reaction to generate mixed gas of hydrogen and oxygen which is conveyed to air suction hole after passing through a gas washing purifying system for combustion with oil material. The electrode in the electrolytic cell is a compound electrode coated with a nickel or nickel alloy layer. The exposed heat radiating part of electrode is mounted with heat radiating fin and heat radiating fan connected with control system.    USE - Electrochemical device for internal combustion engine of car.    ADVANTAGE - Achieves heat radiation at low-cost since electrode material is prepared by coating active catalyst substance to an inexpensive metal and externally configuring heat radiating fins and providing a small fan. Obtains low energy consumption, high stability and long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of the electrochemical device.
NOVELTY - Agrocybe aegerita culture material comprises (mass%) dry duck manure (10-16), corn powder (24-30), dry rabbit manure (8-11), dry pig manure (6-13), wheat straw powder (3-9), cob powder (5-9), broomcorn powder (6-11), green grass powder (7-13), glucose (0.5-1), ammonium bicarbonate (5.5-9), paclobutrazol (0.5-1), and oxygenation powder (0.5-1).    USE - A. aegerita culture material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of A. aegerita culture material comprising crushing dry duck manure, corn powder, dry rabbit manure, dry pig manure, wheat straw powder, cob powder, broomcorn powder, and green grass powder into 180-mesh granules using a crusher; adding glucose, ammonium bicarbonate, paclobutrazol, and oxygenation powder; uniformly stirring the materials in a stirrer for 80 minutes; adding water at 1:1.6-1:1.8 ratio; uniformly stirring and piling the materials; pre-wetting for 48 hours before pouring the materials in a fermenting tank; fermenting the mixture for 48 hours; adding manure and water at 1:0.5 ratio; uniformly stirring the materials; piling and turning the pile once; turning the pile for 4 times every 7, 6, 5, 4, and 3 days, respectively; supplementing water at 1:0.5 ratio; fermenting the culture material; and obtaining qualified culture material.
NOVELTY - The device has two electrodes that are made to form electric field. The water supply nozzle is made of ceramic material. The electrode is provided with supporting unit and temperature controller.    USE - Water dissociating device.    ADVANTAGE - The water vapor reflux phenomenon can be overcome as well as the normal dissociation operation can be performed.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the water dissociating device.
NOVELTY - An organic compound is temporarily stored in a storage tank to form a precipitate, and pulverized. The organic compound is transferred to stable tank through a screw belt, and pulverized. Air is supplied to organic substance. A fermentation catalyst is added to the organic compound. An ejected material of stabilized and aged organic compound is discharged. The discharged organic compound is transferred through a storage bucket. The heated air is supplied to the ejected material. The fermentation product is transferred to a liquefied fertilizer aging tank.    USE - Fermentation of organic compound to produce liquid fertilizer.    ADVANTAGE - The method enables efficient fermentation of organic compound.    DETAILED DESCRIPTION - An organic compound is temporarily stored in a storage tank to form a precipitate, and pulverized. The organic compound is transferred to stable tank through a screw belt, and pulverized with a mixing blade. Air at 70 degrees C or more is supplied to organic substance to sterilize. A fermentation catalyst is added to the organic compound to stabilize. An ejected material of stabilized and aged organic compound is discharged. The discharged organic compound is transferred through a storage bucket. The heated air which is supplied through the storage bucket and which is heated by a hot air heating device, is supplied to the ejected material to ferment. The fermentation product is removed by a vacuum pump, and transferred to a liquefied fertilizer aging tank to age. An INDEPENDENT CLAIM is included for apparatus for fermentation of organic compound.
NOVELTY - The apparatus has an anaerobic digester (110) in which anaerobic digestion process of organic waste is advanced, and an exhaust guide (120) connected to bottom surface of a space portion (111) of anaerobic digester in longitudinal direction so that sludge or adulteration is accumulated in anaerobic digester among the input organic waste. The concentration of hydrogen sulfide in biogas is reduced by performing thin coloring (140) for desulfurization, in anaerobic digester wall so that the sulfation microorganism grows on water surface in the digestion tank.    USE - Lateral anaerobic absorption apparatus for use in production of biogas from sewage, effluent and excrements generated from stockbreeding farmhouse, industrial site, etc.    ADVANTAGE - The growth of sulfation microorganism is increased, and the hydrogen sulfide concentration contained in the biogas is reduced, without the need for providing desulfurization facility, so that the operating cost can be saved. Generation of blind spot in the device is prevented, and the operation and maintenance convenience and gas production efficiency are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the lateral anaerobic absorption apparatus. (Drawing includes non-English language text)    Anaerobic digester (110)    Space portion (111)    Exhaust guide (120)    Thin coloring (140)    Gas holder (150)
NOVELTY - Invention refers to remedies for environmental pollution and concerns the use of Clonostachys rosea f. catenulata (J.C.Gilman et E.V.Abbott) Schroers strain, Russian National Collection of Industrial Microorganisms No. F-991, as a biological destructor of polyvinyl alcohol (PVA). The presented Clonostachys rosea f. Catenulata 2B strain is recovered in vivo by a polyvinyl alcohol bait method from a soil sample: the Moscow Region. Lyubertsy District, fruit-tree nursery "Moscow Area Gardens"; the soil is agrogenically treated, podzolic sod, heavy loam; and the strain is deposited on 12.01.2009 in the Russian National Collection of Industrial Microorganisms, under No. F-991.    USE - Medicine.    ADVANTAGE - Use of the invention allows effective polyvinyl alcohol destruction. 1 dwg, 1 ex
NOVELTY - Method for preparing liquid fish fertilizer, involves sterilizing aqueous waste at low temperature, pulverizing sterilized aqueous waste, subjecting pulverized material to proteolysis based on aerobes, fragmenting the proteolyzed product into particle fragments and processing obtained fragments underwater vortex, where the aqueous waste is subjected to aging process and stabilized based on anaerobes.    USE - The method is useful for preparing liquid fish fertilizer (claimed) used for improving quality of seed.    ADVANTAGE - The method increases yield of fertilizer and minimizes generation of secondary contamination. The fertilizer contains organic acids and amino acids required by plants.
NOVELTY - The present invention provides two novel Cellulomonas species, which are capable of hydrolyzing cellulous and have been deposited with the Food Industry Research and Development Institute and assigned the indicated BCRC deposit numbers 910407 and 910408. The present invention further provides a method for hydrolyzing cellulous. The method includes mixing at least one Cellulomonas bacteria and cellulosic biomass, and then performing a ferment process to hydrolyze the cellulosic biomass.
NOVELTY - The present invention provides a novel method for preparing an atypical antipsychotic agent Zyprexa. The overall process which owns high recovery yield, easy operation, high safety and eliminating environmental pollution is suitable for industrial production.
NOVELTY - Method for producing hydrogen, involves producing Escherichia coli host cells transformed by hydrogenase gene and nitrogenase gene of Rhodobacter sphaeroides, and culturing the host cells.    USE - The method is useful for producing hydrogen.    ADVANTAGE - The method improves hydrogen yield by 10% or more.
NOVELTY - Method of producing amino acid fertilizer, involves extracting gibberellin fermentation liquor using solvent, separating the obtained liquid to obtain mixture of extract and raffinate, distilling the mixture to remove organic solvent, evaporating the mixture using triple effect evaporator, regulating pH of the mixture at 4-6, adding trace element to the mixture, and controlling the total trace element content of the mixture to 2% or more to obtain the amino acid liquid fertilizer, or spray-drying the mixture to obtain powdered amino acid solid fertilizer.    USE - The method is useful for producing amino acid fertilizer in the form of powder or liquid, which is used for improving disease resistance of crops.    ADVANTAGE - The method is reliable and environmentally-friendly, and produces fertilizer having excellent quality.    DETAILED DESCRIPTION - Method of producing amino acid fertilizer, involves extracting gibberellin fermentation liquor using a solvent, separating the obtained liquid to obtain mixture of extract and raffinate, distilling the mixture at 60-80 degrees C and constant pressure to remove organic solvent, recycling the solvent at concentration of greater than or equal to 95%, evaporating the mixture using triple effect evaporator, controlling the concentration cycle to 10 times or more, specific gravity to 1.5 r/ml and concentration of amino acid to 10% or more, regulating pH of the mixture to 4-6, adding trace element to the mixture, and controlling the total trace element content of the mixture to 2% or more to obtain the amino acid liquid fertilizer, or spray-drying the mixture to obtain powdered amino acid solid fertilizer.
NOVELTY - Orange peel residue biomass energy particle is obtained by squeezing orange peel residue, agriculture and forest waste, and anti-fermentation agent, and pressing mechanically.    USE - Orange peel dreg biomass energy particle used as fuel.    ADVANTAGE - The method of preparing orange peel dreg biomass energy particle makes a great number of waste peel residues produced by orange mass processing directly enter into a flow line processing system, where peel residues are processed into particle biomass energy fuel in hours. The biomass energy particle is compact, easy to store and transport, and convenient to use; and has high energy density and thermal efficiency that can reach greater than or equal to 80%. It is a clean resource product with excellent combustion characteristic and full of orange flavor; and has high burn-up rate, less ash, and low chemical pollution discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of orange peel residue biomass energy particle comprising squeezing orange peel residue at 0.6-0.8 MPa; crushing the orange peel residue into less than or equal to 3 mm; crushing the agriculture and forest waste into less than or equal to 1.7 mm; mixing the orange peel residue (30-70 wt.%), agriculture and forest waste (30-70 wt.%), and anti-fermentation agent (0.3-1 wt.%); drying at 180-220 degrees C for 35-45 minutes until water content is 12-20%; and molding and pressing the dried mixture at 40-60 degrees C into biomass energy particles by a molding machine.
NOVELTY - The model is realized by coupling flow with mass transfer and reaction, and verified the model through fluid test and waste gas purification test. An analogue result is matched with test value. The model is used for predicting local instantaneous ingredient distribution of liquid phase and solid phase, quantitatively researching relation between mass transfer and reaction and for discussing speed limiting speed of a toluene waste gas purification process of an air-lift type three-phase circulation bioreactor.    USE - Air-lift type three-phase circulation bioreactor computational fluid dynamics model.    ADVANTAGE - The model researches the dynamic behavior of fixed P.WQ-O3 odorous waste gas purification of the air-lift type three-phase circulation bioreactor on the basis of odorous waste gas purification behavior of the air-lift type two-phase circulation bioreactor and creates gas-liquid-solid three-phase flow three dimension instantaneous computational fluid dynamics model based on Euler's method to couple flow with mass transfer and reaction. The model predicts the fluid mechanical property, ingredient concentration field and speed limiting speed in the reactor, and has guide required for operation condition selection and reactor design.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an air-lift type three-phase circulation bioreactor purifying device for toluene waste gas    (2) an air-lift type three-phase circulation bioreactor purifying method for toluene waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an air-lift type three-phase circulation bioreactor purifying device for toluene waste gas. '(Drawing includes non-English language text)'
NOVELTY - Restaurant-kitchen garbage is classified and material with diameter of more than 40 mm is selected. The material is sterilized in sterilizing device by pasteurization. The grease in liquid portion is recycled using vertical centrifugal machine, to obtain methane, and ratio of recycled grease is 0.5-3% of garbage. The yield of methane is 100-700 m3/ton of dry material. Biogas residue and biogas liquid are separated using horizontal sludge dehydrator from mixed liquid, and the moisture content of the separated biogas residue is 60-70% and the solid content rate of biogas residue is 1-3%.    USE - Method for processing restaurant-kitchen garbage and producing methane.    ADVANTAGE - The method is economically enabled without affecting environment and oxidizing products.
NOVELTY - Water-based liquid formulation comprises (in wt.%): dimefluthrin (0.31-0.62), propanediol (15-20), sulfolane (10-15), hydrogenated castor oil (0.30-0.90) and deionized water (63.48-74.39).    USE - The water-based liquid formulation is useful in electric heater for repelling mosquitoes.    ADVANTAGE - The formulation uses water to replace traditional alkane solvent and thus has safe storage and transportation, and is environmentally-friendly, and prevents air pollution, and thus safe.
NOVELTY - The method involves crushing and drying the truffle waste. The splitting gas is generated by the microwave reactor through segments of condensers. The gas in the split product is condensed to prepare bio-oil. The power of microwave reactor is about 1000-12000 W and temperature is about 130-1750 degrees C.    USE - Method for preparing bio-oil by truffle waste.    ADVANTAGE - The requirements of circular economy, low-carbon and environment friendly demands can be satisfied.
NOVELTY - Method for dehydrogenating cardiac glycoside aglycone compound at 16C and 17C using Arthrobacter globiformis, involves inoculating A.globiformis into first tank containing culture medium, culturing strain, collecting seed liquid, inoculating seed liquid into fresh fermentation medium, culturing the strain, adding cardiac glycoside aglycone compound into the fermentation liquid, reacting the mixture, filtering the product, drying and concentrating dried product, and separating compound from the concentrate by silica gel column chromatography.    USE - The method is useful for dehydrogenating cardiac glycoside aglycone compound at 16C and 17C using A.globiformis.    ADVANTAGE - The method dehydrogenates glycoside aglycone compound to obtain new structure with high efficiency.    DETAILED DESCRIPTION - Method for dehydrogenating cardiac glycoside aglycone compound at 16C and 17C using Arthrobacter globiformis, involves (a) extracting A.globiformis (ATCC 31250) strain, inoculating the strains into first tank containing culture medium, culturing the strain at 30-34 degrees C and speed of 140-180 revolutions/minute (rpm) for 20-30 hours, collecting the seed liquid, inoculating 5-10% of the seed liquid into fresh fermentation medium, and culturing the strain, (b) adding cardiac glycoside aglycone compound into the fermentation liquid, reacting the mixture at 30-35 degrees C and at a speed of 150-200 rpm for 70-80 hours, and terminating the reaction, and (c) filtering the product, separating A.globiformis from fermentation liquid, repeatedly using organic solvent to extract A.globiformis from the filtrate, mixing filtrate, drying the mixture, concentrating the mixture under reduced pressure, separating the compound from the concentrate by silica gel column chromatography, and obtaining dehydrogenated product of cardiac glycoside aglycone compound.
NOVELTY - The system has inlet tube, inlet branched tube and water distribution tube located on side portion of land treatment system. The water collection branched tube, water collection tube and a drainage tube are located on another side of land treatment system. Multiple water distribution tubes are arranged vertically. The water distribution tube is penetrated through biology filler, water collection layer, and water distribution layer. The water outlet network is layered between biology filler and water collection layer.    USE - Water distribution and water collection pipe network system of sewage land treatment application.    ADVANTAGE - The pipe network system improves the volume utilization ratio of the system. The cost of water distribution and water collection pipe network system can be reduced, since the number of tubes to realize the uniform water distribution and water effluent can be reduced. The tube breakage rate can be reduced. The efficiency of water distribution and water collection pipe network system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the water distribution and water collection pipe network system.
NOVELTY - A biogas producing apparatus has an anaerobic digester for anaerobic digestion of raw material and producing biogas, solid removal unit for removing solid contained in digested liquid waste discharged from digester, carrier unit for returning discharged solid to digester, a filter for filtering treated water, and carrier unit for returning concentrate discharged from filter to anaerobic digester.    USE - Apparatus for producing biogas.    ADVANTAGE - The apparatus efficiently enables to produce biogas.
NOVELTY - The power plant has solar battery (1) to produce current that is input to a brine electrolysis hydrogen production device (4) to in turn produce hydrogen. The hydrogen is input to a container manufacturing workshop (6). The hydrogen fuel storing container conveyed from the workshop is then arranged on a solar hydrogen new energy motor-driven gardening cropper (12). Hydrogen fuel from the container is then input into the battery of the cropper. The power output shaft (11) of an electrical machine (10) outputs mechanical energy to rotate a turntable (13) to in turn drive a cutter (14).    USE - Power plant for applying solar hydrogen new energy to gardening cropper.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the components of the system by which power is supplied to the gardening cropper via a power plant.    Solar battery (1)    Brine electrolysis hydrogen production device (4)    Container manufacturing workshop (6)    Electrical machine (10)    Power output shaft (11)    Solar hydrogen new energy motor-driven gardening cropper (12)    Turntable (13)    Cutter (14)
NOVELTY - Method of producing biogas using lignocellulose, involves (a) cutting the lignocellulose raw material and subjecting the cut lignocellulose to steam explosion, (b) washing the obtained lignocellulose using water, and separating the washed raw material to obtain liquid containing sugar and solid material, (c) fermenting the obtained liquid containing sugar using microorganism to obtain biogas, and (d) processing the solid material obtained in the step (b), separating the lignin under acid environment, and drying the separated lignin to obtain product.    USE - The method is useful for producing biogas and for producing resin, mulching film, adhesive, rubber additive and drug delivery agent (claimed).    ADVANTAGE - The method can be produce biogas by simple process and is environmentally-friendly.    DETAILED DESCRIPTION - Method of producing biogas using lignocellulose, involves (a) cutting the lignocellulose raw material and adding the cut lignocellulose in steam explosion apparatus and subjecting the cut lignocellulose to steam explosion, (b) washing the obtained lignocellulose raw material using water (5-20 times with respect to raw material), and separating solid and liquid from the washed raw material to obtain liquid containing sugar and solid material, (c) fermenting the obtained liquid containing sugar using microorganism to obtain biogas, and (d) processing the solid material obtained in the step (b) using basic solution, separating cellulose product and liquid from the processed material using super filter system, separating the lignin under acid environment, drying the separated lignin to obtain lignin product, and washing the cellulose product to obtain cellulose product.
NOVELTY - Traditional Chinese medicinal yield-increasing fertilizer comprising rhizoma cyperi, includes (in wt.%): dry human excrement (4-6), dry duck manure (4-6%), dry cow manure (14-18), bean pulp powder (12-16), sorghum flour (6-8), ryegrass powder (2-4), trash fish powder (4-6), bran (2-6), corn stalk powder (4-6), ammonium bicarbonate (12-14), a nitrogenous fertilizer (8-10), a zinc fertilizer (2-4), potassium chloride (3-5), dipterex (1-3) and chloroprene rubber (4-6).    USE - Used as a traditional Chinese medicinal yield-increasing fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising: uniformly mixing the powders, stirring the mixture for 80 minutes, and grinding the mixture to obtain granules of about 100 meshes; stirring the granules for 150 minutes and pouring into a fermentation pond, fermenting for 28 hours by adding the human excrement in a proportion of 1:1.5, stirring the mixture up and down to prepare in stacks, tightly compacting the stacks and using a plastic cloth to press the stacks tightly; fermenting for 45 hours by overturning the stacks, adding the human excrement in a proportion of 1:1.5, stirring the mixture up and down to prepare in stacks, tightly compacting the stacks and using the plastic cloth to press the stacks tightly; fermenting for 76 hours by overturning the stacks, using the method which is identical to the last overturning method to process them in stacks to obtain the product; introducing the fermented yield-increasing fertilizer into a die having 30 cm height, 25 cm width and 40 cm length and compacting the product into a block-shaped yield-increasing fertilizer.
NOVELTY - Cultivation fertilizer comprises (in wt.%): dry chicken manure (10-14), dry cow dung (10-16), rapeseed cake powder (12-18), sorghum powder (6-8), peanut cake powder (6-10), bran (2-6), an organic fertilizer (15-25), tea leaves powder (1-3), a large tea branch and leaf powder (2-4), motherwort powder (1-3), Ligusticum wallichii powder (3-5), radix ophiopogonis (1-3), Coptis powder (2-4), honeysuckle powder (1-3) and safflower powder (2-4).    USE - The cultivation fertilizer is useful for planting dandelion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the cultivation fertilizer, comprising: combining all raw materials and placing into a blender, blending for 60 minutes, taking out, placing in a crusher, crushing into powder, taking out and pouring into a fermenting tank, stacking into piles, closely pressing via a plastic cloth, performing closed fermentation for 72 hours, performing the first stack overturn, adding the dry excrement in a ratio of 1:0.6 during stack overturn, uniformly stirring and stacking, tightly covering and pressing in time by using the plastic cloth during the stack overturn reaction, continuously fermenting for 72 hours, at 80 degrees C, overturning the stack for once every 72 hours, then again adding the dry excrement in a ratio of 1:0.6 during each stack overturn, uniformly stirring and stacking for 7 times to obtain the product.
NOVELTY - Straw powder-based fertilizer anticaking agent comprises (in parts by wt.) straw powder (75-9), stearic acid (0.5-5), octadecylamine (0.1-1), alcohol amine (0.1-0.5), white oil or solid paraffin wax (0.5-5) and natural oils (2-15).    USE - Used as a straw powder-based fertilizer anticaking agent.    ADVANTAGE - The anticaking agent: comprises straw as a main component, which is pure and natural, hence the agent is ecofriendly, does not cause any adverse effect on the soil, crops and farm environment after long term use, is highly efficient, does not need machine oil, is easily prepared and and is ecofriendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the straw powder-based fertilizer anticaking agent, comprising uniformly stirring the straw powder, stearic acid, octadecylamine, alcohol amine, white oil or solid paraffin wax and natural oils at 60-120 degrees C, reacting for 5-60 minutes and cooling to room temperature.
NOVELTY - Organic fertilizer comprises (in parts): peanut stems and peanut shells (100); chinaberry bark (10); calcium superphosphate (30); ammonium molybdate (0.01); and carbofuran (0.3).    USE - The fertilizer is useful for synthesizing peanut lipoproteins, killing soil insects, and promoting growth of peanut.    ADVANTAGE - The fertilizer: meets the growth requirements of peanut; improves yield and quality of peanut; and increases soil fertility, soil conditioning and probiotic in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising: (i) crushing the peanut stems and the peanut shells into powder of 100 meshes; (ii) crushing the chinaberry bark into powder of 100 meshes; (iii) mixing the materials prepared in the steps (i) and (ii), and placing into a fermenting tower to be fermented for 7-8 days; (iv) uniformly mixing the fermented material prepared in the step (iii), calcium superphosphate, ammonium molybdate and carbofuran; and (v) granulating, drying and packing for the storage.
NOVELTY - Cultivation fertilizer comprises (in wt.%): dry excrement (8-12), dry duck excrement (14-18), cottonseed cake powder (10-14), an organic fertilizer (12-16), nitrogenous fertilizer (10-14), potash fertilizer (6-10), phosphate fertilizer (2-4), Coptis chinensis powder (2-6), red-knees herb powder (1-3), pepper powder (2-6), tea leaves powder (4-8 ), pine needle powder (1-3), Aconitum powder (2-6 or 1-2) and monkshood powder (1-2).    USE - The cultivation fertilizer is useful for planting Artemisia capillaries.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the cultivation fertilizer, comprising: taking all the materials and stirring for 75 minutes by a stirrer, extracting, crushing by a crushing machine to powder, taking out and pouring into a fermenting tank, closely pressing via a plastic cloth, fermenting for 75 hours, turning the pile for the first time, adding the dry excrement in a ratio of 1:0.6, when turning the pile, adding the dry excrement, tightly covering and pressing in time by using the plastic cloth during the stack overturn reaction, continuously fermenting for 75 hours, at 80 degrees C, overturning the stack once for every 75 hours, adding dry excrement in a ratio of 1:0.6 each time, turning the pile from the upper layer to the lower layer and from the internal layer and the external layer, uniformly stirring and stacking for 7 times to obtain the cultivation fertilizer.
NOVELTY - A sludge biological fuel comprises sludge mixed together, coal powder, combustion catalyst featured with alkali metal compound, and combustion improver including vegetable fiber, turf and/or charcoal.    USE - A sludge biological fuel.    ADVANTAGE - The sludge biological fuel can reduce pollution to the environment, produce heat energy by effectively using waste such as sludge, provide new energy obtaining way, and remit energy shortage pressure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of sludge biological fuel comprising:    (A) mixing the sludge and the coal powder;    (B) adding the combustion catalyst featured with alkali metal compound, and the combustion improver featured with the combination of one or several of vegetable fiber, turf and charcoal; stirring uniformly; and    (C) shaping, drying and screening the mixture.
NOVELTY - Disease and insect resisting bacterium fertilizer comprises (kg) plant straws (380-420), dry chicken manure (80-120), shale (180-220), bran (60-100), bone powder (40-60), fish powder (40-60), bean pulp (80-120), water (500-580), fermenting bacterium (8-12), and toosedarin (18-22).    USE - Disease and insect resisting bacterium fertilizer used as replacement for manure, for promoting maturity of crops and resisting infection.    ADVANTAGE - The fertilizer provides no pollution to environment; increases production yield; has wide raw material sources and simple and convenient preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of disease and insect resisting bacterium fertilizer comprising preparing all components as raw materials, except toosedarin; fermenting the raw materials at normal temperature; turning the raw materials until the third day of fermentation and drying once at lower than 70 degrees C; turning the raw materials until the fifth day of fermentation and drying once at lower than 70 degrees C; drying the raw materials at 60-70 degrees C until the seventh or eighth day of fermentation; adding toosedarin and water-retaining agent; mixing uniformly; and packaging.
NOVELTY - A system and method for harnessing biogas energy from farm waste/food waste/cow dung/any agricultural and organic waste, are disclosed. The biogas digester is made of a flexible polyester fabric, coated with polyvinyl chloride (PVC) in glossy finish. Cow dung/any other organic input is mixed with water and added to the digester which is then fermented, to generate biogas. The digested slurry is also obtained which can be used as rich organic manure. Image 0/0
NOVELTY - A composite material comprises polyethylene terephthalate/silver-silver salt.    USE - Composite material is used as antibacterial material (claimed).    ADVANTAGE - The composite material has excellent antibacterial property, and can be manufactured economically, by a simple process without polluting the environment.    DETAILED DESCRIPTION - A composite material comprises polyethylene terephthalate/silver-silver salt (AgX)    X=chloro, bromo, iodo or acetate.    An INDEPENDENT CLAIM is included for preparation of composite material, which involves preparing precursor of soluble silver salt-ethylene glycol colloidal solution using precipitator, performing esterification and polycondensing.
NOVELTY - A polyatomic alcohol modulation for preparing platinum on carbon catalyst comprises heating platinum bis(acetylacetonate) in a diphenyl ether solvent to dissolve at 80-120 degrees C in the presence of nitrogen gas; adding surfactants oleic acid and oleamide as a stabilizing agent; adding the treated carbon black into the solution and stirring for 1-3 hours; adding a reducing agent polyatomic alcohol while stirring condition and heating and refluxing for 0.5-1 hour to reduce acetyl acetone to platinum; and filtering the solution, washing by absolute ethyl alcohol and vacuum drying.    USE - Method for polyatomic alcohol modulation for preparing platinum on carbon catalyst (claimed) used for hydrogen-oxygen fuel cell.    ADVANTAGE - The catalyst has high electro-catalysis activity in a hydrogen-oxygen fuel cell. The prepared catalyst has small grain size, good dispersity, and uniform size distribution. The average grain size of a transmission electronic microscopy effect drawing of the catalyst is 2.3 mm.
NOVELTY - The method involves providing a combination of combustible and flammable cellulose polymer compounds, where the combustible material is selected from one of cellulose, polymer, petroleum waxes, metal salt of a fatty acid such as magnesium or aluminum stearate, sodium bicarbonate contained inorganic salt, hydroxide, sodium, and potassium. The flammable cellulose derived from organic sources such as wood flour and sawdust.    USE - Method for obtaining a combustible material i.e. artificial fire log, from flammable cellulose combined with polymer compounds and synthetic polymers such as fatty acid esters and fatty alcohols, to be utilized in an artificial fireplace at home.    ADVANTAGE - The method allows deriving the flammable cellulose with low toxic binder material from the organic sources so as to make the combustible material to be affordable and efficient to use while reducing carbon emission during burning.
NOVELTY - An azasetron percutaneous paste comprises a back lining layer, a medicine storage and an anti-adhesive layer. The medicine storage comprises (wt.%) azasetron (1-15), pressure-sensitive adhesive (70-90) and percutaneous absorption enhancer (0.5-20).    USE - Azasetron percutaneous paste.    ADVANTAGE - The percutaneous paste can avoid stimulation of oral formulation for gastrointestinal tract; has low toxic side effect, and stable curative effect; and is convenient to use and store, good in flexibility and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the azasetron percutaneous paste, comprising:    (A) mixing azasetron with pressure-sensitive adhesive and percutaneous absorption enhancer;    (B) transferring to coat on anti-adhesive layer;    (C) drying at 40-80 degrees C; and    (D) combining with a mounting material of PVC or nonwoven fabric, then punching until forming a certain size and standard.
NOVELTY - Producing nanocrystalline zeolite form coal ash, comprises melting coal ash and sodium hydroxide at a high temperature, mixing the molten coal ash in condensed sea water, and aging to obtain silica-alumina gel, performing hydrothermal crystallization of the silica-alumina gel, washing to be neutral, and drying, where coal ash is used as a raw material.    USE - The nanocrystalline zeolite is useful in catalyst, absorption, ion exchange and soil improvement.    ADVANTAGE - The method recycles the coal ash and condensed sea water, and hence it is environmental friendly method.
NOVELTY - The apparatus has cylindrical wall structure (102) positioned at upper portion of floor and main structure (100). The gas exhaust port (20) is connected to combustion device, so that gas stored at gas holder is supplied to combustion device. The side terminals of hot water supply pipe are provided with warm water supply unit (60) installed at outer structure. The warm water supply unit is provided at side terminals of hot water supply pipe, while ejecting warm water from feed port (61) of warm water supply unit to exhausting portion.    USE - Non-welding type integrated fermenting apparatus of organic waste such as food waste and livestock excretion for producing biogas.    ADVANTAGE - The stable operation of the non-welding type integrated fermenting apparatus is achieved. The maintenance cost of the apparatus is reduced efficiently. The fermenting process of organic waste is performed effectively in short duration.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial side cross-sectional view of the non-welding type integrated fermenting apparatus.    Gas exhaust port (20)    Warm water supply unit (60)    Feed port (61)    Main structure (100)    Cylindrical wall structure (102)
NOVELTY - The manufacturing facility has rotary apparatus (2) for rotating and agitating the pinnule which is dried in dryer room of dryer (1) for preset temperature. A fermenting device (3) adds water, additive and yeast and ferments yeast in agitated pinnule to obtain dye. A control device (4) controls and transfers the dye to next apparatus through material transfer unit (5) according to preset condition.    USE - Automatic fermentation indigo dye manufacturing facility.    ADVANTAGE - The fermentation indigo dye can be manufactured automatically.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic fermentation indigo dye manufacturing facility.    Dryer (1)    Rotary apparatus (2)    Fermenting device (3)    Control device (4)    Material transfer unit (5)
NOVELTY - A depressant contains terpolymer obtained by mixing ester-type monomer (I), carboxyl-type monomer (II) and furan-2,5-dione monomer in presence of maleic anhydride and comonomer.    USE - Depressant is used for biodiesel.    ADVANTAGE - The biodiesel using the depressant has improved mobility and cold-filter plugging point.    DETAILED DESCRIPTION - A depressant contains terpolymer obtained by mixing ester-type monomer of formula: CH2=CR1-COOR2 (I), carboxyl-type monomer of formula: CH2=CR1-COOR3 (II) and furan-2,5-dione monomer in presence of maleic anhydride and comonomer.    R1=H or methyl;    R2=1-30C alkyl;and    R3=6-30C alkyl.    An INDEPENDENT CLAIM is included for manufacture of terpolymer.
NOVELTY - Invention relates to technology for breeding culture of earthworms in nutrient medium. Compost is prepared, for this purpose organic material is ground: tree waste or sunflower husks or fruit cake, etc, which is treated with milk whey at the following ratio of components: 40-80 l of milk whey per 1 t of organic material, is left for fermentation at the temperature of 19-35 degrees C. Compost is mixed with black soil or sapropel at the components ratio of 4: 1 wt parts. Then mixture is treated with crude oil at the ratio of components: 1 wt % of oil per 100 wt % of produced mixture. Treated mixture is populated with native types of red earthworms in amount of 25-30 individuals per 1 kg of mixture into layer of 25-40 cm thickness. Worms are additionally fed on a weekly basis. Maintained in cultivator for three cycles of development, every of which lasts for 140-180 days at the optimal moisture of medium.    USE - Agriculture.    ADVANTAGE - Invention makes it possible to produce earthworms, capable of preserving survival rate in medium-contaminated substrates within the limits of 93-98%, in highly-contaminated - 60-80%. 5 cl, 1 dwg, 3 ex
NOVELTY - Invention relates to agriculture and ecology, namely, livestock, and can be used for disinfection of manure effluents and odor control at facilities of pig-breeding complexes. The method consists in preparation of aqueous solution of microbial preparation Tamir at a ratio of 1:9 and the area of industrial premises is treated by spraying at the rate of 0.3 l of the resulting solution per 1 m2 of the area, and with the method of application liquid manure at the rate of 10 litres of the resulting solution per 5 m3 of manure followed by separation of manure effluents into liquid and solid fraction.    USE - Agriculture.    ADVANTAGE - Invention enables to improve rheological properties of liquid manure, as well as microclimate at pig-breeding complexes. 1 tbl
NOVELTY - A nickel-iron hydrogenase protein isolated from Hydrogenovibrio marinus comprising a 593 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The nickel-iron hydrogenase protein is useful for developing biosensor and biofuel cell, and as an electrical catalyst.    ADVANTAGE - The protein has high purity and resistance to biocorrosion, and is prepared simply.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the above-mentioned protein;    (2) recombinant vector comprising the above-mentioned gene;    (3) microorganisms transformed by the above-mentioned vector; and    (4) method of producing hydrogen, involves cultivating transformed microorganism in presence of nickel-iron under microaerobic condition.
NOVELTY - A recombinant vector comprising hyaA and hyaB gene among Escherichia coli NiFe hydrogenase 1 operon, is new.    USE - The recombinant vector is useful for producing methane (claimed) which is used in biosensor and biofuel cell and as electrocatalyst.    ADVANTAGE - The method is environmentally-friendly and enables production of methane with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microorganism in which the vector is transformed; and    (2) method for producing hydrogen, involves transforming the microorganism with the recombinant vector, and culturing the transformed microorganism in a culture medium containing nickel and iron.
NOVELTY - The system has a feeding unit (120) supplying a material e.g. reducing agent and oxidizer, to a main fuel cell (110). A reproducing unit (150) removes moisture and impurity in inner side of the main fuel cell. A sensing unit (140) reads reducing agent ejected from the main fuel cell. A control unit (160) controls operation of a clean up unit and the feeding unit. A return duct guides unreacted substance from a sacrifice fuel cell. A manometer measures pressure in inner side of the sacrifice fuel cell. An ammeter measures current generated in the sacrifice fuel cell.    USE - Encapsulated type fuel cell system.    ADVANTAGE - The system removes moisture and impurity, and improves durability of the main fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an encapsulated type fuel cell system.    Main fuel cell (110)    Feeding unit (120)    Sensing unit (140)    Reproducing unit (150)    Control unit (160)
NOVELTY - The furnace has a combustion chamber (14) arranged at an internal lower part of a furnace barrel (1). A circular air returning air flue (5) is formed between the combustion chamber and the furnace barrel. An upper part of the combustion chamber is provided with a ring of air nozzles (6), and a top part of the furnace barrel is provided with a ring of water sealing grooves (8). A sealing cover (9) is installed with an air conveying pipe (10) that is vertically extended into a purifier (2), where the purifier is vertically installed with a purification pipe (12).    USE - Biomass straw gasification furnace.    ADVANTAGE - The furnace can self-discharge waste water and combust for ten hours by adding fuels at a time. The furnace combusts dray and wet materials that are fed and combusted randomly with fire power greater than 1000 degree Celsius. The furnace is simple to operate, and ensures effective combustion for three furnace heads for every 5 to 8 days.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass straw gasification furnace.    Furnace barrel (1)    Purifier (2)    Circular air returning air flue (5)    Air nozzles (6)    Water sealing grooves (8)    Sealing cover (9)    Air conveying pipe (10)    Purification pipe (12)    Combustion chamber (14)
NOVELTY - A hydrogen gas generating apparatus (10) comprises: a housing (12) having a fixed interior volume; an expandable reaction chamber (14) within the housing comprising a moveable partition defining an expandable reactant zone (75) and containing a solid reactant component (24) within the reactant zone; a collapsible receptacle within the housing containing a liquid reactant component (26); a fluid path for transporting the liquid reactant component from the collapsible receptacle to the reactant zone of the reaction chamber; and a liquid reactant transport control system.    USE - The apparatus is useful for generating hydrogen gas (claimed).    ADVANTAGE - The hydrogen gas generating apparatus efficiently provides hydrogen gas to a fuel cell stack.    DETAILED DESCRIPTION - A hydrogen gas generating apparatus comprises: a housing having a fixed interior volume; an expandable reaction chamber within the housing comprising a moveable partition defining an expandable reactant zone and containing a solid reactant component within the reactant zone; a collapsible receptacle within the housing containing a liquid reactant component; a fluid path for transporting the liquid reactant component from the collapsible receptacle to the reactant zone of the reaction chamber; and a liquid reactant transport control system; where the liquid reactant component reacts with the solid reactant component within the reaction chamber to generate hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional schematic view of a hydrogen gas generating apparatus.    Hydrogen gas generating cartridge (10)    Housing (12)    Reaction chamber (14)    Bladder (16)    Fuel ports (18)    Connector end (20)    Follower (22)    Solid reactant component (24)    Liquid reactant component (26)    Fill port (28)    Liquid feed valve assembly (30)    Single or multiple liquid feed tubes (32)    Cap (34)    Spring (36)    Vent tube (60)    Reactant zone (75)
NOVELTY - A method for biohydrogen gas production is presented. The method comprises the following steps: (a) a bacterial species cultivation step: calturing a Clostridium bacteria or a mixed bacteria with at least one Clostridium bacteria as bacterial species; (b) a mixture step: disposing the bacterial species and the calture medium into a reactor providing an anaerobic environment and mixing them to obtain a fermentable solution; (c) a dark fermentation step: subjecting the fermentable solution to an dark fermentation and an ultrasonic treatment, so as to obtain a hydrogen gas.
NOVELTY - Preparing an imine, comprises using a green solvent.    USE - The method is useful for preparing an imine, which is aldimine, preferably an aryl aldimine (all claimed).    ADVANTAGE - The method: prepares imine in a short time using green solvents, thus the method is environmentally friendly; and purifies imine without the need for recrystallization or without the need for evaporating remaining solvent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) forming an imine comprising using a polarity-tuned co-solvent; and    (2) determining the optimal polarity of the solvent in forming aryl aldimine comprising: mixing aryl amine and aryl aldehyde in a green solvent; determining the yield of the resulting aryl aldimine; and modifying the polarity of the solvent, so as to optimize the yield of the resulting aryl aldimine.
NOVELTY - Treating aqueous organic waste or by-product streams, comprises passing an organic waste or by-product stream comprising soluble and insoluble solids through a biodigester reactor, and subjecting the stream to a pervaporation separation using a membrane which permits only water vapor to be transported through it to generate from it an essentially contaminant free water stream and a stream containing an increased dry matter content as compared to the stream immediately prior to the pervaporation separation.    USE - The method and process plant are useful for treating aqueous organic waste or by-product streams (claimed).    ADVANTAGE - The method is environment friendly, and provides a water stream associated with a bio-digester process plant that is essentially contaminant free and aseptic.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) process plant for treating aqueous organic waste or by-product streams, comprising a biodigester reactor for treating an organic waste or by-product stream comprising soluble and insoluble solids and a pervaporation separation unit comprising a membrane which permits only water vapor to be transported through it and from which an essentially contaminant free water stream and a stream containing an increased dry matter content as compared to the stream immediately prior to the pervaporation separation may be generated; and    (2) an aseptic fertilizer product comprising a bio-digester reactor digestate having a dry matter content of at least 20% by weight.
NOVELTY - The system has a plasma discharge vessel (100) continuously placed at an aerobic vessel (30). A waste sludge conveyor pipe (110) transfers sludge ejected from the aerobic vessel into the plasma discharge vessel. A sludge conveyor pipe (120) transfers sludge byproducts electrically discharged from the plasma discharge vessel into an anoxic vessel (20). The aerobic vessel includes a submerged-type membrane (90) of a membrane bioreactor (MBR). A unit selectively manages discharged sludge mode operation of the plasma discharge vessel installed with the submerged-type membrane.    USE - Fouled/waste water advanced treatment system.    ADVANTAGE - The system generates radicals and ozone that has high oxidizing power by aqueous high voltage discharge of plasma making sludge soluble by enabling the radicals and ozone to act as a powerful oxidizing agent against sludge made by the system, thus reducing the amount of sludge. The anoxic vessel supplies external carbon source such as methanol, separately during treatment procedure as the system conveys solublized sludge into the anoxic vessel, which is to be recycled, thus reducing sludge disposal cost and system management cost. The system oxidizes a cake layer formed on the membrane surface of the membrane bioreactor using each type of radical and ozone including high oxidation power produced by plasma, thus controlling contamination of the membrane. The system is easy and simple to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a membrane combined-type fouled/waste water advanced treatment system with a plasma discharge vessel in drive mode.    Anoxic vessel (20)    Aerobic vessel (30)    Submerged-type membrane (90)    Plasma discharge vessel (100)    Waste sludge conveyor pipe (110)    Sludge conveyor pipe (120)
NOVELTY - An electrical energy generating comprises a first component, which can be a sintered porous metal plate or a reticulate metal plate, comprising a metal having void volume and partially exposed to a reaction medium during use; and a second component comprising reactive metal nanoparticles suspended in reaction medium and diffused through the first component when the device is in use. The device comprises an electrolysis cell where reaction products are produced when energy is applied.    USE - Electrical energy generating device for use in electrochemical and/or catalytic application for generating hydrogen from water.    ADVANTAGE - When reactive metal particles are diffused into the electrode structure and suspended in electrolyte by gasses, a fluidized bed is established, thus reaction efficiency is increased and products can be produced at a higher rate. When an electrolysis device can be operated such that incoming reactants and outgoing products enter and exit from opposite faces of an electrode, reaction rate and efficiency are improved. Ideally, the device can be used to rapidly produce significant quantities of high purity hydrogen gas with minimal electricity cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view improved electrolysis device.    Electrolyte (201)    Cathode electrode (204)    Separator membrane (207)    Anode electrode (209)    Outlet port (210)    Inlet port (211)
NOVELTY - The system (5) has a feed hopper (10) comprising a flow measurement device. A reactor (15) is operable in a gasification mode or a pyrolysis mode, where the reactor receives a biomass feedstock from the hopper. The reactor is operable to provide heat to the biomass feedstock from the hopper for producing synthesis gas i.e. syngas (70) and bio-char i.e. char. The produced synthesis gas comprising the bio-char is fed into a cyclone assembly (25) that removes the bio-char from the synthesis gas. A reactor bed (20) of the reactor is fluidized by a fluidizing medium input.    USE - Pyrolysis and gasification system for producing synthesis gas and bio-char from a biomass feedstock such as cotton gin trash e.g. pulverized cotton gin trash and raw cotton gin trash, switch grass, sorghum, sludge, straw, rye, wood chips, poultry litter and dairy manure.    ADVANTAGE - The system effectively converts the biomass. The system comprises a gap to allow the removal of excess heat from the reactor to heat the incoming air with improved efficiency. The system is operated in a continuous mode without use of external power. The system is plugged into an operational fluidized bed gasifler so as to avoid the external heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasification and pyrolysis of a biomass feecistock in a reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a pyrolysis and gasification system.    Pyrolysis and gasification system (5)    Feed hopper (10)    Reactor (15)    Reactor bed (20)    Cyclone assembly (25)    Syngas (70)
NOVELTY - Fuel oil composition comprises biodiesel oil and at least one additive for improving the filterability.    USE - The fuel oil composition, polyalkyl (meth) acrylate polymer, or method is useful for improving filterability of fuel oil (claimed).    ADVANTAGE - The invention provides composition having improved filterability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for improving the filterability of fuel oil comprising biodiesel where an additive for improving the filterability is added to the fuel oil composition.
NOVELTY - A hydrogen production apparatus comprises reforming reactor (100) faced between louvers (110) (armor-shape wall) which is filled with modification catalyst (120), pressure swing adsorption apparatus which separates and recovers hydrogen gas, carbon monoxide modifying device which transforms carbon monoxide gas in extraction gas, and source gas supply device which supplies steam and hydrocarbon fuel to reforming reactor inlet port by fixed ratio.    USE - Hydrogen production apparatus.    ADVANTAGE - The hydrogen production apparatus has simple structure.    DETAILED DESCRIPTION - A hydrogen production apparatus comprises reforming reactor (100) faced between louvers (110) (armor-shape wall) which is filled with modification catalyst (120), circulating gas fan (200) for circulating reactive gas, circulating gas temperature rising device (300) which heats up circulating gas to reaction temperature, pressure swing adsorption apparatus which separates and recovers hydrogen gas, carbon monoxide modifying device which transforms carbon monoxide gas in extraction gas, source gas supply device which supplies steam and hydrocarbon fuel to reforming reactor inlet port by fixed ratio, primary pressure control valve for extracting generated gas, and extraction gas waste heat boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the hydrogen production apparatus by reactive gas circulation. (Drawing includes non-English language text).    Reforming reactor (100)    Louver (110)    Modification catalyst (120)    Circulating gas fan (200)    Circulating gas temperature rising device (300)
NOVELTY - Biomass fuel is manufactured by carbonization process which heats the sewage sludge biomass in low oxygen concentration atmosphere, gasifies greater than or equal to 92% volatile matters contained in the biomass and produces carbonized material, and cooling process which cools to a predetermined temperature without humidifying the carbonized material.    USE - Manufacturing method of biomass fuel e.g. biomass charcoal (claimed).    ADVANTAGE - Substance temperature raise by hydration and self-heating property are suppressed, stability during storage, preservation and transport is very high, transport cost is reduced, simple apparatus is used, fuel does not adhere to the apparatus and maintenance overhead cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass charcoal processing system (10) comprising carbonization furnace (11) which carbonizes sewage sludge biomass to produce carbonized material, cooling unit (20) which cools carbonized material at a predetermined temperature without humidifying, storage tank (15) which stores the cooled carbonized material, and discharge part (16) installed in the storage tank which discharges the stored carbonized material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biomass charcoal processing system. (Drawing includes non-English language text).    Biomass charcoal processing system (10)    Carbonization furnace (11)    Dust collector (12)    Volumetrical feeder (13)    Filter (14)    Storage tank (15)    Discharge part (16)    Delivery container (17)    Cooling unit (20)    Screw conveyer (21)    Air flow cooler (22)
NOVELTY - Hydrogen is added to the process target gas containing methane as main component and oxygen as impurity. The content of oxygen in the process target gas is reduced by reacting oxygen contained in process target gas and hydrogen for predetermined time in presence of catalyst.    USE - Processing of gas e.g. biogas used as fuel for boiler, generator and automobiles.    ADVANTAGE - The processing of gas is effectively enables, thus the content of oxygen in gas is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of removing oxygen from gas, which involves pre-heating process target gas containing carbon monoxide at 150 degrees C or more and reacting oxygen and hydrogen; and    (2) processing apparatus, which has reactor (2) filled with catalyst and flow path (3) which introduces hydrogen to the process target gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for processing of gas.    Reactor (2)    Flow path (3)    Gas supply source (5)    Hydrogen supply source (7)
NOVELTY - Method for fermenting waste tea grounds to prepare methane, involves (a) mixing the waste tea grounds with water, and (b) reacting in anaerobic condition to obtain methane.    USE - The method is useful for fermenting waste tea grounds to prepare methane in the form of slag or liquid used as fertilizer (all claimed) and in power generation.    ADVANTAGE - At least 2 kg of waste water can be consumed by each kg of waste tea grounds to produce 0.12 m3 of methane. The heating value of methane is 20000-23000 KJ/m3, which is equivalent to the heating value produced by burning 0.7 kg of fuel coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane in the form of slag or liquid obtained by the above-cited method.
NOVELTY - Enhancing reactivity of a moist fuel in a device for producing cement, comprises: compressing (1a) feeding air followed by heating (1b) the compressed feeding air in a heat exchanger; crushing (2a) the moist fuel in a crushing device; supplying (c) the crushed fuel into the compressed feeding air; and transporting (d) the crushed fuel with the compressed feeding air to a burner. The heating of the compressed feeding air is carried out through the waste heat of a clinker cooler provided in the device for producing cement.    USE - The method is useful for enhancing reactivity of a moist fuel.    ADVANTAGE - The method: improves ignition and uniformity of the burning properties of the fuel, and thus it increases the reactivity of low fuels, preferably the moist fuel at low cost; prevents emissions of nitrogen oxides by controlling the temperature of the tertiary air pipe and subsequently controlling the temperature level in a calcinator; and avoids formation of caking of the moist fuel in the crushing device, and thus it does not affect the output of the crushing device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the method, comprising a compressor for the feeding air; the heat exchanger following the compressor; the crushing device for the moist fuel; a supplying device for supplying the crushed fuel into the compressed and heated feeding air; and the burner, where the heat exchanger is arranged in a primary or a secondary exhaust pipe of the clinker cooler provided in the device for producing cement.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method.    Compressing step (1a)    Heating step (1b)    crushing step (2a)    Supplying step (c)    Transporting step (d)
NOVELTY - Synthesis method of multi-purpose self-adjusting catalyst for liquid-phase low-temperature oxidation cracking of organic raw material, including natural biomass, is described, and it consists in the fact that iron salt FeCl3 x 6H2O is dissolved in water containing lower alcohol in concentrations required for formation of colloid system capable of peptisation, at heating up to the temperature not exceeding 100 degrees C and constant mixing so that suspension of colloid solid particles of iron oxides containing organic impurities is obtained. The above suspension can change its activity depending on type of organic raw material and oxidiser, and at cracking of natural biomass and in case the latter represents lignine or lignine-containing biomass it has properties of ferments in relation to lignine. Method of liquid-phase low-temperature oxidising cracking of organic raw material, including natural biomass, in presence of catalyst at atmospheric pressure is described. At that, air oxygen and/or hydrogen peroxide is used as oxidiser and the above catalyst is used as catalyst.    USE - Oil and gas industry.    ADVANTAGE - High-activity catalyst of liquid-phase oxidising cracking. 8 cl, 7 dwg, 11 ex
NOVELTY - Precipitating calcium and optionally, other divalent cations, contained in brine originating from desalination plants as carbonates and simultaneously achieving sequestration of carbon dioxide using halotolerant microorganisms having a carbonic anhydrase activity, is claimed.    USE - The method is useful for precipitating calcium and optionally, other divalent cations, contained in brine originating from desalination plants and achieving sequestration of carbon dioxide using halotolerant microorganisms, where the brine is useful as feedstock in aerobic water treatment units, the precipitated carbonate slurry is useful as source of raw material in a soda ash process, the calcium cured brine as sodium (Na+) is useful as source in a soda ash process, and the halotolerant microorganisms having a carbonic anhydrase activity is useful for promoting and/or accelerating both the generation of bicarbonate and carbonate ions from carbon dioxide and carbonate precipitation with divalent cations contained in brines (all claimed).    ADVANTAGE - The method precipitates calcium and other divalent cations with reduced carbon dioxide emissions in an economical manner. The method is energy efficient and an ecologically friendly.
NOVELTY - Process for the removal of salts and surfactants from wastewaters or effluents, involves contacting a fungal biomass with the wastewaters or effluents for a period of time to enable the absorption of the salts and surfactants, where the fungal biomass comprises the fungal species Cunninghamella elegans (Lendner).    USE - For the removal of salts (preferably sodium chloride, sodium sulfate, sodium nitrite and ammonium chloride) and surfactants (preferably anionic, cationic, non-ionic and amphoteric surfactants including ethoxylated alkylphenols, ethoxylated nonylphenols, alkylbenzenesulfonates, perfluoro-octanesulfonic acid or perfluoro-octanoic acid) from wastewaters or effluents; and for the reduction of the ecotoxicity of wastewaters or effluents (all claimed).    ADVANTAGE - The process provides the wastewaters of effluents containing salts at a concentration of 1-100 g/l. The process reduces the ecotoxicity of wastewaters or effluents by at least 50% (preferably by at least 70%, especially at least 80%) according to the algae test with monospecies culture of Pseudokirkneriella subcapitata and the UNI EN ISO 8692:2005 standard. The process is quick; and allows more effective biological treatment, which, in turn, could reduce the need for expensive tertiary treatments. The Cunninghamella elegans (Lendner) biomass in the process shows an extraordinary versatility in adsorbing different molecules as both salts and surfactants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the reduction of the ecotoxicity of wastewaters or effluents involving contacting a fungal biomass with the wastewaters or effluents for a period of time.
NOVELTY - The method (20) involves machining a portion producing the tailings including the natural flake graphite. The tailing is mixed (24) with a material including the specific natural flake graphite, to produce a mixture. The mixture is formed (26) into a fuel cell plate. The binder made of fluoropolymer, is laminated at the natural flake graphite material.    USE - Method for manufacturing fuel cell plate (claimed) for fuel cell e.g. phosphoric acid fuel cell.    ADVANTAGE - The tailings are provided with the natural flake graphite that is laminated with the binder that is used to produce the fuel cell plate, so that the thermal conductivity of fuel cell plate can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the process for manufacturing fuel cell plate.    Method for manufacturing fuel cell plate (20)    Step for providing tailings (22)    Step for mixing tailing with material (24)    Step for forming fuel cell plate (26)    Step for cutting flow field (32)
NOVELTY - Method for producing isobutanol, involves obtaining fermentation medium comprising carbon substrate, and contacting the medium with recombinant yeast capable of expressing an engineered isobutanol biosynthetic pathway, where the pathway involves substrate to product conversions chosen from (a) pyruvate to acetolactate, (b) acetolactate to 2,3-dihydroxyisovalerate, (c) 2,3-dihydroxyisovalerate to alpha -ketoisovalerate, (d) alpha -ketoisovalerate to isobutyraldehyde, and (e) isobutyraldehyde to isobutanol.    USE - The method is useful for producing isobutanol (claimed). The isobutanol is useful as biofuel or fuel additive, feed stock chemical in plastic industry, foodgrade extractant in food and flavor industry, and for beverage fermentation.    ADVANTAGE - The method enables mass production of isobutanol cost-effectively and environmentally-friendly.    DETAILED DESCRIPTION - Method for producing isobutanol, involves obtaining fermentation medium comprising carbon substrate, and contacting the medium with recombinant yeast capable of expressing an engineered isobutanol biosynthetic pathway, where the pathway involves substrate to product conversions chosen from (a) pyruvate to acetolactate, (b) acetolactate to 2,3-dihydroxyisovalerate, (c) 2,3-dihydroxyisovalerate to alpha -ketoisovalerate, (d) alpha -ketoisovalerate to isobutyraldehyde, and (e) isobutyraldehyde to isobutanol. The enzymes involved in the above substrate to product conversions are chosen from (i) acetolactate synthase enzyme for step (a), (ii) acetohydroxy acid isomeroreductase enzyme for step (b), (iii) acetohydroxy acid dehydratase enzyme for step (c), (iv) decarboxylase enzyme for step (d), and (v) alcohol dehydrogenase enzyme for step (e).
NOVELTY - The device has a static coke-removing device connected to a roots blower, where the roots blower is connected to a gas purification device. A circulating water system and a cyclone dust collector are connected to the gas purification device. The cyclone dust collector is connected to a gasification furnace and a rice-hull fuel tank. The gasification furnace is connected to an ash pipe and the rice-hull fuel tank, where the ash pipe is connected to a dry ash chamber.    USE - Rice-hull generating device.    ADVANTAGE - The device utilizes rice hull to replace fossil fuel so as to reduce discharge of carbon dioxide greenhouse gas and save electric charge. The device is inexpensive, environmental-friendly and simple and convenient to maintain.
NOVELTY - Environment cleaning method, involves using first atomization portion capable of producing first fine particles (P1) comprising an acidic aqueous hypochlorous acid solution (S1) and second atomization portion capable of producing second fine particles (P2) comprising an alkaline aqueous hypochlorous acid solution (S2).    USE - The method is useful for cleaning environment by inactivating or eliminating microorganisms including virus and bacteria.    ADVANTAGE - The method is effective as the alkaline solution reacts with organic substances while enabling the acidic solution to inactivate or eliminate microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for environment cleaning device, which comprises the above-cited first and second atomization portions.
NOVELTY - Biogas production process with enzymatic pre-treatment comprises: (a) providing a slurry comprising a lignocellulose-containing material, water and at least one enzyme; (b) allowing the enzyme to degrade the lignocellulose-containing material at a suitable temperature and pH; and (c) adding the enzyme-degraded material to a biogas digester tank at a suitable rate and ratio to convert the material to biogas in the digester.    USE - The process is useful for producing biogas with pre-enzymatic treatment.    ADVANTAGE - The process: provides higher conversion rate and higher productivity per unit of volume in the digester tank; utilizes low cost tank; provides higher gas production per tank volume; allows for more efficient conversion of the lignocellulosic material at higher dry matter concentration; reduces amounts of unconverted material in the purge; provides higher dry matter content in the unconverted solids; does not require post-converter or storage tank; and allows for easier dewatering of unconverted material and easier cleaning of the gas phase.
NOVELTY - Producing a catalyst, comprises (a) producing an aqueous suspension comprising red mud and at least one calcium salt, (b) heating the suspension to a temperature of 25-78 degrees C, and (c) removing at least most part of an aqueous phase from a solid product mixture produced in step (b), where the solid product mixture comprises the catalyst.    USE - The catalyst is useful for cracking organic carbon compounds such as kerogen, coal, tar, oil and/or biomass. The carbon monoxide, hydrogen and/or methane comprising reaction product is useful for performing a Fischer-Tropsch process, a gas-to-liquids process and/or for operating a heating plant. The magnetic reaction product is useful for production of metallic iron and/or its alloy as fertilizer and/or the solid non-magnetic reaction product is useful as a mineral additive, a soil conditioner, a clarifying agent, a cement additive, a building material and/or as mineral fertilizer. The solid reaction product separated in step (c1) is used as a filter element, preferably for the filtration of vegetable oil and/or polluted water (all claimed).    ADVANTAGE - The process produces the catalyst in an inexpensive manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the catalyst, obtained by the above process; and    (2) cracking at least an organic carbon compound using the catalyst, comprising (a1) mixing the catalyst with at least one of the organic carbon compound, (b1) heating the mixture, and (c1) separating at least a gaseous reaction product of at least one solid reaction product.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for performing a method for making red mud.    Reservoir (12)    Transport equipment (14)    Conditioner (16)    Reactor (18)    Separator. (20)
NOVELTY - An electrolytic solution (7) is filled into an electrolytic vessel (5). A circulating flow generator generates circulating flow of solution in in-tank space (4) within the vessel. Several electrode rings (2) include an electrode plane orthogonal to the circulating flow, and immersed in the solution. Several insulator rings (3) inserted between the electrode rings, include an insulator surface orthogonal to circulating flow. A gas separation tank separates and extracts active ionized gas containing oxonium ion generated by electrolyzing the solution.    USE - Apparatus for generating active ionized gas containing oxonium ion.    ADVANTAGE - The active ionized gas generation apparatus is provided for generating the active ionized gas containing oxonium ions with high efficiency. The process of active ionized gas generation is highly economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the array arrangement of electrode ring and insulator ring of the active ionized gas generation apparatus.    Electrode ring (2)    Insulator ring (3)    In-tank space (4)    Electrolytic vessel (5)    Electrolytic solution (7)
NOVELTY - The manufactured combustible fuel article comprises a wood-derived cellulosic material (10-80 wt.%), a densified thermoplastic material (1-50 wt.%), ion exchanged zeolite (2-20 wt.%), a material (0-70 wt.%) consisting of coal (30-70 wt.%), torrified biomass, char, asphalt and/or lignin, and binder. The fuel article provides a heat output of 10000-16000 BTU per pound. The fuel pellet or briquette has a size of 1/8-12 inches in diameter and 1/8-24 inches in length. The thermoplastic material is present in particulate form before the manufacture of the fuel article.    USE - Used as a manufactured combustible fuel article such as a fuel pellet, briquette or fire log is useful for industrial boilers, residential fireplace and campfire applications.    ADVANTAGE - The manufactured combustible fuel article has reduced emission of sulfur compounds, improved toughness and water resistance, and high specific energy content.    DETAILED DESCRIPTION - The manufactured combustible fuel article comprises a wood-derived cellulosic material (10-80 wt.%), a densified thermoplastic material (1-50 wt.%), ion exchanged zeolite (2-20 wt.%), a material (0-70 wt.%) consisting of coal (30-70 wt.%), torrified biomass, char, asphalt and/or lignin, and binder. The fuel article provides a heat output of 10000-16000 BTU per pound, and has a size of 1/8-12 inches in diameter and 1/8-24 inches in length. The thermoplastic material is present in particulate form before the manufacture of the fuel article, and is ground into a particle size of 80-200 Mesh.
NOVELTY - The system (1) has a reversible electric power-hydrogen conversion stage (2) which includes a fuel cell stack (7) to produce electric power from stored hydrogen. An electrolytic cell stack (9) produces hydrogen from electric power. A hydrogen pressure modification stage (3) modifies pressure of hydrogen from/to the reversible electric power-hydrogen conversion stage. A management stage (5) manages operation of the reversible electric power-hydrogen conversion stage, hydrogen pressure modification stage and electric power management and conditioning stage (4).    USE - System for producing electric power from hydrogen using fuel cells e.g. electric generator and hydrogen from electric power using electrolytic cells e.g. electrolyzer.    ADVANTAGE - The efficiency of system can be improved with low production cost by management of hydrogen production parameters in relation to the surrounding conditions. The system is more reliable due to higher maturity of the technology and possibility of performing interventions in a separate and independent manner on the fuel cell stack and on the electrolytic cell stack. The system is more efficient due to the possibility of independently designing the hydrogen production and use stages.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for software loadable in management stage of system for producing electric power from hydrogen and hydrogen from electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for producing electric power from hydrogen.    System for producing electric power from hydrogen (1)    Reversible electric power-hydrogen conversion stage (2)    Hydrogen pressure modification stage (3)    Electric power management and conditioning stage (4)    Management stage (5)    Fuel cell stack (7)    Electrolytic cell stack (9)
NOVELTY - The apparatus (10) has reformer (20) that takes out hydrogen from water by electrolyzing water. A supply-flow channel supplies the hydrogen obtained by reformer to anode (32), and supplies air to cathode (31). A fuel cell (30) produces electric power according to electrochemical reaction of hydrogen and in-air oxygen. An ejection opening (30a) of fuel cell is provided to take out clean water obtained during generation of electric power through electrochemical reaction, so that electricity acquired by fuel cell is refluxed to direct current (DC) power supply (40).    USE - Water treatment apparatus.    ADVANTAGE - Since the ejection opening of fuel cell is provided to take out clean water obtained during generation of electric power through electrochemical reaction, the supply of electric power during electrolyzing the water can be reduced. The energy efficiency of water-purifying generation can be improved. Thus, the structure of water treatment apparatus can be simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water treatment apparatus. (Drawing includes non-English language text)    Water treatment apparatus (10)    Reformer (20)    Anode (25,32)    Cathode (26,31)    Fuel cell (30)    Ejection opening of fuel cell (30a)    DC power supply (40)
NOVELTY - A reciprocating compressor comprises isobutane as coolant, refrigerator oil main component containing base oil(s) chosen from monoester oil (I) and polyol-ester oil (II), and 1-30 weight% of secondary polyol-ester oil (III).    USE - Reciprocating compressor is used for refrigerator (claimed).    ADVANTAGE - The reciprocating compressor has excellent compatibility and abrasion resistance, without using toxic phosphorus extreme pressure agent. The refrigerator using reciprocating compressor has excellent durability.    DETAILED DESCRIPTION - A reciprocating compressor comprises isobutane as coolant, refrigerator oil main component containing base oil(s) chosen from monoester oil of formula: R1-C(=O)-O-R2 (I) and polyol-ester oil of formula: R3-C(=O)-O-CH2-C(-CH3)2-CH2-O-C(=O)-R3 (II), and 1-30 weight% of secondary polyol-ester oil of formula: (R4-C(=O)-O-CH2)3-CCH2-O-CH2C-(CH2OC(=O)-R4)3 (III).    R1=5-9C alkyl;    R2=8-10C alkyl;    R3=5-9C alkyl;and    R4=7-9C alkyl.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of reciprocating compressor.    Airtight compressor (11)    Motor (12)    Refrigerator oil (13)    Cylinder (14)    Piston (15)    Crankshaft (16)    Ejection opening (17)
NOVELTY - A membrane electrode assembly consists of hydrogen permeability metal foil having thickness of 1 mu m or more, and amorphous inorganic solid electrolytic membrane having proton conductivity. The metal foil has a self-support. An intermediate layer containing metal having low deformation at the time of hydrogen storage is provided between the metal foil and electrolytic membrane. The electrolytic membrane consists of metal oxide chosen from silica, titania, zirconia, alumina and ceria, doped with cation which can take coordination number more than pentacoordinate in metal oxide.    USE - Membrane electrode assembly for fuel cell (claimed) e.g. medium temperature type fuel cell, solid polymer electrolyte type fuel cell, phosphoric acid type fuel cell and solid oxide type fuel cell used as power source of motor vehicles, and hydrogen generating apparatus.    ADVANTAGE - The membrane electrode assembly provides fuel cell having excellent chemical and mechanical stability and drive stability. An airtight electrolyte thin film which does not contain grain boundary in which voids and pinholes can be formed easily. The diffusion and combustion reaction in the joining interface of gas leak and electrode substance can be inhibited by the electrolyte thin film, and the self-supportive property and ionic conductivity are improved. The electrode assembly is manufactured economically without using an expensive vacuum device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of membrane electrode assembly.
NOVELTY - The device has gasification furnace whose upper portion is connected with filtering system through gas pipeline, and lower portion is provided with residue discharging hole. The filtering system is provided with filter connected with a gasification furnace and a water pond through gas pipeline. The filter is connected with fuel gas conveying pipeline.    USE - Biomass gasification device.    ADVANTAGE - The combustible gas is purified by filtering system to remove the dust and coke so as to obtain the purified combustible gas. Hence environmental pollution can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification device. (Drawing includes non-English language text)
NOVELTY - The device has a fuel cell that is provided with a hydrogen inlet and a hydrogen outlet, where a hydrogen production unit is connected with the hydrogen inlet for generating hydrogen, which enters into an inner side of the fuel cell. A bill valve is arranged at the hydrogen inlet to prevent hydrogen in the fuel cell from being flowed out via the hydrogen inlet. An exhaust valve i.e. pressure control valve, is arranged at the hydrogen outlet for exhausting hydrogen in the fuel cell. An end of the elastic element is arranged with the fuel cell.    USE - Power supply device.    ADVANTAGE - The device controls inner pressure of the fuel cell, thus improving generation efficiency of the fuel cell in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a power supply device.'(Drawing includes non-English language text)'
NOVELTY - A business model enables processing using organic refuse and excrement as biomass energy, which is exploited at every house by thermoelectric supply, and constructs social system at both surfaces of energy.    USE - Business model.    ADVANTAGE - The recovery of refuse is avoided, and generation of carbon dioxide by fossil fuel for incineration disposal is enabled, and hence, economical. The generation of methane gas in sewer line is prevented, and maintenance expense of sewer line is reduced.
NOVELTY - An electrode (1) is formed at the surface of porous-shaped electrolyte, which is subjected to metal plating by electroless plating method. The electrolyte contains solid oxide having proton conductivity.    USE - Electrode is used for fuel cell, hydrogen producing apparatus and hydrogen permselective apparatus (claimed).    ADVANTAGE - The electrode has large reaction area and excellent peeling resistance, and provides fuel cell having high efficiency, stability and durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell, hydrogen producing apparatus and hydrogen permselective apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of electrode.    Electrode (1)    Proton conductor (2)
NOVELTY - A sewage treatment technique comprises using vertical current settling pool as primary physical treatment unit for removing most particles and regulating water quality and water quantity and degrading part macromolecular organic material; using biological contact oxidization pool as secondary biological treatment unit for purifying most organic material and part nitrogen and phosphor by microorganism film attached on filler; and using composite vertical current artificial wetland as third-stage ecological treatment unit for deeply purifying various pollutants remained in water body.    USE - Sewage treatment technique for water quality and water quantity countryside dispersive living sewage.    ADVANTAGE - The method has easy management and operation, low operation energy consumption and excellent treatment effect. It has good pollutant purifying effect, easy operation and management, and flexible application and installation.    DETAILED DESCRIPTION - Sewage treatment technique comprises using vertical current settling pool as primary physical treatment unit for removing most particles and regulating water quality and water quantity and degrading part macromolecular organic material; using biological contact oxidization pool as secondary biological treatment unit for purifying most organic material and part nitrogen and phosphor by microorganism film attached on filler; and using composite vertical current artificial wetland as third-stage ecological treatment unit for deeply purifying various pollutants remained in water body through ecological system adsorption, filter, plant adsorption and microorganism effect. An INDEPENDENT CLAIM is included for an integral device which comprises vertical current sedimentation tank, biological contact oxidization pool and composite vertical current artificial wetland from center to outside with diameter ratio of 1: 2.5:5.
NOVELTY - A biological treatment of drilling waste of oil fields comprises mixing drilling waste of oil fields and water at wt. ratio of 1:1-5 to form slurry solution; preprocessing slurry solution; performing biological treatment to preprocessed slurry solution which comprises anoxic treatment and aerobic treatment, adding in acclimated activated sludge during anoxic treatment and aerobic treatment; and performing slurry separation after biological treatment.    USE - Method for biological treatment of drilling waste of oil fields (claimed).
NOVELTY - The system has a gasification furnace i.e. lower suction static bed gasification furnace, whose gas outlet is connected to a high temperature dust remover via a pipeline. A gas outlet of the high temperature dust remover is connected to a tar processing device. A gas outlet of the tar processing device is connected to a gas conveyer that is connected to a gas storage cylinder. The gas storage cylinder is connected to a gas internal combustion generator set. A tar processing device is provided with a heavy tar cold precipitator whose inlet is connected to the gas outlet of the dust remover.    USE - Gasification generating system for a biomass static bed.    ADVANTAGE - The system is simple in structure and easy to manufacture with low manufacturing cost. The system reduces biomass gas tar content in produced biomass gas during production process to achieve nation standard, and avoids damage to a gasification generating device when biomass gas tar content is high. The system improves biomass gasification generation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a gasification generating system.'(Drawing includes non-English language text)'
NOVELTY - The device has a gas inlet tube, a gas outlet tube, a liquidometer, a liquid level valve and a connector that are arranged on an external part of a water seal device. The water seal device is connected with an upstream buffer device of a downstream gas burner. A high voltage igniter is arranged on a center part of a mixing chamber and an installed furnace body of a burning furnace of a steam boiler. The high voltage igniter is connected with a steam boiler system. The steam boiler system is connected with an upstream air-gas burner and an automatic control system.    USE - Steam boiler system device for an air-gas generating furnace of a bio-fuel fluidized bed in an industry.    ADVANTAGE - The device utilizes waste wood blocks, wood bits, rice husks, straws and waste mushroom culturing master materials, thus saving energy and manufacturing cost of industries. The device reduces sulfur dioxide discharge, thus increasing environment friendly effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a steam boiler system device.
NOVELTY - The burner has a boiler burning device embedded to a bottom part of a boiler (1). A secondary burning-assisting oxygen-supply device (10) is provide with a multilayer annular air nozzle structure (17) and arranged between a gasifying and carbonizing chamber (4) and a direct-injection burning chamber (5). A boiler adding opening (21) is utilized as an adding opening. The burner is provided with an assisting airway (12). A chimney opening of the boiler is provided with a strong exhaust fan (14). The boiler is installed with an electric contact pressure meter (2).    USE - Gasifying direct-injection burning-type boiler burner for bio-fuel.    ADVANTAGE - The burning device integrates the gasifying, carbonizing and burning functions in an inner side of the boiler, so as to realize tar-less opened burning and prevent heat loss of the device. The burner is provided with 95 percent heat efficiency. The burner utilizes reproducible energy in an efficient manner. The burner is environment-friendly and energy-saving, and provides better benefits for the country and people, and has wide range application.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gasifying direct-injection burning-type boiler burner.    Boiler (1)    Electric contact pressure meter (2)    Gasifying and carbonizing chamber (4)    Direct-injection burning chamber (5)    Secondary burning-assisting oxygen-supply device (10)    Assisting airway (12)    Strong exhaust fan (14)    Multilayer annular air nozzle structure (17)    Boiler adding opening (21)
NOVELTY - The rotary device has a rotary carbonizing furnace comprising a hearth and a rotary furnace. One path of high-temperature hot gas produced via combusting in an oxygen distribution combustion chamber is introduced into the hearth of the rotary carbonizing furnace via a flue to introduce into a carbonizing section. The structure of the rotary furnace comprises a drum body, an inner heat pipe and a block ring. One end head of the inner heat pipe is fixed on the wall of the drum body on one side, and is fixed on the wall of the drum body on the other side via passing through the block ring.    USE - Continuous rotary device for integrated pyrolysis and carbonization of biomass with heat supply of boiler.    ADVANTAGE - Work efficiency of rotary carbonizing furnace is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the structure of the continuous rotary device.
NOVELTY - A microbial activity enhancing fluid agent comprises an enzyme, a carrier, an organic acid, and nutrient substances at weight ratio of 1:0.1-8:200-600:50-2000.    USE - Microbial activity enhancing fluid agent used in biological treatment of domestic sewage and industrial wastewater (claimed).    ADVANTAGE - The fluid agent can promote catalysis function of sludge zoogloea, so as to reinforce activities of beneficial microorganisms in sludge and rapidly catalyze and decompose organic pollutants. The carrier improves structure of sludge zoogloea to reinforce the biological treatment capacity of the sewage. Further, the fluid agent is convenient to use, and has less dosage and high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the microbial activity enhancing fluid agent, comprising:    (A) preparing accurately weighed enzyme and nutrient substances as solution 1;    (B) adding accurately weighed carrier in aqueous solution of organic acid to prepare solution 2; and    (C) mixing the two prepared solutions and storing in refrigerator at 0-4 degrees C for future use.
NOVELTY - Forming a nanocatalyst comprising at least one reactive species attached to a metal oxide nanoparticle, involves mixing at least one hydroxyl-containing compound carrying the reactive species with a metal oxide nanoparticle coated with a hydrophobic surfactant, where the hydroxyl-containing compound replaces the hydrophobic surfactant on the surface of the metal oxide nanoparticle and the nanocatalyst is produced.    USE - For forming nanocatalyst (claimed) which is used to catalyze the hydrolysis of an environmental pollutant e.g. pesticide, insecticide, herbicide, insect repellent, paraoxon, parathion, methyl parathion, malathion, methoprene, atrazine, azinophos-methyl, diazinon, and O-chlorobenzylmalononitrile, in surface water, ground water, or the soil.    ADVANTAGE - The nanocatalyst is small, stable, biomimetic catalyst that also recovered and reused; and hydrolyzes and inactivates the environmental pollutant in water, soil, or another medium at ambient temperatures.
NOVELTY - Methane fermentation method, involves adding organic waste into methane fermentation tank, performing methane fermentation with high temperature methane bacteria, and measuring temperature more upward than liquid level of fermented liquor in the fermentation tank, or detecting if the temperature is greater than the temperature rise width based on normal operation and if the duration of the temperature rise is longer than the temperature rise duration based on the normal operation by maintaining control which suppresses foaming in the fermentation tank.    USE - Methane fermentation method.    ADVANTAGE - The method enables to suppress foaming. The damage to pipe and measuring device can be prevented. The maintenance cost can be reduced.
NOVELTY - Producing (p1) a denatured ethanol composition, involves: hydrogenating an acetic acid feed in the presence of a catalyst to form a crude ethanol product comprising ethanol and at least one denaturant; separating the crude ethanol product in at least one separation unit into a denatured ethanol composition and at least one derivative stream, where the denatured ethanol composition comprises denaturant (0.01-40 wt.%).    USE - For producing a denatured ethanol composition which is used in fuel composition, feed stock for ester production, and a solvent (claimed); for use in a variety of applications including pharmaceutical products, cleansers, sanitizers, or hydrogenation transport; in gasoline for motor vehicles such as automobiles, boats and small piston engine aircrafts; as a solvent for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks, and pharmaceuticals; as a processing solvent, e.g. in manufacturing processes for medicinal products, food preparations, dyes, photochemicals and latex processing; as a chemical feedstock to make other chemicals such as vinegar, ethyl acrylate, ethyl acetate, ethylene, glycol ethers, ethylamines, aldehydes, and higher alcohols, especially butanol.    ADVANTAGE - The denatured ethanol composition is prepared without the addition of outside denaturant. Thus, by forming the denaturant in situ along with the ethanol in the hydrogenation step, the process produces denatured ethanol more efficiently and reduces processing steps. The process eliminates the need for separately producing or obtaining a denaturant and subsequently adding the denaturant to ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a denatured ethanol composition formed by the process (p1).
NOVELTY - The apparatus (10) has an ink tank (12) connected with a die head (16) through an ink supply piping (14). A sheet-like base material (18) is arranged to a face of an ink discharge opening of the die head. An ink layer forming apparatus forms a layer of catalyst ink (20) supplied from the tank on the base material. An ultrasonic processing apparatus (24) is arranged between the die head and a drying furnace (22). The ultrasonic processing apparatus re-disperses the catalyst ink that is supplied to an ink layer forming apparatus.    USE - Electrode manufacturing apparatus for a fuel cell.    ADVANTAGE - The ultrasonic processing apparatus re-disperses the catalyst ink that is supplied to the ink layer forming apparatus, so that heterogeneous-izing of the ink layer and discontinuitization of the coating surface can be suppressed, thus improving yield of the electrode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrode manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrode manufacturing apparatus.'(Drawing includes non-English language text)'    Electrode manufacturing apparatus (10)    Ink tank (12)    Ink supply piping (14)    Die head (16)    Sheet-like base material (18)    Layer of catalyst ink (20)    Drying furnace (22)    Ultrasonic processing apparatus (24)
NOVELTY - The apparatus (10) has seal grooves (64a,68a) that are formed in anode and cathode side separators (34,36) and are located outward of anode side and cathode side electric power feeding structures (40,42). The recess (70) obstructed by solid polymer electrolyte membrane (38) is formed in separator planar portion (36aa) located outward of seal groove (64a). The receiving pressure portion (72) is formed in flat portions other than recess of separator planar portions (36aa,34aa) to receive load of lamination direction on both sides of solid polymer electrolyte membrane.    USE - Water electrolysis apparatus for high-pressure hydrogen manufacturing apparatus.    ADVANTAGE - The receiving pressure portion is formed in flat portions other than recess of separator planar portions to receive load on sides of polymer electrolyte membrane such that the pushing force provision area in receiving pressure portion can be reduced and size of external pushing force providing apparatus can be reduced. The desired seal contact pressure can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the unit cell used in water electrolysis apparatus.    Water electrolysis apparatus (10)    Anode side separator (34)    Separator planar portion (34aa,36aa)    Cathode side separator (36)    Solid polymer electrolyte membrane (38)    Anode side electric power feeding structure (40)    Cathode side electric power feeding structure (42)    Seal grooves (64a,68a)    Recess (70)    Receiving pressure portion (72)
NOVELTY - The detector i.e. portable type gas detector, has an output correction mechanism correcting a sensor output value (V1) from a gas sensor i.e. semiconductor heat ray type gas sensor, comprising a gas sensitive element, which sensitizes a detection object gas in a state heated by electricity supply. The sensor output value from the gas sensor is acquired during an output correction object measurement based on an output value for correction acquired by an output acquisition process and an output correction process.    USE - Gas detector i.e. portable type gas detector, for detecting presence or absence of an object gas e.g. combustible gas. Uses include but are not limited to liquefied petroleum gas, methane, hydrogen, carbon monoxide, alcohol, arsine, phosphine, silane, diborane, germane and nitrogen trifluoride.    ADVANTAGE - The gas sensor outputs the sensor output value, which is acquired during the output correction object measurement based on the output value for correction acquired by the output acquisition process and the output correction process, so that the sensor output value in the time of the output correction object measurement is estimated based on the tendency of the time-dependent output change of the sensor output value and an actual sensor output initial variation characteristic curve, thus performing gas concentration measurement at an early stage after power activation without waiting for stabilization of a sensor output.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of a relationship between a sensor output value and time.'(Drawing includes non-English language text)'    Sensor output initial variation characteristic curve (alpha)    Logarithmic function area (LA)    Approximated curve (SL)    Sensor output values (Vm, V1, V2)
NOVELTY - The automatic dosing device has a liquid indicator for detecting the height of chemical liquid while arranged in the liquor storage tank. The output of the liquid indicator is connected with the PLC. The liquid outlet pipe of the liquor storage tank is provided with a metering pump for controlling the output of the chemical liquid. The feeding device, the water inlet electromagnetic valve, a blast blower, a stirring machine, the medicine inlet electromagnetic valve, and a control end of the metering pump are connected with the PLC.    USE - Automatic dosing device for sewage treatment.    ADVANTAGE - The automatic dosing device has a rational and compact structure, automatic control, good operation stability and reliability, simple and convenient operation, and is beneficial for increasing the sewage treatment efficiency such that it solves the problems that the agent dosage is inaccurate and the lack of timeliness is controlled in the process of adding flocculating agent and coagulant aid by manual control.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the automatic dosing device. (Drawing includes non-English language text).
NOVELTY - The filter has a sponge filter core located in a shell and formed with multiple gas guide passages, where diameter of the gas guide passage is less than 8 mm.    USE - Fuel gas filter for a straw gasification furnace (claimed).    ADVANTAGE - The filter has better filtering effect, so that gas does not contain impurity, thus protecting environment from being polluted during combustion of the gas. The filter reduces blockage. The filter core is convenient to clean and replace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a straw gasification furnace, comprising an exhaust pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fuel gas filter.
NOVELTY - Herbicide comprises a glyphosate water solution containing glyphosate, a surfactant consisting of an alkyl alcohol polyethoxylated or polypropoxylated, isopropylamine and 4-10C amine, where the alkyl group is branched in order to reduce substantially the surface tension and improve efficacy.    USE - Used as herbicide. No biological data given.    ADVANTAGE - The surfactant allows a reduction of the quantity of active substance per hectare, and improves the speed of absorption of the water solution of the glyphosate formulation by the leaves of the weeds. The herbicide is absorbed within a shorter time before it rains compared to standard formulations. The herbicide strongly increases the yield of food per hectare. The herbicide is cost effective and environmentally friendly.
NOVELTY - A manufacturing process for preparing stable and easily transportable liquid fuel from high moisture carbonaceous materials from waste and/or renewable resources, is provided. Accordingly, the manufacturing process for converting any high moisture carbonaceous waste into biomass water fuel, which is a pumpable, nonhazardous, nontoxic, low cost alternative to petroleum derived fuels that can use existing oil and coal infrastructure for handling, storage and transportation, is described. Image 0/0
NOVELTY - The manufacturing method involves using a catalyst carrier to support a catalyst component. The ratio of the amount of hydrogen gas with respect to the amount of vegetable oil is set according to the ratio of the flow volume of hydrogen gas with respect to the flow volume of vegetable oil. The hydrogen gas is made to react with the vegetable oil to refine the vegetable oil and obtain a hydrogenated vegetable oil.    USE - Manufacturing method for bio-hydrocarbon (claimed).    ADVANTAGE - Enables production of bio-hydrocarbon which has controlled carbon number excellent low-temperature viscosity by hydrogenating vegetable oil in a predetermined condition. Enables hydrogenating vegetable oil at extremely high efficiency. Facilitates separation of bio-hydrocarbon and catalyst component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bio-hydrocarbon manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic flow diagram of the manufacturing method for bio-hydrocarbon. (Drawing includes non-English language text).
NOVELTY - Solid fuel is obtained by thermal compression molding of composition comprising dried material (70 wt.% or more dry weight) of Arundo donax, Leucaena leucocephala, sugarcane, cassava, straw, seaweed or algae.    USE - The solid fuel is useful for electric power generation (claimed), or thermal power generation.    ADVANTAGE - The solid fuel can be produced in large quantities, has stable heat emission value and is highly stable and environmentally-friendly (does not cause global warming) as the fuel does not emit harmful or toxic gases and carbon dioxide production is suppressed by using plant material, particularly leftover waste residue of seeds, grains and bulb as raw material.
NOVELTY - Performing highly effective aerobic composting biologically involves using a novel reactor, where oil and water are removed from the raw material. Waste is added to a squeezing device of a movable high effective composting reactor, where the device is covered by a sealing cover. The food waste is pressed to remove oil and water by a rotary axle. The waste is mixed and stirred and then the materials are discharged from the outlet door, where the waste is discharged to a lower stirring container. A structure adjusting agent is added to the container.    USE - Method for performing highly effective aerobic composting biologically (claimed) used in performing movable screen treatment of food wastes in food unit and goods processing factory to recycle food waste.    ADVANTAGE - The method enables to perform highly effective aerobic composting biologically, and protects environment and ensures high social and economical benefits.    DETAILED DESCRIPTION - Performing highly effective aerobic composting biologically involves using a novel reactor, where oil and water are removed from the raw material. Waste is added to a squeezing device of a movable high effective composting reactor, where the device is covered by a sealing cover. The food waste is pressed to remove oil and water by a rotary axle. The waste is mixed and stirred and then the materials are discharged from the outlet door, where the waste is discharged to a lower stirring container. A structure adjusting agent is added to the container. The materials are mixed and stirred uniformly. Aerobic composting is performed for food wastes, where wastes are mixed uniformly in a composting container of the reactor. The composting process is controlled by a ventilation system and an automatic control system.
NOVELTY - A garbage disposal device comprises reaction chamber, combustion chamber which has fuel inlet in lower end and heat conducting pipe in upper end, heat conducting pipe, collecting pipe, water-cooling type condensing pipe, oil-gas separator which is connected with air outlet and liquid outlet, collector which is provided in airtight connection with reaction chamber, and collecting branch pipe provided in upper end of reaction chamber which is connected with collecting pipe going through center of water-cooling type condensing pipe.    USE - Garbage disposal device.    ADVANTAGE - The garbage disposal device is environment-friendly and practical.    DETAILED DESCRIPTION - A garbage disposal device comprises reaction chamber, combustion chamber which has fuel inlet in lower end and heat conducting pipe in upper end, heat conducting pipe, collecting pipe, water-cooling type condensing pipe, oil-gas separator which is connected with air outlet and liquid outlet, collector which is provided in airtight connection with reaction chamber, and collecting branch pipe provided in upper end of reaction chamber which is connected with collecting pipe going through center of water-cooling type condensing pipe. The reaction chamber and combustion chamber are separated and alternated. The end of collecting pipe collected with oil-gas separator extends out of water-cooling type condensing pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the garbage disposal device.
NOVELTY - The furnace has a furnace body (1) whose inner chamber is provided with a net cylindrical storage inner sleeve (4) and forms a gap with an inner wall of the furnace body. A bottom part of the furnace body is outwardly provided with an ash outlet (5). An upper end of the furnace body is movably connected with a press rod (6). An upper end of the press rod is provided with a handle (7). A middle lower part of the press rod is located in the inner chamber of the furnace body. A lower end of the press rod is connected with mulitple tension rods (8).    USE - Straw gasifying furnace.    ADVANTAGE - The furnace ensures the water steam to be produced from burning the straw and pass through the net cylindrical storage inner sleeve to attach to the inner wall of the furnace body, so that the cooled water is prevented from being fallen on the straw material, thus avoiding the bad influence. The spiral toggling rod pushes the straw to move downward. The furnace ensures better continuous and average burning and gas production of the straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a straw gasifying furnace.    Furnace body (1)    Net cylindrical storage inner sleeve (4)    Ash outlet (5)    Press rod (6)    Handle (7)    Multiple tension rods (8)
NOVELTY - Making fatty acid alkyl esters involves: a) combining a feedstock with an alcohol and an acid catalyst, where the feedstock comprises (i) free fatty acids (FFAs) and/or glycerides; and (ii) cellulosic material and/or proteins; and b) reacting the feedstock and the alcohol at 140-300 degrees C, and at a pressure to prevent boiling of the alcohol during the reaction to generate fatty acid alkyl esters, cleave the cellulosic material, if present, and shorten the proteins, if proteins are present.    USE - For making fatty acid alkyl esters, cleaved cellulosic material, shortened proteins (claimed), and amino acids; for production of biofuels and ethanol.    ADVANTAGE - The method is a fast, single-step, and efficient method for conversion of biomass into biofuel and sugars to produce ethanol. The potentially lower cost feedstock does not contain a current agricultural food source commodity but rather second generation nonfood materials such as algae or agricultural by-products. The incorporation of dry distillers grain (DDG) treatment operations within existing ethanol plants enhances the potential economic attractiveness.
NOVELTY - A hydrogen storage material capable of reversibly storing and releasing hydrogen comprises: amorphous phase containing an aluminum-magnesium alloy and a crystalline aluminum phase and crystalline titanium hydride phase each having a maximum length of less than or equal to 200 nm and dispersed in the amorphous phase.    USE - In fuel-cell vehicles.    ADVANTAGE - The hydrogen storage material is capable of reversibly storing and releasing hydrogen; it exhibits high hydrogen storage capacity even under a relatively mild condition and such as low temperature and low pressure and thus requires low energy for the hydrogen storage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production (M1) of the hydrogen storage material involving: mixing aluminum hydride (AlH3), magnesium hydride (MgH2), and titanium hydride (TiH2) to prepare a mixed powder; ball-milling the mixed powder in a hydrogen atmosphere for 60-600 minutes while applying a force of 5-30G (in which G is gravitational acceleration) to prepare a milled product and dehydrogenating the milled product to obtain the hydrogen storage material.
NOVELTY - The chamber (10) has a chamber body in a shape of a hollow cylinder with a cone-shaped bottom (11) to which a grit channel (13) is installed below a center portion. The grit channel includes a grit removing device. The body includes a wall mixer (14), a vertical mixer (15) and a spiral grit remover (16). The cylinder includes a wall with the wall mixer and a center of the cylinder includes the remover with a grit-removing blade (17) for removing grit on the cone-shaped bottom. The cone-shaped bottom includes a vertical mixer installed at a position close to the bottom and vertical to the wall.    USE - Grit chamber for a grit removing system (claimed) for removing grit and feathers in a fowl dung such as a chicken dung.    ADVANTAGE - The vertical mixers installed at a position close to the cone-shaped bottom of the hollow cylinder and vertical to the wall of the cylinder, thus sinking the grid efficiently and completely in the dung of domestic animals into water bottom to completely separate the grit from the dung of domestic animals and obtaining the feathers contained in the dung of domestic animals as fermentation material when passing the dung through a cutting and filtering device. The distance between the grit-removing blade of the spiral grit remover and the cone-shaped bottom is about 5 cm, thus preventing the grit-removing blade at the bottom of the spiral grit remover from contacting the bottom of a hydrolysis chamber and removing the grit efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for removing grit from dung of domestic animals.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a grid chamber.    Grit chamber (10)    Cone-shaped bottom of cylinder (11, 12)    Grit channel (13)    Wall mixer (14)    Vertical mixer (15)    Spiral grit remover (16)    Grit-removing blade (17)
NOVELTY - An emulsion fuel comprises water, high-temperature volatile oil, animal-and-vegetable oil, and/or biodiesel fuel, and C-heavy oil. The content of C-heavy oil is 0.001-3 weight% with respect to total content of water, high-temperature volatile oil, animal-and-vegetable oil, and/or biodiesel fuel.    USE - Emulsion fuel.    ADVANTAGE - The emulsified state of emulsion fuel is stabilized with reduced content of emulsifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of emulsion fuel, which involves pressurizing the liquid containing water, high-temperature volatile oil, animal-and-vegetable oil, and/or biodiesel fuel, and C-heavy oil using a pressurizing unit, passing through a flow path, and emulsifying using high pressure stirring apparatus.
NOVELTY - The method comprises synthesizing a composition comprising a perovskite and a slurry by a microwave-assisted combustion method and using a metal precursor, forming an electrolyte support using a dry-pressing method, applying the composition on the electrolyte support to form an anode and a cathode, adjusting a pH of the composition, and operating the anode as the cathode and the cathode as the anode.    USE - The method is useful for fabricating a symmetrical solid oxide fuel cell to generate electricity.    ADVANTAGE - The method is capable of economically fabricating self-regenerative solid oxide fuel cell with high stability and efficiency and high performance and reliability and without poisoning effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a symmetrical solid oxide fuel cell.
NOVELTY - Removing contaminants from a natural gas stream, comprises feeding the natural gas stream to a first adsorption unit (H), and then feeding the natural gas stream to a second adsorption unit (K).    USE - The method is useful for removing contaminants including water, non-methane organic compounds, hydrogen sulfides, carbonyl sulfide or carbon dioxide, from the natural gas stream (claimed), where the natural gas stream includes biogas or landfill gas stream.    ADVANTAGE - The method utilizes smaller vacuum pumps to regenerate the adsorption beds from first adsorption unit, which saves the power consumption, hence it is cost-effective.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of an integrated biogas/landfill gas purification system.    Condenser (F)    Heat exchanger (G)    First adsorption unit (H)    Blower/vacuum pump (I)    Second adsorption unit (K)
NOVELTY - A sewage treatment apparatus comprises anaerobic tank (1) which is installed upstream, reaction tanks into which activated sludge is thrown, aeration unit (5-7) which is installed in aerobic tank (2-4), gas recovery unit (10-12) which is installed in upper part of aerobic tank and collects aeration gas, dinitrogen monoxide measurement unit which measures dinitrogen monoxide concentration in waste gas collected by gas recovery unit, and control unit which controls front stage aeration unit regulator (9) based on measurement signal of dinitrogen monoxide unit.    USE - A sewage treatment apparatus.    ADVANTAGE - The apparatus reduces greenhouse gas and accelerates denitrifying reaction.    DETAILED DESCRIPTION - A sewage treatment apparatus comprises anaerobic tank (1) which is installed upstream, reaction tanks into which activated sludge is thrown, aeration unit (5-7) which is installed in aerobic tank (2-4), gas recovery unit (10-12) which is installed in upper part of aerobic tank and collects aeration gas, dinitrogen monoxide measurement unit which measures dinitrogen monoxide concentration in waste gas collected by gas recovery unit, control unit which controls front stage aeration unit regulator (9) for adjusting air flow of aeration unit at side of anaerobic tank based on measurement signal of dinitrogen monoxide unit, and front stage aeration unit regulator. An INDEPENDENT CLAIM is included for a sewage-treatment process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage treatment apparatus. (Drawing includes non-English language text).    Anaerobic tank (1)    Aerobic tank (2-4)    Aeration unit (5-7)    Front stage aeration unit regulator (9)    Gas recovery unit (10-12)
NOVELTY - A fermentation apparatus (20) comprises fermenter (21) provided with outer shell part (23), belt-shaped stirring blade part (24) and baffle plate part which is rotated to focus on inclined rotating shaft, rotation mechanism (22) which rotates fermenter, fermentation chamber provided in outer shell part which ferments processed material, receiving opening provided in edge part below rotating shaft direction which receives processed material in fermentation chamber, and discharge port which discharges processed material fermented in fermentation chamber.    USE - Fermentation apparatus for toilet equipment e.g. urine drying apparatus.    ADVANTAGE - The fermentation apparatus favorably ferments processed material.    DETAILED DESCRIPTION - A fermentation apparatus (20) comprises fermenter (21) provided with outer shell part (23) formed in axial symmetry centered on rotating shaft and provided in edge part above rotating shaft direction, belt-shaped stirring blade part (24) extended in rotating shaft direction that recovered from inner surface of outer shell part towards center and baffle plate part of inner frame shape that formed surface orthogonal to rotating shaft which is rotated to focus on inclined rotating shaft, rotation mechanism (22) which rotates fermenter, fermentation chamber provided in outer shell part which ferments processed material, receiving opening provided in edge part below rotating shaft direction which receives processed material in fermentation chamber, and discharge port which discharges processed material fermented in fermentation chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fermentation apparatus.    Fermentation apparatus (20)    Fermenter (21)    Rotation mechanism (22)    Outer shell part (23)    Stirring blade part (24)
NOVELTY - A nitrogen containing wastewater is processed by selecting hydrogen donor used by biological denitrification process of nitrogen containing wastewater based on biological oxygen demand (BOD)/chromium chemical oxygen demand (CODCr) value and value of nitrogen removal rate obtained by denitrifying continuous experiment.    USE - Processing of nitrogen containing wastewater.    ADVANTAGE - The operation cost is reduced.
NOVELTY - Production highly purified hydrogen, comprises: a carbon monoxide (CO) adsorption-treatment process; a hydrogen separation collection process; a hydrogen storage off-gas storage process; and CO selective-adsorbent initial stage purge process.    USE - The method is useful for producing highly purified hydrogen (claimed).    ADVANTAGE - The method is highly efficient and effective in producing purified hydrogen, cost effective and has excellent properties.    DETAILED DESCRIPTION - Production highly purified hydrogen, comprises: a carbon monoxide (CO) adsorption-treatment process of having CO adsorption step which obtains CO removal gas and CO selective-adsorbent reproduction step which reproduces the CO selective adsorbent of the adsorption removal device, where hydrogen rich gas containing CO is made to contact CO selective adsorbent of CO adsorption removal device, and CO is removed by absorption; a hydrogen separation collection process which has the hydrogen storage step which makes a hydrogen storage alloy occlude the hydrogen contained in the CO removal gas and the hydrogen desorption step to which the hydrogen occluded by the hydrogen storage alloy is discharged; a hydrogen storage off-gas storage process of storing the off gas discharged at the hydrogen storage step of the hydrogen separation collection process in an off-gas storage tank; and CO selective-adsorbent initial stage purge process which performs the initial stage purge of this CO selective adsorbent where, in restarting, after stopping the hydrogen production by implementation of each the process, the hydrogen storage off gas stored in CO selective adsorbent of the adsorption removal device used in the CO adsorption-treatment process at the hydrogen storage off-gas storage process is circulated.
NOVELTY - A hydrogen-producing material which produces hydrogen by the contact of water and produces water by the contact of hydrogen, comprises: a hydrogen storage metal which can occlude/release hydrogen by an oxidation reduction is used as a base material; and at least one substance of the metal or the metal oxide which is added to the surface of the hydrogen storage metal using an atomic layer depositing method (ALD) method or an liquid phase deposition (LPD) method.    USE - The hydrogen-producing material is useful in a fuel cell (claimed).    ADVANTAGE - The hydrogen-producing material has improved durability and reliability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a fuel cell comprising: an electrolytic membrane; a fuel electrode formed on one surface of the electrolytic membrane; an air electrode formed on the other surface of the electrolytic membrane; the hydrogen-producing material, where hydrogen is produced by oxidizing by making it react with the water produced by the electric power generation, the produced the hydrogen is supplied to the fuel electrode, water is produced by reducing by making it react with the hydrogen produced by reproduction, and the water by which it was generated is supplied to the fuel electrode; and    (2) a method of manufacturing the hydrogen-producing material which produces hydrogen by the contact of water and produces water by the contact of hydrogen.
NOVELTY - Metal microparticles having amphipatic molecule in the surface and specified particle size, is prepared. The obtained metal microparticles are formed into a film on a substrate by Langmuir-Blodgett (LB) method using amphipatic molecule. Metal microparticles in the obtained metal microparticle layer are contacted with a growth catalyst, and carbon nanotubes are grown. Thus, carbon nanotubes are manufactured.    USE - Manufacture of carbon nanotubes used for manufacturing electrode for fuel cell (claimed).    ADVANTAGE - The method efficiently provides carbon nanotubes having controlled density.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of electrode, which has an electrode layer formed using carbon nanotubes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of Langmuir-Blodgett film preparation apparatus.    Langmuir-Blodgett film preparation apparatus (10)    Trough (12)    Float (14)    Electronic balance (16)    Platinum board (18)    Water (20)    Langmuir-Blodgett film substance (22)    Glass substrate (30)
NOVELTY - Treating a methane-containing gaseous mixture, comprises: producing a gaseous mixture containing methane, carbon dioxide and optionally other ingredients; and subjecting the gaseous mixture to a gas-separation for providing the purest methane and/or carbon dioxide. The gas separation comprises a step for dynamic gas separation (4), in which a separation into a methane-rich pure gaseous phase and a low-methane weak gaseous phase takes place depending on different particle mass of the gaseous component.    USE - The methane is useful for operating motor vehicles or introducing into a gas supplying network.    ADVANTAGE - The method allows recycling of methane from the methane-containing gaseous mixture with improved quality and high purity in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for treating the methane-containing gaseous mixture comprising a device for separating the gaseous mixture into the methane-rich pure gaseous phase and the low-methane weak gaseous phase, where the device for separating the gaseous mixture comprises a device for dynamic gas separation, in which the separation of the components of the gaseous mixture takes place due to their different particle mass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of biogas production and treatment (drawing includes non-English language text).    Pre-treatment (1)    Fermentation (2)    Desulfurization (3)    Dynamic separation step (4)    Pneumatic separation step (5)
NOVELTY - The apparatus (10) has an ink tank (12) connected with a die head (16) through an ink supply piping (14). A sheet-like base material (18) is arranged to a face of an ink discharge opening of the die head. A cooling device (24) is arranged between the die head and a drying furnace (22). The cooling device suppresses fluidity of catalyst ink (20) before drying of a layer of the catalyst ink containing catalyst-carrying carbon, ionomer and a dispersion medium. The drying furnace adjusts temperature and supply-amount of air that is supplied to inside of the tank.    USE - Apparatus for manufacturing an electrode of a fuel cell.    ADVANTAGE - The apparatus reduces fluidity of the catalyst ink layer before drying of the layer of the catalyst ink containing the catalyst- carrying carbon, the ionomer, and the dispersion medium, thus improving viscosity of the catalyst ink, and hence suppressing segregation of the ionomer at the time of mass production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrode manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrode manufacturing apparatus.'(Drawing includes non-English language text)'    Electrode manufacturing apparatus (10)    Ink tank (12)    Ink supply piping (14)    Die head (16)    Sheet-like base material (18)    Catalyst ink (20)    Drying furnace (22)    Cooling device (24)
NOVELTY - A fuel cell system comprises modifier which modifies raw fuel to produce reformed gas, carbon monoxide modifying device (12) which is integrally provided in modifier so that modifier may be located in pipe, carbon monoxide removal device (13) which disposes in parallel along axial direction with respect to carbon monoxide modifying device while integrally providing in modifier, and fuselage part which dividedly installs introductory passage for introducing reformed gas from carbon monoxide modifying device to carbon monoxide removal device.    USE - Fuel cell system used as domestic electric power supply source.    ADVANTAGE - The fuel cell system attains size reduction and efficiency improvement.    DETAILED DESCRIPTION - A fuel cell system comprises modifier which modifies raw fuel to produce reformed gas, carbon monoxide modifying device (12) which integrally provided in modifier so that modifier may be located in pipe, carbon monoxide removal device (13) which disposes in parallel along axial direction with respect to carbon monoxide modifying device while integrally providing in modifier, and fuselage part provided between carbon monoxide modifying device and carbon monoxide removal device which dividedly installs introductory passage for introducing reformed gas from carbon monoxide modifying device to carbon monoxide removal device. The carbon monoxide concentration of reformed gas produced with modifier and reduced by carbon monoxide modifying device is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front view of the fuel processing system. (Drawing includes non-English language text).    Carbon monoxide modifying device (12)    Carbon monoxide removal device (13)    Introductory passage (52)    Reformed gas inflow port (53)    Air inflow port (54)
NOVELTY - Organic fertilizer is produced from organic waste by crushing organic waste via a crusher, mixing the material in a stirrer, filling into plastic weaving bag to ferment, sending to a drying machine, then granulating, weighing, and packaging.    USE - Process for producing organic fertilizer from organic waste (claimed).    ADVANTAGE - The process requires little fermenting area for producing organic fertilizer with fermenting time of 8-10 days, has little investment cost, and does not use electricity and oil in the whole fermenting process.
NOVELTY - Treatment of a papermaking wastewater comprises adding Agrobacterium tumefaciens GXUNC1 (CGMCC 3455) to an activated sludge.    USE - Method for the treatment of a papermaking wastewater or industrial wastewater (claimed).    ADVANTAGE - The method does not need to increase device investment, enhances flocculation activity, and shortens treating time.
NOVELTY - Producing general flavone of Dendranthema morifolium (Ramat.) growing in Bozhou comprises: (i) extracting D. morifolium (Ramat.) to obtain a crude extract; (ii) purifying the obtained crude extract by using a large-pore resin to obtain the general flavone of D. morifolium (Ramat.), where the large-pore resin is AB-8 type large-pore resin.    USE - The method is useful for producing general flavone of D. morifolium.    ADVANTAGE - The method: produces more than 50-75% of the general flavone with high purity and relatively good yield, is environmental friendly and is suitable for large scale industrialization.
NOVELTY - A method comprises (a) culturing a first organism in the presence of a carbon source under conditions suitable for the organism to oxidize the carbon source, where the organism produces carbon dioxide (CO2) as part of the oxidation process; and (b) culturing a second organism in the presence of CO2 produced in (a) under conditions suitable for the second organism to reduce the CO2, where the organism produces a carbon substrate as part of the reduction process.    USE - The method and bioreactor are used for converting a carbon source into a lipid (claimed).    ADVANTAGE - The present invention provides bioprocess and microbe engineering for total carbon utilization in biofuel production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a bioreactor comprising (a) an aerobic fermentor, the aerobic fermentor comprising (i) a carbon source, (ii) an organism oxidizing the carbon source and generating CO2 and (iii) an outflow, through which the CO2 is removed from the fermentor; (b) an anaerobic fermentor comprising (i) an organism reducing CO2, and (iii) an inflow providing CO2 to the fermentor, where the inflow is connected to the outflow of (a) (iii).
NOVELTY - A green fertilizer comprises (pts. wt.): animal manure (10-30), organic accessory material (70-90) and efficient biological strain (0.05-0.3).    USE - Green fertilizer for vegetable, fruit tree, tea, tobacco leaf, tomato, flower and culturing of gardening (claimed).    ADVANTAGE - The fertilizer has simple preparation, natural, rich and easy to obtain raw material. It greatly improves labor efficiency, lightens labor intensity, reduces production cost, and obtains stable performance and high mass. The resource can be recycled.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of the fertilizer; and    (2) use of green fertilizer for culturing vegetable and fruit tree    The production of the fertilizer comprises:    (A) mixing animal manure, organic accessory material and efficient biological strain, and stirring for 8-10 minutes with a stirrer;    (B) heating to 60-65 degrees C, and fermenting for 2-3 days to kill pathogenic bacteria and parasitic ovum;    (C) turning the pile with turning machine for 3-4 days each time, turning pile for 3-4 times, fermenting for 10-12 days, drying or drying in sum, and sampling to detect;    (D) crushing qualified substance with crusher, and passing through sieve by selector, where bore diameter of sieve is 4-6 mm; and    (E) measuring sieved fertilizer to pack, and obtaining desired fertilizer.    The use of the fertilizer comprises scattering, strip applying, ditching or ditch circular groove, applying 80-150 kg in each acre, covering soil to compress after applying fertilizer along with watering to well develop the fertilizer effect.
NOVELTY - Bactericide is produced by selectively breeding and compounding microbial bacterium group in a methane tank at low temperature conditions.    USE - As bactericide.    ADVANTAGE - The bactericide can be prepared simply and cost-effectively, improves utilization ratio of the methane tank of Northern areas in winter and popularization degree of methane in rural areas, and improves life quality of rural population and environment.
NOVELTY - A synthetic fuel comprises (wt.%): components A (60-90) comprising biomass powder; components B (10-60) comprising residue after cutting, residue after bucking and residue after processing; and components C (5-50) comprising coal powder.    USE - Synthetic fuel.    ADVANTAGE - The fuel has simple processing method, good burning resistance, high thermal value and easy storing and transporting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing the fuel which comprises preparing components A, B and C into powder; mixing the components; and pacing and storing material.
NOVELTY - The structure has a cap (12) equipped on a top side of a housing (10), and a guide projection (22) and a vent installed at a bottom of a fermentor (20). A stirring axis is installed in an inner side of the fermentor and fixed with a tie bar. An agitating blade (45d) shatters food waste to pieces. A microorganism nozzle pipe is installed at an upper end of the fermentor for jetting moisture to a curved inner surface of the fermentor. A collection box takes away food waste discharged through an exhaust pipe to an outer side.    USE - Discharge structure for an herbal medicine and food waste disposer utilized in a dining room.    ADVANTAGE - The vent is installed at the bottom of the fermentor, thus preventing blockage of the vent due to the pulverized residue. The structure ensures mucilage generation through fermentation of the micro-organism within the fermentor, thus mixing the micro-organism and medicine, and hence taking away the waste food through the collection box in a smooth manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an herbal medicine and food waste disposer.    Housing (10)    Cap (12)    Fermentor (20)    Guide projection (22)    Agitating blade (45d)
NOVELTY - The method involves providing a dry solid biomass in first containers (2a, 2b). The first containers are filled with one set of liquid digestates. The first containers are subjected to a fermentation process to dispose produced biogas i.e. methane. The outgoing biogas is introduced into a second container (5). The first containers are filled with another set of liquid digestates, where the two liquid digestates are removed from the first containers.    USE - Method for fermenting a dry solid biomass in a horizontal reactor. Uses include but are not limited to garden waste such as vegetable and fruit waste, grass, weeds, hedge and leaves.    ADVANTAGE - The method performs warming and fermenting operations in a quick and an inexpensive manner, saves time, reduces pre-treatments such as cutting, sieving and mixing of the biomass and avoids physical contaminants such as sand and stones.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for fermenting a dry solid biomass in a horizontal reactor comprising a gas pipe connected with two containers.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a dry solid biomass fermenting device.    Dry solid biomass fermenting device (1)    Containers (2a, 2b, 5)    Liquid line (8)    Removable cover (10)
NOVELTY - Building a steroid-6 beta ,7 beta -methylene structure by cascade reaction, comprises performing methylation reaction on epoxy steroid compound (I) by using methylating reagent under complexing action of inorganic metal salt or organic metal compound and triggering action of a trigger to obtain hydroxy-6 beta ,7 beta -methylene-steroid compound.    USE - The method is useful for building a steroid-6 beta ,7 beta -methylene structure by cascade reaction.    ADVANTAGE - The method: utilizes easily available and low cost materials, has less reaction steps, is simple, exhibits high three-dimensional selectivity for building 6 beta ,7 beta -methylene structure unit, prepares the product with high yield and is suitable for industrial production.    DETAILED DESCRIPTION - Building a steroid-6 beta ,7 beta -methylene structure by cascade reaction, comprises performing methylation reaction on 3 beta -R3O-7 alpha -R7-5 alpha ,6 alpha -epoxy-steroid compound of formula (I) by using a methylating reagent under complexing action of an inorganic metal salt or an organic metal compound and triggering action of a trigger to obtain 3 beta -R3O-5 alpha -hydroxy-6 beta ,7 beta -methylene-steroid compound of formula (II).    R3 = H, alkyl, acetyl, benzyl, benzoyl, butyl, neopentyl, trialkylsilyl, haloalkylsilyl or butyl dimethyl silyl;    R7 = OH, benzenesulfonyloxy, benzoyloxy, para-toluenesulfonyloxy, acetoxy, trimethylsiloxy, I, Br or Cl;    -R15-R16- = -CH2-CH2-, cyclopropane-1,2-diyl, -CH2-CH(Br)-, -C(OH)-CH2-, -C(OR1)-CH2-;    -Q- = -C(OH)-, -C(=O)-, 1,3-dioxolane-2,2-diyl, dihydrofuran-2(3H)-one-5,5-diyl, -C(OH)(CH2-CH2-CH2-OH)-, -C(OH)(CH2-CH2-CH(=O))- or -C(OH)(CH2-CH2-CH(OR1)(OR1))-; and    R1 = CH3 or C2H5.
NOVELTY - A methane enriched gas producing system comprises reactor having combining gas inlet on its end and methane enriched gas outlet on the other end; reaction-absorption area between the combining gas inlet and methane enriched gas outlet in the reactor, and having methanation catalyst and adsorbent for adsorbing carbon dioxide and sulfide gas; and adsorbent regenerator communicated with the reactor through a waste adsorbent transport pipeline and a regeneration adsorbent transport pipeline.    USE - System for producing CH4 enriched gas (claimed).    DETAILED DESCRIPTION - Methane enriched gas producing system comprises reactor having combining gas inlet on its end and methane (CH4) enriched gas outlet on the other end; reaction-absorption area between the combining gas inlet and CH4 enriched gas outlet in the reactor, and having methanation catalyst and adsorbent for adsorbing carbon dioxide (CO2) and sulfide gas; and adsorbent regenerator communicated with the reactor through a waste adsorbent transport pipeline and a regeneration adsorbent transport pipeline. The waste adsorbent generated in the reactor enters the adsorbent regenerator through the waste adsorbent transport pipeline and regenerated in the adsorbent regenerator. The regeneration adsorbent is circulated to the reactor through the regeneration adsorbent transport pipeline.
NOVELTY - Nickel/silicon carbide catalyst is used in converting synthesis gas into methane, and comprises silicon carbide as carrier and metal nickel as active component. The nickel in the catalyst is present at 1-20%.    USE - Ni/SiC catalyst is used in converting synthesis gas into methane.    ADVANTAGE - The catalyst has strong anti-abrasion capability, high activity, and strong carbon deposition resistance, and is operated at high air speed and high pressure.
NOVELTY - An E4 ethanol and diesel oil mixed fuel comprises (pts.vol.) absolute ethyl alcohol (4), diesel oil (96) and ethylene glycol monomethylether or ethylene glycol monomethyl ether (0.1-0.3). The ethanol is absolute ethyl alcohol or industrial alcohol. The diesel oil is mixture of finished product diesel oil, straight-run diesel oil and secondary processing diesel oil.    USE - An E4 ethanol and diesel oil mixed fuel.    ADVANTAGE - The fuel has low quality requirement to base diesel oil, and is suitable for all diesel oils. Compared with the base diesel oil, there is no impact to power performance of the engine. Evaporating property of the mixed fuel is reduced and transporting and using safety can be raised. Mixed property and solubility in water for the diesel oil and ethanol can be raised and optimized.
NOVELTY - Complex microbial organic fertilizer is prepared by adding materials comprising (pts.wt.) castor bean meal (1-50), cow or chicken manure (1-50), rice husk bran (1-20), bone meal (1-10), straws (1-80), and rape oil cake (1-40) to Saccharomyces cerevisiae liquid (0.5-0.8 wt.% of the materials), Bacillus laterosporus liquid (0.1-0.5 wt.% of the materials), B. megaterium liquid (0.1-0.5 wt.% of the materials); fermenting; and adding (pts.wt.) urea (1-20), calcium superphosphate (0.5-10), and potassium sulfate (0.5-15). It has water content of less than or equal to 30%.    USE - Complex microbial organic fertilizer.    ADVANTAGE - The organic fertilizer can fully replace the chemical fertilizer as base fertilizer or additional fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of complex microbial organic fertilizer comprising: (A) taking castor bean meal, cow or chicken manure, rice husk bran, bone meal, straws, rape oil cake, urea, calcium superphosphate, and potassium sulfate; (B) uniformly mixing castor bean meal, cow or chicken manure, rice husk bran, bone meal, straws, and rape oil cake; adding S. cerevisiae liquid; after 12 hours, feeding air to perform aerobic fermentation; controlling fermentation temperature at 40-50 degrees C; and controlling humidity of the material at 40-50%; (C) fermenting using S. cerevisiae for 6-12 days; and adding B. laterosporus liquid and B. megaterium liquid to perform heap fermentation for 2-3 days; and (D) adding urea, calcium superphosphate, and potassium sulfate; and mixing uniformly to obtain the product.
NOVELTY - The material has a combination of combustible and flammable cellulose fatty acid ester derivatives, where 30 to 70 percent mass/mass of cellulose and 30 to 70 percent mass/mass of fatty acid ester are combined. Saturated fatty acid, hexadecanoic and octadecaanzuur are combined together. Inorganic salt contains sodium bicarbonate. Flammable cellulose is derived from an organic source i.e. wood flour and sawdust. Waste cooking oil contains fatty acid ester derivative.    USE - Combustible material i.e. artificial fire log, for use in a home to provide heat.    ADVANTAGE - The material is easier to purchase and store, and has high heating values, so that the material is easy and safe to light, thus maintaining fire during burning.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a mixture of combustible materials.
NOVELTY - The nitrogen replacing device has an oxygen separator, a hydrogen separator and a nitrogen replacing pipeline including a single-way valve (3) and a first stop valve (4) connected between the two separators. The nitrogen replacing pipe includes a second stop valve (5) and a third stop valve (6). The third stop valve is communicated between the inputting end of the nitrogen and the first stop valve. The second stop valve is communicated between the first stop valve and third stop valve.    USE - Nitrogen replacing device for hydrogen manufacturing system.    ADVANTAGE - Exhibits high security and stability while normal running or in the standby state. Improves efficiency. Enables the operator to easily detect and treat with simple and convenient operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the nitrogen replacing device for hydrogen manufacturing system.    Single-way valve (3)    First stop valve (4)    Second stop valve (5)    Third stop valve (6)
NOVELTY - Compound fertilizer comprises (in parts): sludge or mud (70-80), where fertilizer contains nitrogen (4-10), phosphorus (4-10) and potassium (4-10).    USE - Compound fertilizer.    ADVANTAGE - The compound fertilizer has capability of turning waste into wealth and low manufacturing cost, and can effectively reduce pollution of environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing compound fertilizer, which involves:    (A) collecting sludge or mud from lakes, rivers, ponds, wetland, sewer or wastewater treatment factory;    (B) dehydrating and crushing the sludge or mud to obtain dry sludge or mud raw material;    (C) weighing (in pts.wt.): sludge, mud or their mixtures (70-80), where fertilizer contains nitrogen (4-10), phosphorus (4-10) and potassium (4-10);    (D) placing raw materials in a stirrer;    (E) adding 10-20 pts.wt. of water in stirrer to obtain the compound fertilizer raw materials;    (F) preparing grains of the compound fertilizer raw materials; and    (G) drying the finished product of compound fertilizer to obtain base fertilizer.
NOVELTY - The apparatus has two cryogenic rectifying towers and two fin type heat exchangers. The first cryogenic rectifying tower has top which is connected to second cryogenic rectifying tower via pipeline, and bottom is connected to a gas-liquid separator. The separator is connected to second fin type heat exchanger which is respectively connected to first fin type heat exchanger and second cryogenic rectifying tower. The second cryogenic rectifying tower and gas-liquid separator form the cyclic path.    USE - Apparatus for recycling and separating components in synthesis ammonia released gas and purge gas.    ADVANTAGE - The apparatus is simple in structure and can perform stable operation. By using the apparatus, production cost and pollution to environment can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for recycling and separating components in synthesis ammonia released gas and purge gas.
NOVELTY - The air and biogas flow gauges (1,4) are connected with biogas desulfurization reaction zone through air and methane intake automatic adjusting valves. The one ends of oxygen alarms (6,13) are connected with oxygen probes (5,11). The one ends of hydrogen sulfide alarms and oxygen alarms are connected with the hydrogen sulfide and oxygen probes. A data collecting and analyzing regulating device (8) is connected with other ends of hydrogen sulfide and oxygen alarms, air and methane intake automatic adjusting valves and dissolved oxygen probe.    USE - Automatic control system of desulfurizing biogas.    ADVANTAGE - The gas content of the biogas desulfurization reaction zone can be monitored efficiently and safely. The gas content of the biogas exhaust zone can be monitored on line by the user. The purified biogas can be safely used. The biogas can be desulfurized continuously through the automatic control process to recover the elementary sulfur.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the automatic control system of desulfurizing biogas. (Drawing includes non-English language text)    Air flow gauge (1)    Biogas flow gauge (4)    Oxygen probes (5,11)    Oxygen alarms (6,13)    Data collecting and analyzing regulating device (8)
NOVELTY - The hydrogen energy oil-saving system includes a microcomputer chip (5) that is connected to a power cord (1), a ground wire (2), an accelerator signal wire (3) and an engine rotating speed signal wire (4), and that is connected to a power supply controller (7) by one control signal wire (6). The power supply controller is connected to a pure water electrolytic cell (9) by another control signal wire (8). The pure water electrolytic cell is connected to an engine (11) by a gas pipe (10).    USE - Hydrogen energy oil-saving system.    ADVANTAGE - Provides a hydrogen energy oil-saving system that has simple structure, small volume, light weight, high intelligence property and high oil-saving efficiency, and that can save oil by more than 20 percent.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the hydrogen energy oil-saving system. (Drawing includes non-English language text).    Power cord (1)    Ground wire (2)    Accelerator signal wire (3)    Engine rotating speed signal wire (4)    Microcomputer chip (5)    Control signal wires (6,8)    Power supply controller (7)    Pure water electrolytic cell (9)    Gas pipe (10)    Engine (11)
NOVELTY - Preparing rocuronium bromide having high purity, comprises mixing anti-solvent having low boiling point with rocuronium bromide containing organic solvent and/or impurities, removing organic solvent and/or impurities in the rocuronium bromide, where the organic solvent and/or impurities can be dissolved in the anti-solvent having low boiling point and rocuronium bromide is insoluble or is difficult to dissolve in the anti-solvent having low boiling point, thus the rocuronium bromide precipitates or crystallizes to obtain the product without organic solvent and/or impurities.    USE - The method is useful for preparing rocuronium bromide having high purity.    ADVANTAGE - The method: performs extraction and separation processes at a temperature close to the room temperature, thus retains all the active ingredients of the product; produces low organic solvent residue that can not be detected; has simple operation process; and is environment-friendly and saves energy.
NOVELTY - Producing a biogas comprises: (a) producing a biogas feed stream (202) in an anaerobic digestion system (200); (b) compressing the biogas feed stream; (c) passing at least a portion of the compressed biogas feed stream to a separation unit capable of discharging a purified, methane-containing product gas from it and discharging a low-quality gas stream comprising a minor amount of methane, carbon dioxide and other impurities present in the biogas feed stream; and (d) utilizing the low-quality gas stream as a fuel in the anaerobic digestion system.    USE - The method is useful for producing a biogas (claimed), which is useful as a fuel for the facility and/or digester boiler.    ADVANTAGE - The method: utilizes the intermediate-quality blended gas as a fuel, which eliminates the need for an expensive and maintenance intensive flare and provides for complete utilization of all digester gas, thus reducing the environmental impact of the anaerobic digester; utilizes the pressure swing adsorption (PSA) system, which produces a high-British thermal units fuel that can be sold directly to the pipeline or converted to compressed natural gas or liquid natural gas; utilizes the wasted tail gas as a fuel supplement; and reduces or eliminates the use of the flare, thus reducing the capital cost of PSA system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the process of utilizing the tail gas from a membrane separation unit.    Anaerobic digester (200)    Biogas feed stream (202)    Membrane unit (204)    Stream (206)    Permeate (208)
NOVELTY - A light oil composition comprises base light oil, 2C alcohol and 4C alcohol. The volume ratio of 4C alcohol with respect to 2C alcohol, is 0.2-1.0. The volume ratio of 2C and 4C alcohols with respect to base light oil is 0.1-1.2. The cetane number of light oil composition is 39 or more.    USE - Light oil composition is used for diesel engine. Uses include but are not limited to motor vehicles, hybrid vehicles, plug-in hybrid vehicles, electric vehicles and fuel-cell vehicles.    ADVANTAGE - The light oil composition is economical, has favorable diesel-engine compatibility, premixed compression ignition (PCI) combustion property under low and high load conditions, and improved fuel consumption property with reduced discharge amount of exhaust gases (e.g. carbon dioxide and nitrogen oxides).
NOVELTY - Producing product mixture comprising hydrocarbons from vegetable and animal oils and fats, comprises thermally and catalytically cleaving the vegetable and animal oils and fats in a concentrated solution of alkali hydroxide and/or carbonate. The solution comprises the alkaline components in a ratio of its eutectic mixture and preferably comprises water (at least 5%) and dissolved aluminate.    USE - The hydrocarbon mixture obtained by the method is useful as motor fuel.    ADVANTAGE - The method: exhibits reduced cleavage temperature; and produces the product with high yield and with small amount of unsaturated compounds and aromatics.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the process flow for producing a product mixture comprising hydrocarbons. Drawing includes non-English language text.    Reactor (1)    Stirrer (2)    Cooler (3)    Product supply (4)    Oil end product (5)
NOVELTY - The gas alarm has measurement unit that measures different reference resistance values of gas detection layer when layer temperature reaches predetermined temperature respectively. The alarm determines whether gas type is hydrogen gas when first and third reference resistance values are smaller than respective resistance value. Hydrogen concentration is calculated from second resistance value. Hydrogen gas detection warning is outputted from warning unit when concentration of hydrogen gas is more than predetermined density.    USE - Alarm for warning about detection of gas such as hydrogen, methane and carbon monoxide (all claimed). Can also be used for detecting town gas, methanol and propane.    ADVANTAGE - The gas alarm selectively detects type of gas by setting period of cold condition, so that power consumption of gas alarm can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for detecting gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow chart illustrating method for detecting gas.(Drawing includes non-English language text).
NOVELTY - An organic-refuse composting container (1) has an organic-refuse storage chamber (7) which accommodates organic refuse and a fermentation base material. The organic refuse is fermented and composted in the organic-refuse storage chamber. A vent hole is connected to the organic-refuse storage chamber. Porous components (13,14) are interposed at intervals between vent hole and organic-refuse storage chamber.    USE - Container is used for composting organic refuse (claimed) discharged from factory, restaurant and house.    ADVANTAGE - The container efficiently and economically ferment organic refuse within short period of time, without generation of offensive odor. The foreign material mixed in the organic refuse is easily removed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic-refuse composting method.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the organic-refuse composting container.    Organic-refuse composting container (1)    Container main component (2)    Inner cover (3)    Organic-refuse storage chamber (7)    Porous components (13,14)
NOVELTY - A gas manufacturing apparatus comprises water mixture production part which produces water mixture from liquids other than water and water, and methane gas production part which generates methane gas by using water mixture as raw material. Liquids other than water are oil, dimethyl ether, tar, benzene, toluene, xylene, and/or hydrocarbon liquids. Oil contains naphtha, gasoline, kerosene, light oil, A heavy oil, B fuel oil, C heavy oil, crude oil, animal oil or waste oil.    USE - A gas manufacturing apparatus.    ADVANTAGE - Water in steam reforming process is significantly reduced, catalyst is not necessary, and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gas manufacturing apparatus. (Drawing includes non-English language text).    Water tank (11)    Pump (12)    Flowmeter (13)    Flow control valve (14)    Liquid tank (15)
NOVELTY - Method of treating a biomass material to produce a torrefied product comprises: (a) preheating the biomass material to a temperature of 80-100 degrees C; (b) drying the biomass material until the biomass material has a maximum water content of no more than 3%; (c) applying microwave radiation to the dried biomass material of 3-8 GHz to transfer heating energy to the dried biomass material to reach a temperature of 230-280 degrees C and causing torrefaction of the biomass material; and (d) cooling the biomass material.    USE - The method is useful for treating a biomass material to produce a torrefied product, preferably solid torrefied bio-fuel.    ADVANTAGE - The method: can be able to produce a more homogeneous refined pellet product at faster processing rate by the adoption of simultaneous heating on the inside and the surface (thermal heating and microwave heating) of pellets; is efficient for torrefaction of the dried biomass and for heat penetration into small sized biomass materials such as pellets; produces a torrefied fuel which consumes less energy during the torrefaction process making the torrefied fuel more economically feasible and with better energy balances; and avoids the risk of triggering the exothermic pyrolysis process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of stages of the torrefaction process.    Chamber (11)    Pre-drying chamber (21)    Hopper (22)    Conveyor (24)    Gas burner. (26)
NOVELTY - A biogas slurry treating system of biogas engineering has sedimentation pool, adjusting pool and anaerobic reaction device successively connected. A biochemical ceramic after-treatment device is connected with the anaerobic reaction device. The anaerobic reaction device is internally provided with a spiral biological filling material, which is fixed by PVC plate arranged with eyelets. A water inlet is arranged at a side wall lower part of the anaerobic reaction device; a water outlet and a sampling opening are provided at the side wall upper part; and an air outlet is provided at the top part.    USE - Biogas slurry treating system of biogas engineering.    ADVANTAGE - The system has high treatment efficiency, small coverage, low cost and convenient maintenance and use.    DETAILED DESCRIPTION - The spiral biological filling material is a long spiral strip-like structure formed by the arch-shaped structure by forward and reverse folding in the cylindrical spiral face, where central angle of the arch-shaped structure is 60-120 degrees . Width of the cylindrical spiral face is 1.0-2.0 cm and thickness is 0.10-0.20 mm. Specific surface area of the spiral biological filling material is 2800-3000 m2/m3.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the biogas slurry treating system of biogas engineering.
NOVELTY - A solar methane generator comprises polyurea elastomer materials of waterproof anti-corrosive coating sprayed on inner and outer walls. One end of high-intensity polyvinyl chloride (PVC) radiating pipe is connected with solar heat collector and other end enters ground, and is uniformly provided with rings around methane generator and returns to ground to connect water return pipe of solar heat collector. A feed inlet is located on upper cover of methane generator. A discharge port is provided with discharge pipe on one side at bottom of the generator.    USE - Solar methane generator.    ADVANTAGE - The generator has mobility and convenient installation, and is suitable for production and life of countryside households and enterprises and public institutions.    DETAILED DESCRIPTION - A solar methane generator comprises polyurea elastomer materials of waterproof anti-corrosive coating sprayed on inner and outer walls. One end of high-intensity PVC radiating pipe is connected with solar heat collector and other end enters ground, is uniformly provided with rings around methane generator and returns to ground to connect water return pipe of solar heat collector. A feed inlet is located on upper cover of methane generator. A discharge port is provided with discharge pipe on one side at bottom of the generator. One end of discharge pipe is connected with slurry pump at bottom of the generator. The other end rises to ground to form discharge port. A gas pressure meter is arranged on discharge pipe on upper part of the generator cover. A first pressure sensor and second pressure sensor are arranged on upper part inside the generator.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing a solar methane generator. (Drawing includes non-English language texts).
NOVELTY - A biological organic compound fertilizer is manufactured by mixing (pts. wt.) human and animal manures (20-30) , straw and saw dust fermented mixture (20-30) , humic acid (2-6), biological bacterial manure (5-8), nitrogenous fertilizer (8-15), phosphatic fertilizer (8-15) and potash fertilizer (8-15); fermenting the mixture at 70-85 degrees C for 10 days; stirring; pelletizing; drying; and screening using 10 mesh sieved.    USE - Method of manufacturing a biological organic compound fertilizer.    ADVANTAGE - The manufactures product that improves crop quality, improves production yield, improves structure of soil and reduces hardening of the soil.
NOVELTY - A bio-organic fertilizer is manufactured by, mixing (pts. wt.) pig manure (20-30), chicken manure (20-30), Brevibacillus laterosporus (8-15), borax (5-8) and clay (20-35); subjecting mixture to aerobic fermenting at room temperature; stirring; pelletizing; drying; and screening using 20-mesh sieve.    USE - Method of manufacturing a bio-organic fertilizer.    ADVANTAGE - The method manufactures product that improves soil texture, accelerates growth of crop, improves production yield, reduces plant diseases and pest, and have reduced pesticide residue.
NOVELTY - A fertilizer is produced by processing a biomass, gasifying with a gasifying oxidant to produce syngas, purifying the syngas by separating all of the ash from the syngas, removing all carbon monoxide and carbon dioxide from the syngas, converting the syngas into ammonia, converting ammonia into an ammonia product, and mixing at least some of the ammonia product with at least some of the separated ash to produce a fertilizer.    USE - Method for producing a fertilizer (claimed). No biological data given.    ADVANTAGE - The method enhances the quality of the environment by reducing the quantity of material going to landfills, reduces green house gas emission by using materials that can be burned, and conserves energy resources by providing a useful product that can be burned or tossed into a landfill to dispose them.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing fertilizer from biomass.
NOVELTY - Operating a water electrolysis system comprises determining whether or not the water electrolysis apparatus is shut down; releasing pressure on the cathode side when it is determined that the water electrolysis apparatus is shut down; and operating, under a condition in which a release of pressure on the cathode side is completed, the water circulation apparatus until a concentration of hydrogen remaining on the anode side is a specified value or less.    USE - The method is used for operating a water electrolysis system (claimed).    ADVANTAGE - The blower is set to a large capacity, thus causing an uneconomical problem.
NOVELTY - The sewage processing device has a micro nanometer air flotation pool (I) with oxygen-enriched water outlet (5) that communicates with a distributing pipe (9) set at bottom of a planting matrix layer (11) by an artificial wetland processing pool (III). A clear water outlet (15) at the bottom of wetland processing pool communicates with a buffer sedimentation pool (16) at the bottom of a depth processing pool (IV). The sedimentation pool connects with a discharging pipe (17) through a top guiding hopper. A suspension separating pool communicates with air flotation sludge collecting pool (II).    USE - Micro nanometer air flotation vertical under flow type sewage processing device for artificial wetland.    ADVANTAGE - The processing device employs the micro nanometer air flotation device to improve the removing efficiency for blue-green algae and suspended solids, to strengthen the aerobic processing effect of an artificial wetland system, effectively lower total suspended solids pollution load and to avoid from blocking the artificial wetland. The processing device allows work that is stable and reliable. The capital construction cost of the device is low, the maintaining management is convenient, chemical reagent need not be thrown, the processing cost is low and the service life is above 10 years.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro nanometer air flotation vertical under flow type sewage processing device for artificial wetland.    Oxygen-enriched water outlet (5)    Distributing pipe (9)    Planting matrix layer (11)    Clear water outlet (15)    Buffer sedimentation pool (16)    Discharging pipe (17)    Micro nanometer air flotation pool (I)    Air flotation sludge collecting pool (II)    Artificial wetland processing pool (III)    Depth processing pool (IV)
NOVELTY - Device for producing organic liquid fertilizer from kitchen waste, comprises a pulverizing and separating unit for organic sundries, a processor for further pulverizing the organic sundries, a microbial tank for culturing microorganisms, a tank for microorganism activating agent, and a fermentation tank. The fermentation tank is used for fermenting mixed liquor comprising components chosen from organic sundries, microorganisms, activating agent of microorganisms and water. The outlet of the pulverizing and separating unit is connected to the processor.    USE - The device is useful for producing organic liquid fertilizer from kitchen waste.    ADVANTAGE - The device manages kitchen waste.    DETAILED DESCRIPTION - Device for producing organic liquid fertilizer from kitchen waste, comprises a pulverizing and separating unit for organic sundries, a processor for further pulverizing the organic sundries, a microbial tank for culturing microorganisms, a tank for microorganism activating agent, and a fermentation tank. The fermentation tank is used for fermenting mixed liquor comprising components chosen from organic sundries, microorganisms, activating agent of microorganisms and water. The outlet of the pulverizing and separating unit is connected to the processor. The outlet of tank for activating agent is connected to the processor and the microbial tank. The fermentation tank comprises an overflowing and aeration stirring tank, and an anaerobic reaction tank. The aeration stirring tank and the processor form a first circulation loop. The anaerobic reaction tank and the microbial tank form a second circulation loop.
NOVELTY - A carbon dioxide methanation catalyst comprises a catalyst carrier comprising a compound oxide of rare earth and other metal; and 1-15% nickel.    USE - A carbon dioxide methanation catalyst.    ADVANTAGE - The catalyst achieves 100% carbon dioxide converting rate, 100% methane selectivity, and a methane yield of greater than 1000 g/kg-hour.    DETAILED DESCRIPTION - A carbon dioxide methanation catalyst comprises a catalyst carrier of formula AxB'yOz comprising a compound oxide of rare earth and other metal; and 1-15% nickel.    A=rare earth metal (including La or Ce);    B'=Group IIB, IIIA, VIA, IVB, VB, and/or VIB metal (including Zn, Al, Fe, and/or Ti);    x=0-1;    y=0-2; and    z=2-4.
NOVELTY - A fertilizer is produced by concentrating glutamic acid fermentation liquid waste; reducing water content in material liquid; producing well melted material into fertilizer granules with spiral granulator; rapidly cooling produced fertilizer granules with water and bringing fertilizer granules out of the granulator; rapidly dehydrating fertilizer granules again in dehydrator; and coating dehydrated fertilizer granules with coating agent, drying with fluidized bed, recycling dust, putting fertilizer granules into storehouse, packing with automatic packer and putting into storehouse.    USE - Method for producing fertilizer (claimed).    ADVANTAGE - The method can fully make use of resource value of glutamic acid fermentation liquid, and has simple process operation an, small device investment.    DETAILED DESCRIPTION - Fertilizer is produced by:    (A) concentrating glutamic acid fermentation liquid waste with 6-7 baume degrees to 25-27 baume degrees;    (B) concentrating material with 25-27 baume degrees to 45-47 baume degrees;    (C) reducing water content in material liquid of material with 45-47 baume degrees below 3% in melting tank under vacuum state;    (D) producing well melted material into fertilizer granules with spiral granulator;    (E) rapidly cooling produced fertilizer granules with water and bringing fertilizer granules out of the granulator;    (F) rapidly dehydrating fertilizer granules again in dehydrator; and    (G) coating dehydrated fertilizer granules with coating agent, drying with fluidized bed, recycling dust, putting fertilizer granules into storehouse, packing with automatic packer and putting into storehouse.
NOVELTY - Copper resinate preparation, prepared by: (a) milling dried pine needles and sieving by a 60-mesh sieve or milling pine needles to form slurry and sieving by a 60-mesh sieve; (b) extracting pine needle powder or pine needle slurry by acetone for 3 hours; (c) filtering extract by a 100-mesh sieve to obtain a filtrate, distilling filtrate to recover acetone to obtain a pine needle paste extract; (d) mixing obtained extract, ethyl acetate, Tween-80 (RTM: Polysorbate 80) and copper sulfate solution (0.5 mol/l) in volume ratio of 1:2:3:3 to obtain a copper resinate raw liquid, is claimed.    USE - The copper resinate preparation is useful for preventing aphids (claimed).    ADVANTAGE - The copper resinate preparation: is simple and safe to prepare; is economical and ecofriendly; and has high aphids preventive effect (85%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use of copper resinate preparation in preventing aphids, comprising diluting the copper resinate raw liquid by water (300-500 times) and spraying to the surfaces of plants with aphids.
NOVELTY - The product has recesses, holes or air holes provided with specific shape and diameter such that a location of a notch is varied based on the shape and the diameter of the recesses, where the product is made of sawdust and/or paraffin.    USE - Solid form fuel product e.g. fire wood and fire block.    ADVANTAGE - The product is selected based on type of stove and personal preference, so that the product is utilized for a long period of time. The recesses affect local air flow around and into the recesses such that uniform combustion of fuel is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a solid form fuel product.
NOVELTY - Biomass pellet fuel producing involves crushing biomass raw material less than 200 mm size, and then tempering and curing the crushed raw material. The cured raw material is stirred spirally, and then the stirred material is crushed mechanically to improve the granularity and flexibility of the material. Active organic matter is extruded to obtain natural bonding agent. The active organic matter includes water and tar. The tempered and cured biomass raw material is stirred and dried, and then the dried material is extruded to obtain biomass pellet fuel with granularity of less than 20 mm size.    USE - Method for producing biomass pellet fuel (claimed).    ADVANTAGE - The method enables to produce biomass pellet fuel with high production efficiency in a cost-effective manner.    DETAILED DESCRIPTION - Biomass pellet fuel producing involves crushing biomass raw material less than 200 mm size, and then tempering and curing the crushed raw material. The cured raw material is stirred spirally, and then the stirred material is crushed mechanically to improve the granularity and flexibility of the material. Active organic matter is extruded to obtain natural bonding agent. The active organic matter includes water and tar. The tempered and cured biomass raw material is stirred and dried, and then the dried material is extruded to obtain biomass pellet fuel with granularity of less than 20 mm size. The biomass pellet fuel is cooled in presence of air for controlling moisture content of the biomass pellet fuel less than 10%. An INDEPENDENT CLAIM is also included for an apparatus for producing biomass pellet fuel, which comprises a transmission device, a belt pulley transmission mechanism, a decelerator and a coupler.
NOVELTY - Biodiesel preparing involves feeding aliphatic acid and oxidant in tubular hydrothermal reactor for partially and selectively oxidizing aliphatic acid into unsaturated aliphatic acid and selectively breaking unsaturated bonds for preparing micromolecular saturated aliphatic acid. Dosage of oxidant is 1-10% of oxygen required for completely oxidizing the material oil into carbon dioxide and water. The selectively oxidizing process is performed at 200-350 degrees C and 5-30 MPa for 0.5-10 minutes.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The biodiesel preparation method improves the low-temperature flowing property and oxidation resistance of biodiesel.    DETAILED DESCRIPTION - Biodiesel preparing involves feeding aliphatic acid and oxidant in tubular hydrothermal reactor for partially and selectively oxidizing aliphatic acid into unsaturated aliphatic acid and selectively breaking unsaturated bonds for preparing micromolecular saturated aliphatic acid. Dosage of oxidant is 1-10% of oxygen required for completely oxidizing the material oil into carbon dioxide and water. The selectively oxidizing process is performed at 200-350 degrees C and 5-30 MPa for 0.5-10 minutes. Low-carbon alcohol and micromolecular saturated aliphatic acid are mixed for esterification to prepare high-quality biodiesel. The esterification is performed at 300-400 degrees C and 20-35 MPa for 12-30 minutes.
NOVELTY - The system (100) has a batch-wise operated retort (102) covered with a gas-tight lid, where the retort processes substance in a single batch at a time. The retort, a combustor (104) and a heat buffer (106) are connected in a heat distribution system for distributing heat between the retort, the combustor and the heat buffer. A pipeline system comprises an air supply (112), where a pipe (114) connects the air supply to the combustor. A valve (116) is provided with the pipe. Another pipe (120) connects a manifold (118) to the combustor.    USE - Processing system for processing a substance e.g. biomass and wood. Uses include but are not limited to produce e.g. charcoal, organic acids, liquid distillation product and gaseous distillation product.    ADVANTAGE - The heat produced by combusting the heating fluid e.g. reaction vapor, is temporarily stored in a heat buffer, thus avoiding an additional fuel for heating a retorting process and reducing the processing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing substance e.g. biomass and wood.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a processing system.    Processing system (100)    Batch-wise operated retort (102)    Combustor (104)    Heat buffer (106)    Air supply (112)    Pipes (114, 120)    Valve (116)    Manifold (118)
NOVELTY - An abamectin is prepared by (A) soaking, (B) concentrating, (C) desugaring, (D) crystallizing, (E) recrystallizing, and (F) drying. The step (A) comprises adding dried abamectin dreg and methanol or ethanol into soaking tank at mass ratio of 1:2-8, and continuously stirring for 2-3 hours to prepare mixed suspension liquid; and conveying mixed suspension liquid to helical-conveyer depositing centrifugal and centrifuging at 10-20 m3/hour. The clear liquid separated by centrifugation is processed by procedures of steps (B)-(F).    USE - Method for preparation of abamectin (claimed).    ADVANTAGE - The method exhibits environmental friendly performance, and has short technique period, low preparation cost and high yield coefficient of product.    DETAILED DESCRIPTION - Abamectin is prepared by (A) soaking, (B) concentrating, (C) desugaring, (D) crystallizing, (E) recrystallizing, and (F) drying. The step (A) comprises adding dried abamectin dreg and methanol or ethanol into soaking tank at mass ratio of 1:2-8, and continuously stirring for 2-3 hours to prepare mixed suspension liquid; and conveying mixed suspension liquid to helical-conveyer depositing centrifugal and centrifuging at 10-20 m3/hour. The clear liquid separated by centrifugation is processed by procedures of steps (B)-(F). The liquid is sent back to step (A) to be processed after dreg is dried.
NOVELTY - The device includes treatment pools (1,8), overflow pipes (7,9), a deodorization tank (10), a storage pool(11) and a rich water pipe (12) that are connected in series. A food residue and a drainage outlet pipes (3,6) are arranged at one side of upper portion of pool (1), while an arch-shaped quadrate guide plate (2) is arranged at other side. A spiral propeller (15) is arranged at bottom portion of pool (1). One end of hosing of propeller extends to a power groove (18). The spacing wall of pools is internally provided with a spacing wall of pool (8) and storage pool.    USE - Harmless food waste material treatment device for producing liquid fertilizer.    ADVANTAGE - The device can harmlessly treat the food residues to produce the liquid fertilizer without odor. The fertilizer can be conveyed to the edges of the field at any distance through the pipelines and the pipe network. The operation time of the treatment device can be reduced, and the work required for performing treatment process can be reduced. The waste can be efficiently converted into beneficial materials.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the harmless waste material treatment device.    Treatment pools (1,8)    Arch-shaped quadrate guide plate (2)    Food residue outlet pipe (3)    Drainage outlet pipe (6)    Overflow pipes (7,9)    Deodorization tank (10)    Storage pool (11)    Rich water pipe (12)    Spiral propeller (15)    Power groove (18)
NOVELTY - A hydrogen generator consists of a microbe generation portion for producing microorganisms, a storage unit for storing organic waste from land, a reactor in which the organic waste is reacted with microorganisms provided from the microbe generation portion, and a sea-wave transmission drifting buoy which delivers a transport element by a connected propeller. The movement of transport element inside the reactor carries out up-and-down motion of microorganisms and organic waste and promotes reaction in the absence of water.    USE - Hydrogen generator is used in marine structures e.g. barge (claimed).    ADVANTAGE - The hydrogen generator enables efficient generation of hydrogen by effectively using organic waste.
NOVELTY - Biological organic fertilizer (100 pts.wt.) comprises raw material, which is 0.2-2 pts.wt. of Streptomyces fradiae fungicide.    USE - Biological organic fertilizer used for preventing disease and insect pest on field plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biological organic fertilizer, which involves:    (A) adding powdered rock phosphate and organic matter-decomposing inoculants to raw material to ferment the mixture for 6-12 days;    (B) overturning the mixture for 1-3 times to obtain the fermented organic fertilizer, where weight ratio of raw material, powdered rock phosphate and organic matter-decomposing inoculant is 100:3-20:0.1-0.3;    (C) adding Streptomyces fradiae fungicide to the mixture to ferment it for 3-6 days at less than 40 degrees C and less than 35% moisture content, where weight ratio of fermented organic fertilizer and Streptomyces fradiae fungicide is 100:0.2-100:2; and    (D) crushing and sieving the mixture to obtain powdered biological organic fertilizer at less than 35 degrees C and less than 30% moisture content.
NOVELTY - A biological organic fertilizer from rural waste is prepared by preparing raw material, proportioning nutrition, crushing and mixing, anaerobic fermenting, aerobic fermenting, drying, prilling, parching, checking, packing and storing.    USE - Method of preparing biological organic fertilizer from rural waste (claimed).    ADVANTAGE - The method involves short production period, and optimizes usage of rural organic waste, thus saving energy and protecting the environment. The obtained fertilizer has high fertilizing efficiency. Further, the method is suitable for diverse biological organic fertilizer manufacture and waste treatment.
NOVELTY - Preparation of urea-based compound fertilizer containing phosphate rock powder, comprises spraying urea solution with concentration of 95-99.7 wt.% and temperature of 110-140 degrees C into a fundamental fertilizer containing phosphate rock powder and other elements such as nitrogen, phosphorus, and potassium inside a granulator; rotating and granulating; and sieving to obtain granular nitrogen-phosphorus-potassium compound fertilizer.    USE - Preparation of urea-based compound fertilizer containing phosphate rock powder, preferably granular nitrogen-phosphorus-potassium compound fertilizer (claimed).    ADVANTAGE - The method simplifies the production technology; reduces energy consumption and pollution emission; and improves the quality of fertilizer, which has prolonged fertilizer effect.
NOVELTY - A highly-active earthworm microbial organic fertilizer comprises (wt.%) earthworm manure (35-60), composite fertilizer (25-45) containing nitrogen, phosphorus and potassium, and organosilicon (15-25).    USE - Highly-active earthworm microbial organic fertilizer.    ADVANTAGE - The fertilizer has high microbial activity, and long fertilizer efficiency, water retention and drought resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the fertilizer, comprising collecting poultry manures and fully fermenting manures, allowing earthworm to amplify and fully digest fermented manure to obtain earthworm manures, separating the earthworm and earthworm manure, drying and crushing the collected earthworm manure; and according to characteristic of soil and crop, adding composite fertilizer containing nitrogen, phosphorus and potassium, trace element fertilizer and powder organosilicon and preparing one or two drought-resisting water-saving fertilizer bags.
NOVELTY - An activator comprises (mass%): dextrose (35-40), benzoic acid (28-33) and ammonium sulfate (28-33).    USE - Activator for composting organic solid waste.    ADVANTAGE - The activator solves problem that conventional composting activator has high cost and a long preparing time. The method solves problem that conventional composting method of organic solid waste has long period, slowly start-up and not complete in decomposing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting organic solid waste which comprises adding conditioner into organic solid waste and mixing; adding the activator (0.1-5%), mixing until forming mixture with carbon and nitrogen ratio of 25:35 and water content (55-65%) and pilling to 0.8-1.5 m, where ventilation speed is 0.05-2 m2/minute; when composting temperature rises to 38-45 degrees C, turning for first time, and when composting temperature is over 50 degrees C, turning every 45-50 hours until composting temperature reduces to 38-45 degrees C; and when pile temperature is reduced to environment temperature, finishing composting of the organic solid waste. The conditioner comprises pumice, stalks and sawdust.
NOVELTY - Nitrogen is fixed by culturing bacteria with straw, which uses crop straw to culture nitrogen-fixing bacteria and increase effective nitrogen-fixing bacteria group in soil. The method includes harmlessly treating crop straw, human and animal manure, livestock manure, inorganic fertilizer and biological nitrogen fixation-sensitive elements, vaccinating nitrogen-fixing organism, making it proliferate and reproduce; and transplanting straw cultured nitrogen-fixing bacteria group to soil. The nitrogen-fixing organism are fully grown and reproduced on the straw.    USE - Method for fixing nitrogen (claimed).    ADVANTAGE - The method is easy and simple, which can be completed during agricultural production process. The method can especially increase nitrogen-fixing bacteria in soil and achieve lasting fertility of the soil.    DETAILED DESCRIPTION - Nitrogen is fixed by culturing bacteria with straw, which uses crop straw to culture nitrogen-fixing bacteria and increase effective nitrogen-fixing bacteria group in soil. The method includes harmlessly treating crop straw, human and animal manure, livestock manure, inorganic fertilizer and biological nitrogen fixation-sensitive elements, vaccinating nitrogen-fixing organism, making it proliferate and reproduce; and transplanting straw cultured nitrogen-fixing bacteria group to soil. The nitrogen-fixing organism are fully grown and reproduced on the straw. The straw with the bacteria are expanded to soil again. The nitrogen-fixing organism in soil is increased. The nitrogen-fixing organism is the original soil and is activated and revived because of obtained survival food. Activity is started, the proliferation and breeding are continued.
NOVELTY - A polypeptide with alcohol dehydrogenase activity comprising a polypeptide having a 349 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, polypeptide exhibiting 90% of more homology with the amino acid sequence of SEQ ID NO: 1, and polypeptide encoded by a polynucleotide comprising a 1050 base pair sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The polypeptide is useful for producing bioethanol (claimed).    ADVANTAGE - The polypeptide produces high yield of ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide encoded by the above-mentioned polypeptide;    (2) vector comprising the above-mentioned polynucleotide;    (3) transformant obtained by transforming a host cell containing the vector; and    (4) method for producing bioethanol, involves culturing the transformant in culture medium containing carbon source and collecting ethanol from the medium.
NOVELTY - A polypeptide with alcohol dehydrogenase activity comprising a polypeptide having a 349 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, polypeptide exhibiting 90% of more homology with the amino acid sequence of SEQ ID NO: 1, and polypeptide encoded by a polynucleotide comprising a 1050 base pair sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The polypeptide is useful for producing bioethanol (claimed).    ADVANTAGE - The polypeptide produces high yield of ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide encoded by the above-mentioned polypeptide;    (2) vector comprising the above-mentioned polynucleotide;    (3) transformant obtained by transforming a host cell containing the vector; and    (4) method for producing bioethanol, involves culturing the transformant in culture medium containing carbon source and collecting ethanol from the medium.
NOVELTY - A dendritic platinum catalyst comprises shape-controlled platinum nanoparticles.    USE - Dendritic platinum catalyst is used for manufacture of fuel cell (claimed).    ADVANTAGE - The fuel cell manufactured using dendritic platinum catalyst has excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of dendritic platinum catalyst, which involves mixing platinum salt and surfactant, adding reducing agent to mixture and then heating.
NOVELTY - Wood dust is mixed in ratio of 1:1 as to volume with liquid manure of cattle stock with natural moisture content of 80-90%. Then, the obtained mixture is formed and subject to drying in natural conditions.    USE - Power industry.    ADVANTAGE - Simplifying the technological process, excluding energy consumption during preparation of components, and calorific capacity and mechanical strength of fuel elements meets high requirements. 2 tbl, 3 ex
NOVELTY - The method involves initially pre-drying biomass and feeding the pre-dried biomass into a fluidized bed gasifier. Raw gas is transmitted to a reconducting cyclone (10) and supplied from the cyclone to a raw gas cooler (11). Dust resulting in a warm gas filter (12) is led back into an entry system of the biomass, where the filter is connected downstream to the cooler. Sorbent is supplied for deposition of noxious gases such as hydrogen sulfide and hydrochloric acid. Iron ore, calcium carbonate, calcium oxide, calcium hydroxide and dolomite are used as additives.    USE - Method for gasification of biomass in a fluidized bed.    ADVANTAGE - The dust resulting in the warm gas filter is returned into the entry system of the biomass, where the filter is connected downstream to the cooler, thus enhancing yield of gasification of biomass in the fluidized bed and reducing cost of a system for gasification of biomass in the fluidized bed.    DESCRIPTION OF DRAWING(S) - The drawing shows a connection diagram of a system for gasification of biomass in a fluidized bed.    Star-wheel feeder (3)    Entry lock (5)    Reconducting cyclone (10)    Raw gas cooler (11)    Warm gas filter (12)
NOVELTY - Obtaining hydrogen by electrolysis method involves using unprepared tap water as electrolyte and inert alloy D16 (duralumin) as cathode with voltage of 12-110 V in electrolytic cell and current strength of 4 mA/sm2, activating the alloy for 20 minutes and then disconnecting current for 5-10 minutes, where after activation each subsequent cycle takes 1-10 minutes.    USE - For obtaining hydrogen (claimed).    ADVANTAGE - The method utilizes unprepared tap water as electrolyte thus saves power consumption and provides improvement in ecology.
NOVELTY - Bamboo pellet fuel is manufactured by mixing and crushing 100 wt.% of greater than or equal to 2 year old green bamboo without branches and leaves, and 25-400 wt.% withered bamboo with greater than or equal to 55% moisture content to obtain bamboo mixed powder base, drying with drying machine, and granulating with granulator to obtain pellets.    USE - Manufacturing method of bamboo pellet fuel (claimed).    ADVANTAGE - Fermentation and production of mold are suppressed, drying time is shortened, and drying and manufacturing costs are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of the manufacturing method of bamboo pellet fuel. (Drawing includes non-English language text).    Bamboo thicket (1)    Green bamboo (2)    Cargo field collection (3)    Withered bamboo (4)    Wood (5)
NOVELTY - A manufacturing method of antioxidant involves inoculating and fermenting lactic acid bacteria in raw material which consists of sesamin, and heating. The organic acid is added to raw material which consists of sesamin.    USE - A manufacturing method of antioxidant.    ADVANTAGE - The method obtains water-soluble antioxidants easily. The antioxidant has good absorptivity into body, and improved functionality such as antioxidant activity, immunostimulatory action, and blood pressure elevation suppression effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of conversion ratio of sesamol with respect to organic acids. (Drawing includes non-English language text).
NOVELTY - A catalyst comprises granular active carbon, carbon powder, and/or Bincho charcoal placed in concentrated sulfuric acid or fuming sulfuric acid to sulfonate at 160-200 degrees C.    USE - Catalyst for decomposing and carbonizing organic substances such as foodstuff residue (claimed) used in bioreactor for activated carbon, solid fuel, or underground microbe reproduction.    ADVANTAGE - Processing time is shortened, and apparatus and operation costs are low.
NOVELTY - A biogas fermentation reactor comprises shell comprising liquid storage chamber for receiving fermented biogas liquid, at least one inlet and at least one outlet which are installed on shell, and heating coil pipe installed outside shell in the way of contacting the shell. The cross section of heating coil pipe a semi-circle annular structure. The linear part of annular structure contacts the outer wall of the shell. The reactor further comprises a residue discharging device connected with lowest part of lower end cover.    USE - Biogas fermentation reactor.    ADVANTAGE - The outer coil pipe is used for heating, thus avoiding corrosion of inner coil pipe, and ensuring fermentation temperature in winter. The reactor heats and ferments biogas liquid by straws of crops such as wheat, rice, corn and soybean, and is suitable for industrial mass production.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram showing a biogas fermentation reactor.
NOVELTY - The unit has a pre-heating tank and a catalytic cracking tower arranged on a top part of a heat supply device i.e. fuel coal furnace. The heat supply device is connected with the pre-heating tank through a heat exchange tube. A condensing device is provided with a first stage condensing tank and a second stage condensing tank, where the condensing device is formed as a two-stage condensing structure.    USE - High solidifying point biological diesel catalytic cracking unit.    ADVANTAGE - The unit can increase heat efficiency of a catalytic cracking system and conversion rate of biological diesel. The unit has simple structure, better reliability and high working efficiency, and is produced and installed at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high solidifying point biological diesel catalytic cracking unit.
NOVELTY - The furnace has a vacuum pump (62) and a kettle inlet pipe (63) welded with a methane kettle (64). A falling pipe (71) is welded at a lower end of a steam bag (74) that is welded with a steam inlet pipe (72) and a water gauge (75). A high pressure pump (70) is welded with an air intake duct (69). A vacuum pump (77) is welded with another air intake duct (78). A lower end of a pipe is inserted into a feeding chamber (10). A sealing system is used to prevent entering of air. A gasification medium of the system is oxygen, water steam and hydrogen.    USE - Airflow gasification furnace for generating pure combustible gas i.e. methane, by utilizing biomass powder.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an airflow gasification furnace.    Feeding chamber (10)    Vacuum pump (62)    Kettle inlet pipe (63)    Methane kettle (64)    Air intake ducts (69, 78)    High pressure pump (70)    Falling pipe (71)    Steam inlet pipe (72)    Steam bag (74)    Water gauge (75)    Vacuum pump (77)
NOVELTY - The preparation method involves mixing biomass particles with hot vacuum gas oil that is less than 500 degrees Celsius. The hot vacuum gas oil is used as heat source for pyrolyzing the biomass particles of 2 millimeters or less in size. A hydrocarbon oil pyrolysis product is then recovered after pyrolyzing the biomass particles.    USE - Preparation method for hydrocarbon.    ADVANTAGE - Enables to pyrolytically process biomass material into useful byproducts through the use of refinery feedstock as heat transfer medium and/or source of hydrogen for hydrodeoxygenation. Pyrolyzing biomass with higher conversion rates at lower temperatures that can be scaled up and is cost effective to perform. Improves heat transfer to biomass particle resulting in improved product yield, and the resulting bio-oil is of higher quality due to thermochemical interaction with the hot petroleum feedstock. Reduces reaction temperature from common fast pyrolysis temperatures of 500 degrees Celsius so to improve efficiencies and cost in preparing hydrocarbon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pyrolyzing method for biomass.
NOVELTY - The device (100) has electrolyte solution layers (5,7) which are in contact with photocatalyst electrode (4) and counter electrode (8). Gas extraction opening (14,15) removes oxygen gas or hydrogen gas generated in inside of electrolyte solution layers. The photocatalyst electrode and counter electrode are arranged so that surfaces of photocatalyst layer and counter electrode face each other. A separator (6) suppresses permeation of electrolyte in electrolyte solution layer, and permeation of hydrogen gas and oxygen gas in electrolyte solution layer.    USE - Hydrogen generation device used as hydrogen supply source to fuel cell.    ADVANTAGE - The efficiency of hydrogen generation can be improved. The gas generated on photocatalyst layer surface and gas generated on counter-electrode surface can be separated easily. The light utilization efficiency of counter electrode can be improved. The quantum efficiency of hydrogen generation reaction can be improved by irradiation of light.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of hydrogen generation device. (Drawing includes non-English language text)    Photocatalyst electrode (4)    Electrolyte solution layers (5,7)    Separator (6)    Counter electrode (8)    Gas extraction opening (14,15)    Hydrogen generation device (100)
NOVELTY - Alkali or alkaline earth metal salts of pitavastatin (A) are new, where the alkali or earth metal comprise one or more of magnesium, zinc, potassium, strontium and barium.    USE - (A) are useful for treating hypercholesterolemia and mixed dyslipidemia. No biological data given.    ADVANTAGE - (A) can be prepared with high yield and high purity in an economical, environmentally friendly and industrial manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a pharmaceutical composition comprising pitavastatin magnesium and one or more carriers or excipients;    (2) the preparations of (A);    (3) (4R,6S)-(E)-6-(2-(2-cyclopropyl-4-(4-flourophenyl)quinoline-3-yl)-vinyl-2,2-dimethyl-1,3-dioxane-4-yl)acetic acid tertiary butyl ester (II) in crystalline form; and    (4) preparation of (II), comprising reacting phosphonium bromide compound (IV) with an aldehyde compound (III) in the presence of an alkali or alkaline earth metal base in one or more suitable polar aprotic solvents to provide (II), treating (II) with one or more suitable polar solvents to form a reaction mixture, heating the reaction mixture at an elevated temperature, cooling the reaction mixture to ambient temperature, and isolating (II) in crystalline form.
NOVELTY - A catalyst contains crystalline aluminosilicate containing large-pore zeolite with 12-membered ring structure. The catalyst has 10 volume% distillation temperature of 140 degrees C or more and 90 volume% distillation temperature of 380 degrees C or less. 6-8C Monocyclic aromatic hydrocarbon and 3-4C aliphatic hydrocarbon are manufactured from raw material oil using the catalyst.    USE - Catalyst is used for manufacturing aliphatic hydrocarbon and aromatic hydrocarbon (claimed) for liquefied petroleum gas.    ADVANTAGE - The catalyst enables formation of hydrocarbon with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrocarbon, which involves contacting raw material oil and the catalyst.
NOVELTY - The fuel cell (11) has an electrolytic membrane (101) that is pinchingly supported between a fuel electrode (102) and an oxidizing agent electrode. The electrolytic membrane is formed with an electrolyte to generate water in the fuel electrode at the time of an electric power generation. The fuel is discharged to the fuel electrode by a fuel generation portion (104). The fuel generation portion and the fuel electrode are covered and sealed together with the electrolytic membrane by a sealing element (105). The fuel generation portion is made of iron.    USE - Fuel cell such as solid oxide fuel cell (SOFC).    ADVANTAGE - Since the fuel generation portion and the fuel electrode are covered and sealed together with the electrolytic membrane by the sealing element, the leakage of the fuel to the exterior of the fuel cell can be prevented reliably, without performing highly accurate position alignment between each components of fuel cell. The fuel cell can be manufactured easily by simple process at reduced cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the fuel cell.    Fuel cell (1)    Electrolytic membrane (101)    Fuel electrode (102)    Fuel generation portion (104)    Sealing element (105)
NOVELTY - A downdraft gasifier comprises an air intake that is provided toward top of body to allow air into body. A fuel feed inlet is provided toward top of body to allow the controlled introduction of fuel gasifier. A grate is located inside body and below the fuel feed inlet to support a bed of the fuel. An in-bed air distribution system has pipes with nozzles located inside body and above grate to inject air within the bed. A rotating paddle is located inside the body and above grate to stir the bed. A gas exit port is located below the grate. An ash removal port is provided toward bottom of body.    USE - Downdraft gasifier.    ADVANTAGE - Stability of downdraft gasifier is dramatically improved and gasifier systems have substantially higher energy output rates. Maintaining an even bed height across the entire cross sections promotes even air distribution, thus minimizing the probability of instabilities. Quality of the environment is enhanced by reducing the quantity of material going to landfills or that might otherwise simply be burned, green house gas emission is reduced by more efficiently using materials to produce syngas, and energy resources are conserved by providing a useful product from materials that might otherwise be simply burned or tossed into a landfill.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the grate for gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the components and construction of an actuated sliding grate arrangement.    Upper canopy sections (12)    Sliding paddle (13)    Lower flat plate sections (14)    Outer spacer (15)    Perpendicular slot (18)
NOVELTY - Treating seeds containing toxic components such as curcin, abrin, crotin and/or phorbol esters, preferably Jatropha seeds having a rate of acidity of less than or equal to 3 mg potassium hydroxide/g, comprises: (i) packaging the seeds; and (ii) contacting the seeds packed with light anhydrous alcohol and an alkaline catalyst under conditions of temperature and duration sufficient for extraction and transesterification of vegetable oil for extracting a mixture comprising esters of fatty acids and glycerol, and cake, where the step (i) comprises flattening and drying seeds.    USE - The mixture of esters of fatty acids and glycerol is useful as biofuel. The cake is useful in animal feed (all claimed).    ADVANTAGE - The process: is simple and cost effective for treating seeds; avoids stages of crushing, refining, purification and production of by-products; produces a fraction rich in fatty acid esters, which are non-toxic, and can be used without risk, particularly for manufacturing biodiesel. The process leads to the production of detoxified seeds, which can be handled safely by humans and can be used in feed without risk of poisoning in animals.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) mixture of fatty acid methyl ester obtained by the process, comprising 15-40 wt% of oleic acid methyl esters; (2) and detoxified Jatropha cake obtained by the process, having a rate of curcin detoxification of at least 90%, preferably at least 95%, in activity when the rate is measured by a quantitative test and phorbol ester content of less than or equal to 0.11 mg/g.
NOVELTY - The system has a modifier (3) for performing steam reforming of pyrolysis gas, and a thermal decomposition device (4) for thermally decomposing a woody biomass raw material. A heat carrier path is extended along an up-down direction. An annular distribution supply path is provided so that the circumference of the heat carrier path is surrounded, where the annular distribution supply path is connected to a hot-air blowing outlet. A compressed air blowing inlet is connected to the distribution supply path.    USE - System for gasification of a woody biomass i.e. coppiced timber, to produce heat or electrical energy.    ADVANTAGE - The design of the system maintains the heating efficiency of the heat carrier in the preheater, while stabilizing the quality of generated gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification method of the woody biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification system.'(Drawing includes non-English language text)'    Preheater (2)    Modifier (3)    Thermal decomposition device (4)    Separator (5)    Transfer apparatus (6)
NOVELTY - The system has a modifier (3) performing steam reforming of pyrolysis gas. A thermal decomposition device (4) thermally decomposes a woody biomass raw material. A hot blast stove (1) burns a char and generates hot air. A preheater (2) provides hot air supplied from the stove in mixture supplied from a transfer apparatus (6) in a deposition state and supplied into the stove in a passage process. A heat carrier is heated by direct contact with the mixture. The char supplied from the preheater is burned and the hot air generated by combustion is supplied to the preheater in the stove.    USE - Gasification system for gasifying woody biomass e.g. coppiced timber or pruned branch.    ADVANTAGE - The hot air generated with the hot blast stove is supplied to the preheater in counter current through the heat carrier supply path from the preheater to the hot blast stove with respect to the heat carrier, so that the heating efficiency of the heat carrier is maintainable and the quality of generated gas coming to be stabilized is provided easily. The time-dependent decline in the heating efficiency of the heat carrier is prevented, and the situation in hydrogen concentration of generated gas falls is prevented. The storage of ashes in a path inside of the modifier and between the modifier and the thermal decomposition device is prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasification woody biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification system.'(Drawing includes non-English language text)'    Hot blast stove (1)    Preheater (2)    Modifier (3)    Thermal decomposition device (4)    Transfer apparatus (6)
NOVELTY - Method for processing biomass, involves hydrolyzing the biomass filled in reactor using water-flowing pressurized hot water, where the biomass is hierarchically filled in an order starting from biomass with slow hydrolysis rate by applying from a pressurized hot water inflow port to the decomposition-product outflow port of a reactor.    USE - The method is useful for processing biomass for producing oligosaccharides including xylooligosaccharides and cellooligosaccharides, and polysaccharides used for bioethanol production.    ADVANTAGE - The polysaccharides and oligosaccharides can be recovered in large quantities. The method is environmentally-friendly as the agricultural and building waste including residue of foodstuff, wood chips and waste building materials are used as biomass.
NOVELTY - The method involves immersing a porous reinforcing material (11) e.g. polyamide, in a dispersion liquid (L1) in which radical scavenging particles acquire a hydroxy radical generated from hydrogen peroxide, and making another porous reinforcing material (12) after impregnating a polymer electrolyte. The dispersion liquid is penetrated upon inside of the porous reinforcing material. The radical scavenging particles are adhered to a fiber surface inside the porous reinforcing material. The radical scavenging particles are uniformly distributed by the porous reinforcing material.    USE - Method for manufacturing a polymer electrolyte membrane for a polymer electrolyte fuel cell that is utilized for a motor vehicle and an electric vehicle i.e. ecological car.    ADVANTAGE - The method manufactures a polymer electrolyte membrane without providing damage to the polymer electrolyte membrane containing the porous reinforcing material at time of use, and prevents damage to split of the porous reinforcing material at time of manufacture, while acquiring radical scavenging effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation illustrating a method for manufacturing a polymer electrolyte membrane.'(Drawing includes non-English language text)'    Dispersion liquid (L1)    Washing liquid (L2)    Polymer electrolyte membrane (10)    Porous reinforcing materials (11, 12)
NOVELTY - A biomass processing apparatus comprises pressurized hot water reactor (5) which hydrolyzes biomass by pressurized hot water containing acidic water.    USE - Biomass processing apparatus.    ADVANTAGE - The biomass processing apparatus more efficiently hydrolyzes biomass feedstock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass processing method involving hydrolyzing biomass by pressurized hot water added with acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass processing apparatus. (Drawing includes non-English language text).    First pump (1)    Acidic water adjustment tank (2)    Second pump (3)    Preheater (4)    Pressurized hot water reactor (5)
NOVELTY - The membrane (12) has a set of projections (22) formed at surfaces (18, 20) of the membrane, where the membrane is coated with catalyst layers (14, 16) that are provided for catalyzing electrochemical reaction in a fuel cell. The projections comprise identical form and dimensions in a spatial direction. The projections are formed by the removal of material from a base body of the membrane through a laser. Recesses (24) are formed between the projections, and the surfaces of the membrane are turned towards the respective catalyst layers, where the projections have the form of fins.    USE - Polymer electrolyte membrane for a fuel cell utilized for generating electric current. Can also be used for a catalyst coated membrane.    ADVANTAGE - The projections are formed at the surfaces of the membrane and comprise identical form and dimensions in the spatial direction, where the membrane is coated with catalyst layers that are provided for catalyzing electrochemical reaction in the fuel cell, thus ensuring improved contact between the membrane and the catalyst layers, and hence increasing the efficiency of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a membrane for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a membrane arrangement.    Polymer electrolyte membrane (12)    Catalyst layers (14, 16)    Surfaces of membrane (18, 20)    Projections (22)    Recesses (24)
NOVELTY - A composite gas-adsorption material contains (in parts mass) activated carbon (100), aromatic amino sulfonic acid (2-12) and organic acid (3-20). The activated carbon has Brunauer-Emmett-Teller specific surface area of 700-1300 m2/g. The organic acid is solid 2-6C organic acid which is soluble in water at 25 degrees C.    USE - Composite gas-adsorption material is used for composition for adsorption filter (both claimed). Uses include but are not limited to air cleaner filter, ceiling material, industrial filter and cabin filter for adsorption of acetaldehyde, butane and trimethylamine in interior of residence and motor vehicle.    ADVANTAGE - The composite material has excellent gas adsorption characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of composite gas-adsorption material; and    (2) composition, which contains composite gas-adsorption material and other adsorbent.
NOVELTY - The apparatus has drive control unit (61a) that controls the driving time over predetermined temperature. An output measurement unit (61b) measures output of contact burning gas sensor (15) when temperature of sensitive element is in high temperature. A low-temperature drive time is selected based on output of contact burning gas sensors. The inclination of output of contact burning gas sensor is computed with respect to low-temperature drive time. A correction information storage unit stores the correction information.    USE - Apparatus for detecting gas such as methane, hydrogen and carbon monoxide.    ADVANTAGE - Since the inclination of output of contact burning gas sensor is computed with respect to low-temperature drive time, the deterioration degree can be correctly grasped irrespective of density of detection target gas. Since the output of contact burning gas sensor is corrected based on the correction information and inclination of output with respect to computed low-temperature drive time, gas detection can be performed accurately.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas detection apparatus. (Drawing includes non-English language text)    Contact burning gas sensor (15)    Drive control unit (61a)    Output measurement unit (61b)    Inclination calculation unit (61c)    Output correction unit (61d)
NOVELTY - The device has a dry material loading system connected with a thermal cracking reaction system that is connected with a condensation heat exchange system. A drier (1) is connected with a cyclone separator (2) that is connected with a hopper lifter (3). The hopper lifter is connected with a bin (4). A fluidized bed (25) is connected with the cyclone separator that is connected with a chute board reactor (6). The chute board reactor is connected with a collection chamber (8) that is connected with a spiral feeder (9). Another cyclone separator (7) is connected with a coal powder furnace (23).    USE - Chute board type device for use during biological fuel oil preparing process.    ADVANTAGE - The device is compact in structure, low in energy consumption and cost and high in energy utilization rate and final biological oil conversion rate. The device implements large-scale production, and has high economical and social values.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a chute board type device.    Drier (1)    Cyclone separator (2, 7)    Hopper lifter (3)    Bin (4)    Chute board reactor (6)    Collection chamber (8)    Spiral feeder (9)    Coal powder furnace (23)    Fluidized bed (25)
NOVELTY - Methane preparing system in a sunlight shed comprises a sunlight shed heating and insulation system and a methane preparing system in shed, where an underground methane fermenting pool or tank and a low-pressure floating housing-type methane storage tank are combined and integrally designed by the system and located in the sunlight shed.    USE - Used as a methane preparing system in a sunlight shed.    ADVANTAGE - The system: ensures methane item normally performing to produce gas in winter according to the wall insulation process and the underground anti-freezing process; and is stable, simple and economical.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of the methane preparing system.
NOVELTY - The device has a high temperature heater (7.3) whose outlet is interconnected respectively with an air inlet pipe of an expander of a high temperature expanding-compressing engine (6) and an air outlet pipe of a compressor of the high temperature expanding-compressing engine. The outlet of the high temperature heater is connected with a pipeline inlet of a solar high focusing high temperature heat collector (8) and an inlet of a disk or spiral heating pipe (7.2) that is arranged in a biomass high temperature heating furnace (7).    USE - Solar and biomass power generation refrigerating and heating device.    ADVANTAGE - The device has high efficiency, and reduces the discharge of carbon dioxide and saves the cost and consumption of electric power. The biomass high temperature heating furnace is utilized to effectively complement the heat to make the device to work continuously even in dark environment. The device has high energy conversion efficiency and wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solar and biomass power generation refrigerating and heating device.    High temperature expanding-compressing engine (6)    Biomass high temperature heating furnace (7)    Disk or spiral heating pipe (7.2)    High temperature heater (7.3)    Solar high focusing high temperature heat collector (8)
NOVELTY - The system has guide tubes (3-5) arranged in groups, where the guide tubes in each group are arranged in an offset manner. The guide tube located at a top is loaded with precompressed biomass under exclusion of air by a rotary valve or a sealing screw conveyor (11). Guide shafts (6, 7) in each group of guide tubes are connected such that temperature of fed biomass is increased in a path-dependent and stepwise manner when the biomass passes through the guide tubes and reaches a maximum value required for pyrolysis in the guide tube located at a bottom.    USE - Pyrolysis system for use as a cogeneration plant for biomass.    ADVANTAGE - The guide shafts in the groups of guide tubes are connected such that the temperature of the fed biomass is increased in a path-dependent and stepwise manner when the biomass passes through the guide tubes and reaches the maximum value required for pyrolysis in the guide tube located at the bottom, thus guaranteeing complete utilization of heat and ensuring that desired pyrolysis temperature is achieved in the guide tube located at the bottom before reaching outlets.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side, partial sectional view of a heating chamber of a pyrolysis system.    Heating chamber (1)    Housing (2)    Guide tubes (3-5)    Guide shafts (6, 7)    Sealing screw conveyor (11)
NOVELTY - The device has two mutually concentric and interconnected tanks stored under anaerobic conditions and maintained in mesophilic temperature. A waste water collecting stand is provided in two upper outer spaces (1, 2). A slit (3) is formed into a lower outer space (4) to pass waste water. The lower outer space is linked with a heated tank (5). A biomass substrate (6) is provided in the heated tank and penetrated into a perforated container (7) that is fixed on a top part of gas bells (8). The gas bells pass biogas into a common enclosure (10) through a hose (9).    USE - Device for concurrently cleaning waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for concurrently cleaning waste water.    Upper outer spaces (1, 2)    Slit (3)    Lower outer space (4)    Heated tank (5)    Biomass substrate (6)    Perforated container (7)    Gas bells (8)    Hose (9)    Common enclosure (10)
NOVELTY - An ether-based fuel comprises dimethyl ether and methanol.    USE - Ether-based fuel is used for mixed fuel for gasoline engine of automobile (all claimed), other vehicles and power equipments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mixed fuel, which contains ether-based fuel and gasoline.
NOVELTY - An ether-based fuel comprises dimethyl ether, methanol and 2,6-di-tert-butyl-4-methyl phenol.    USE - Ether-based fuel is used for gasoline engine of automobile (both claimed), other vehicles and power equipment.
NOVELTY - An ether-based fuel contains dimethyl ether, methanol and water.    USE - Ether-based fuel is used for carburetor used in gasoline engine of automobile (all claimed), other vehicles and power equipment.
NOVELTY - An ether-based fuel contains dimethyl ether, methanol and castor oil.    USE - Ether-based fuel is used for blended fuel for gasoline engine of automobile (both claimed), other vehicles and power equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for blended fuel, which contains ether-based fuel and gasoline.
NOVELTY - An ether-based fuel contains dimethyl ether, methanol and succinimide.    USE - Ether-based fuel is used for gasoline engine of automobiles (both claimed) and power equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for blended fuel, which contains ether-based fuel and gasoline.
NOVELTY - An ether-based fuel contains dimethyl ether and ethanol.    USE - Ether-based fuel is used for gasoline engine of automobiles (both claimed) and power equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for blended fuel, which contains ether-based fuel and other fuels chosen from gasoline and 180-type megilp oil.
NOVELTY - An ether-based fuel contains dimethyl ether, ethanol and succinimide.    USE - Ether-based fuel is used for gasoline engine of automobiles (both claimed) and power equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for blended fuel, which contains ether-based fuel and other fuels chosen from gasoline and 180-type meglip.
NOVELTY - An ether-based fuel contains dimethyl ether, ethanol and t-butyl alcohol.    USE - Ether-based fuel is used for gasoline engine of automobiles (both claimed) and power equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for blended fuel, which contains ether-based fuel and other fuels chosen from gasoline and 180-type meglip.
NOVELTY - An ether-based fuel contains dimethyl ether, ethanol and 2,6-di-tert-butyl-4-methylphenol.    USE - Ether-based fuel is used for automobile, other vehicles and power equipment.
NOVELTY - A mesh-shaped insulator (9) having thickness below 0.5 mm is provided on both surfaces of positive electrode plate (7) for maintaining gap between negative electrode plate (8) and positive electrode plate as 0.5 mm or less uniformly. The sum total area of hole provided in a cathode board is set to 5-6 mm, so that sum total of electrode plate of stainless steel punching metal is set to 30-40% of opening area with respect to area of electrode plate used as anode board.    USE - Electrode structure for generating hydrogen and oxygen in bathtub. Can also be used in fuel cell manufacture.    ADVANTAGE - The hydrogenous water bath can be provided by putting electrode structure in the bath tub and efficiently generating and injecting hydrogen and oxygen in bath tub. The water consumption can be reduced and cost of the electrode structure can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the electrode structure. (Drawing includes non-English language text)    Positive electrode plate (7)    Negative electrode plate (8)    Mesh shaped insulator (9)    Filter guard (17)    Filter (18)
NOVELTY - The generator has a sequence comprising of first positively or negatively charged electrodes. The isolated element (21) is followed in the sequence by an electrode of opposite polarity to a first electrode. The isolated element is located between each positively and negatively chargeable electrode of the sequence. The sequence ends with an electrode of opposite polarity to that of the first electrode of the sequence.    USE - Hydrogen generator for use with internal combustion engine of vehicle e.g. car.    ADVANTAGE - The combustion reduces the emission of carbon monoxide, unburned hydrocarbons, nitrogen oxides and sulfur oxides. The improved combustion efficiency results in improved fuel consumption such that energy used per unit of fuel is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of generator.    Electrodes (15)    Anode (17)    Cathode (19)    Isolated element (21)    Non-conductive shaft (25)
NOVELTY - The generator (110) has a cylindrical metal enclosure which is used to operate as an electrode when coupled to respective terminal of a power source. The metal includes stainless steel and titanium. Fuel cell unit is arranged within the enclosure and include electrode coupled to positive terminal of the power source e.g. battery (160). The conductive tubular cells with microscopic indentations on the surfaces are arranged in a longitudinal direction of the enclosure. PTFE base insulator is arranged within enclosure to stabilize the tubular cells within enclosure.    USE - Hydrogen fuel generator for motor vehicle engine such as combustion engine, petrol engine, diesel engine, Liquefied petroleum gas (LPG) engine, Bio Diesel engine, gas turbine engine, jet engine and rocket engine.    ADVANTAGE - Since hydrogen gas is burned at cooler temperature than diesel, the viscosity of the engine's oil may not break down as quickly, reduction of the overall maintenance costs of the engine is ensured. Since the noxious and toxic engine emissions are reduced, reduction of the greenhouse gas emissions is ensured by providing cleaner air. Improvement of the fuel burn system can be ensured with increase in the fuel generation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fuel system with hydrogen fuel generator and injection controller.    Hydrogen fuel generator (110)    Safety valve (111)    Injection controller (122)    Injector (124)    Battery (160)
NOVELTY - Use of a biomass excessively arising in an aerobic biological purification of water, as a raw material for the fermentation in biogas plants, is claimed.    USE - The biomass is useful as a raw material for the fermentation in biogas plants.    ADVANTAGE - The biomass reduces the environmental pollution.
NOVELTY - Granules comprise residual water (less than 8 mass%), chlorine (600 ppm), sulfur (1500 ppm) and fluorine (100 ppm), where the granules have density of greater than 400 kg/m3, heat capacity of greater than 10 GJ/ton and diameter of greater than 10 mm.    USE - Granules for energetic recycling of mixture of biomass source e.g. biomass waste such as intensive livestock slurry or manure, grape wine, grape juicer vegetable oil composting waste, forestry waste, dry residue of biogas, dry residues to produce bio-methanol, and/or sewage sludge, at an end of a recycling chain (all claimed).    ADVANTAGE - The granules ensure energetic recycling of mixture of biomass source in an environment friendly manner, and reduce emission of greenhouse gases e.g. methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing granules.
NOVELTY - The apparatus (100) has an electrode formation part (120) intermittently forming multiple sets of mutually corresponding anode (2a) and cathode (2c) by a fixed space with respect to conveyed electrolytic membranes (1a, 1c). A distance shortening processing part shortens distance of adjacent anode and cathode by bending the membranes between the anode and cathode, and fusing the membranes. A distance extension processing part extends the distance of the adjacent anode and cathode by extending along the longitudinal direction and heating the membranes between the adjacent anode and cathode.    USE - Membrane electrode assembly i.e. electric power generation body manufacturing apparatus for an electric power generation module in a fuel cell i.e. polymer electrolyte fuel cell that receives and generates supply of reactive gas e.g. hydrogen and oxygen.    ADVANTAGE - The distance extension processing part extends the distance of the adjacent anode and cathode by extending along the longitudinal direction and heating the membranes between the adjacent anode and cathode, even if multiple membrane electrode assemblies are continuously manufactured in an efficient manner based on a flow process, thus reducing a formation position of the anode and cathode, which are mutually opposed through the electrolytic membranes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a membrane electrode assembly manufacturing apparatus.'(Drawing includes non-English language text)'    Electrolytic membranes (1a, 1c)    Anode (2a)    Cathode (2c)    Membrane electrode assembly manufacturing apparatus (100)    Electrode formation part (120)
NOVELTY - Treating residential wastewater involves performing flocculation and sedimentation of wastewater for removing fat, oils, surfactants and organic matter.    USE - Method for treating residential wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for equipment for treating residential wastewater, which comprises a digester, a camera and a biogas outlet valve.
NOVELTY - A compound microbial fertilizer comprises 25-30% organic compound, 6-8% total primary nutrients (NPK), and 0.2-10 hundred million/gram effective viable bacteria.    USE - A compound microbial fertilizer.    ADVANTAGE - The product has a high-efficiency effect to the changed water quality.
NOVELTY - The system has a sewage water pipe (3) that is connected with toilet (1) through bent pipe (2). The tail end of the sewage water pipe is connected with methane tank (12). The methane tank is connected with biogas liquid storage pool (10) through biogas discharging pipe (11). Another sewage water pipe (4) whose tail end is connected with sewer (13). The one ends of branch pipelines of the sewage water pipe is connected with a sink of bathroom (8) and waste water pool (7) which is connected with primary water collecting pool (5) through pipeline.    USE - Recycling system for domestic sewage.    ADVANTAGE - The excrement waste water in the toilet and other waste water can be fermented to recycle the methane, so that biogas liquid can be obtained to fertilize the plants and trees. The re-usage of methane can be achieved without pollution. The waste water can be reused repeatedly, by collecting the waste water in the primary water collecting pool. The water in the bathroom and wastewater pool can be discharged to the sewer through sewage pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the recycling system.    Toilet (1)    Bent pipe (2)    Sewage water pipes (3,4)    Primary water collecting pool (5)    Waste water pool (7)    Bathroom (8)    Biogas liquid storage pool (10)    Biogas discharging pipe (11)    Methane tank (12)    Sewer (13)
NOVELTY - An organic alkaline potash fertilizer comprises straw (5), gramineous pasture (7) and lu peng grass (8) which are carbonized as plant ash coke button with pine saw powder (4) and cotton seeds (6) in carbide furnace. The components for processing the fertilizer includes carbide furnace, crushing blender, particle extruder, pine saw powder, straw, cotton seeds, gramineous pasture grain, lu peng grass (annual herb wild plants), anaerobic jar, waste sludge and biogas liquid. The anaerobic jar is employed to process fermentation compost harmless process for straw and livestock and poultry manure.    USE - Organic alkaline potash fertilizer for adjusting soil structure.    ADVANTAGE - The alkaline potash fertilizer not only can increase organic matter potassium of soil, but also can adjust acidity of soil and control the soil to develop for acidity.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating production of organic alkaline potash fertilizer.    Saw powder (4)    Straw (5)    Cotton seeds (6)    Gramineous pasture (7)    Lu peng grass (8)
NOVELTY - Fresh chicken manure is used for producing solid state organic fertilizer by collecting fresh chicken manure generated in the chicken farm, adding water, drying the mixture, and transmitting dried solid residue to a fermenting pond; layering the solid residue, dispersing humic acid or plant straw powder and superphosphate to form fermenting raw material, and spraying aerobic fermentation composite fungicide; and overturning and mixing the material, fermenting, and filtering.    USE - Method of using fresh chicken manure for producing solid state organic fertilizer (claimed).    ADVANTAGE - The method has improved quick-acting performance, can decompose nitrite compound in the soil to activate the soil, improves hardening of the soil and cultivation environment, can restrain soil virus and soil infectious disease, and reduces environment pollution.    DETAILED DESCRIPTION - Fresh chicken manure is used for producing solid state organic fertilizer by:    (A) collecting fresh chicken manure generated in the chicken farm, adding water (20-30 wt.% of manure quantity), drying the mixture to control water content to 50-55%, and transmitting dried solid residue to a fermenting pond;    (B) layering the solid residue at a thickness of 90-115 cm, dispersing (wt.%) humic acid or plant straw powder (20-30) and superphosphate (5-10) to form fermenting raw material, and spraying aerobic fermentation composite fungicide (2-4); and    (C) overturning and mixing the material, fermenting at 0-40 degrees C for 6-10 days, and filtering using 20-mesh sieve.
NOVELTY - A biological fertilizer comprises (pts.wt.) dried straw (35-65), liquid/semiliquid waste organic matter (35-65), biological fungus or bacterium (0-50), medium trace element fertilizer (0-10), and modified additive (0-25).    USE - Biological fertilizer.    ADVANTAGE - The fertilizer can be prepared with simple operation and turn waste into valuable material to realize regenerative utilization of resource, thus promoting development of green organic agriculture and ensuring safety of agricultural product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biological fertilizer using waste organic matter, comprising:(A) grinding dried straw containing less than 5% water to less than 18 meshes to obtain straw powder; (B) adding the straw powder into double-axle stirrer, mixing the straw powder with cassava slag or filter mud or yeast liquid at ratio of 1:1, adding 0.2-0.4% straw rotten agent and 0.2-0.5% carbamide, and uniformly stirring to obtain fermentation material which contains 25-30% water; (C) stacking the fermentation material at height of 2-3 m, fermenting for 10-15 days, turning the stack when the temperature in the stack is higher than 65 degrees C, and turning for 2-4 times during stacking and fermenting; and (D) stirring and uniformly mixing the fermented material with nitrogen, phosphorus and potassium inorganic fertilizer and 5% Bacillus as biological bacterium, or pelletizing to obtain the biological fertilizer.
NOVELTY - A bio-energy compound organic fertilizer is prepared by fermenting materials including (pts. wt.): compound biological germ (1.5-4.5), farmyard manure (850-1000), microbial potash fertilizer (0.5-1.5), mineral substance (15-25) and regulator (0.05-0.15) at room temperature.    USE - Bio-energy compound organic fertilizer.    ADVANTAGE - The fertilizer utilizes beneficial biological fertilizer, chemical fertilizer and organic fertilizer, thus improving action and value of fertilizer, promoting operating factor of fertilizer, and recovering former ecological environment of soil; and has low carbon content and environment protection. It can be used for producing environment-friendly food; has quick acting effect, low cost, small risk and easy spreading.
NOVELTY - A biological organic compound fertilizer is prepared by selecting (pts. wt.): bead tree seed and leaf (30-35), edible fungi waste matrix (40-45) and livestock and poultry manure (15-2), soyabean meal (10-15) and humic acid (5-10); and physically stirring mixture and biologically fermenting.    USE - Biological organic compound fertilizer for resisting insect.    ADVANTAGE - The fertilizer has rational method, simple preparation and good quality of produced product.
NOVELTY - A fermenting bed has a 30-40 cm thick upper layer and a 40-50 cm thick lower layer. The upper layer comprises (wt.%) saw dust (30-70) and chaff (30-70). In each cubic meter of saw dust and chaff mixture, 5-10 kg rice bran and 50-200 g Bacillus subtilis environmentally friendly bactericide are added, mixed, and fermented. The water content is controlled at 40-50%. The lower layer comprises saw dust, chaff, rice bran, and Bacillus subtilis environmentally friendly bactericide. Each cubic meter of lower layer mixture comprises 50-200 g bactericide. The water content is 20-30%.    USE - A fermenting bed for microorganism padding (claimed).    ADVANTAGE - The fermenting bed uses the microorganism bactericide to degrade the pig manure to realize the energy conservation and emission reduction. The permeability management of the whole fermenting bed and padding water content regulation are realized by placing the padding with different water contents of the pit fermenting bed. The water content of the lower layer fermenting bed is reduced. The activity adjustment of the bactericide viable count in the padding is adjusted. The service life of the padding is prolonged. The better excrement and sewage treatment effect is obtained.
NOVELTY - Gene of wetland Alcanivorax borkumensis and Pseudomonas is new. The gene of wetland Alcanivorax borkumensis and Pseudomonas comprising one of the following nucleotides: (i) nucleotide sequence having fully defined 1496 base pairs (SEQ ID NO: 1), as given in the specification; or (ii) DNA sequence having 95% of homology with the nucleotide sequence of SEQ ID NO: 1 for coding the protein with the same biological function.    USE - The gene of wetland Alcanivorax borkumensis and Pseudomonas is useful for degrading the greasy dirt in the diesel oil sewage and the sludge (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a protein coded by the gene of wetland Alcanivorax borkumensis and Pseudomonas, comprising (i) fully defined 481 amino acids (SEQ ID NO: 2), as given in the specification, and (ii) amino acid sequence substituted, deleted or added by at least one of the amino acid residues to produce derived protein via the amino acid sequence of SEQ ID NO: 2, where the derived protein and the protein of SEQ ID NO: 2 have the same biological function; (2) a recombination vector, comprising the gene of wetland Alcanivorax borkumensis and Pseudomonas; (3) a host cell, comprising the recombination vector; and (4) cloning the gene of wetland Alcanivorax borkumensis and Pseudomonas.
NOVELTY - Wetland oil-degrading gene of Pseudomonas, comprising fully defined 1498 base pairs (SEQ ID NO: 1), as given in the specification, or a sequence having 95% homology with the limited nucleotide sequence of the SEQ ID NO: 1, and the biological functional protein encoded by the DNA sequence, is new.    USE - The gene is useful for degrading high concentrations of diesel wastewater (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a coding protein of the gene, comprising either fully defined 110 amino acid residues (SEQ ID NO: 2), as given in the specification, or a sequence obtained by substituting, deleting or adding at least one amino acid residue to SEQ ID NO: 2 and having same biological function as the protein of the SEQ ID NO: 2; (2) a recombinant vector, comprising the gene; (3) a host cell, comprising the recombinant vector; and (4) a method for cloning the wetland oil-degrading gene of Pseudomonas, comprising: (a) extracting 16S ribosomal DNA gene of the bacteria in the colony of Pseudomonas having wetland oil-degrading gene, which is screened from the oil polluted wetland; (b) polymerase chain reaction (PCR) amplification of the extracted 16S ribosomal DNA, where the amplifying condition are: pre-denaturation for 5 minutes at 95 degrees C, denaturation for 35 seconds at 98 degrees C, annealing for 35 seconds at 55 degrees C, extending for 1 minute 30 seconds at 72 degrees C, performing 35 cycles and extending for 8 minutes at 72 degrees C, and the amplifying primer is: P1 forward primer is 5'-agagtttgatcctggctcag-3'; and P2 reverse primer is 5'-ggttaccttgttacgactt-3'; (c) recovering the PCR products; (d) performing fragment TA cloning of the recovered products; and (e) plasmid extraction and obtaining the whole 16S ribosomal DNA sequence.
NOVELTY - Viable bacterial preparation comprises Bacillus circulans, Bacillus subtilis, Alcaligenes faecalis and Penicillium diversum.    USE - The viable bacterial preparation is useful in sewage treatment device, for producing organic waste water purifying agent, activated sludge enhancer for sanitary wastewater and deodorant for waste yards, public places, agricultural products, kitchen and toilet (all claimed), and for degrading organic wastes.    ADVANTAGE - The viable bacterial preparation: is utilized for degrading organic waste with high efficiency, economical and environmental friendly; and highly reduces the amount of the residual sludge generated in combination with active sludge under synergistic effect; and consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the viable bacterial preparation, comprising processing Bacillus circulans, Bacillus subtilis, Alcaligenes faecalis and Penicillium diversum liquid culture for amplification respectively, mixing according to the required ratio, carrying out solid state fermentation, drying, and crushing into powder to obtain the product.
NOVELTY - Use of Bacillus megaterium (CCTCC M2010272), is claimed for degrading aflatoxin B1 in peanut meal, where the B.megaterium is isolated from peanut kernel.    USE - The B.megaterium is useful for degrading aflatoxin B1 in peanut meal. Can also be used for treating wastewater.    ADVANTAGE - The B.megaterium consumes less amount of energy, causes no environmental pollution, and does not need sterilization process. The wastewater can be recycled easily.
NOVELTY - A solar auxiliary heating-type methane producing device has a biomass methane fermenting system having an anaerobic reaction chamber and an air storage tank on upper portion of the anaerobic reaction chamber, and auxiliary heating system having heat exchanger and heat collector. A feed port, a discharge port, a feed port valve and a discharge port valve are arranged in anaerobic reaction chamber. A feed pump is arranged between the feed port valve and the anaerobic reaction chamber. The heat exchanger is arranged at bottom of anaerobic reaction chamber.    USE - Solar auxiliary heating-type methane producing device.    ADVANTAGE - The solar auxiliary heating-type methane producing device has improved fermentation efficiency. The generation of short circuit is prevented.    DETAILED DESCRIPTION - A solar auxiliary heating-type methane producing device has a biomass methane fermenting system having an anaerobic reaction chamber and an air storage tank on upper portion of the anaerobic reaction chamber, and auxiliary heating system having heat exchanger and heat collector. An air outlet is arranged in air storage tank, and a breathing communicating hole is arranged at bottom of air storage tank. A feed port, a discharge port, a feed port valve and a discharge port valve are arranged in anaerobic reaction chamber. A feed pump is arranged between the feed port valve and the anaerobic reaction chamber. The heat exchanger is arranged at bottom of anaerobic reaction chamber. At least one baffle and at least one heat exchanger are arranged in middle of interior anaerobic reaction chamber, which is divided by heat exchanger into several isolation chambers.
NOVELTY - A multifunctional engineered bacteria strain for decomposing chlorpyrifos, Burkholderia vietnamiensis P418-M (CGMCC No.4166), having been preserved in China Microbial Culture Preservation Commission on 13/09/2010, is new.    USE - The multifunctional engineered bacteria strain is useful for decomposing chlorpyrifos not only to restore treatment of soil polluted by chlorpyrifos and prevent plant pathogenic bacteria, but also to function phosphorus and potassium decomposition and fixation of nitrogen. The plant pathogenic bacteria refers to Rhizoctonia solani, Fusarium oxysporum and Rhizoctonia cerealis. The multifunctional engineered bacteria strain is useful for decomposing chlorpyrifos to prepare bio-fertilizer (all claimed).    ADVANTAGE - The strain can promote growth of plant and root fixed breed ability, increase function on decomposing pesticide residue and achieve multifunction of the B. vietnamiensis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for re-constructing multifunctional engineered bacteria strain above.
NOVELTY - Device for processing swill into an organic fertilizer, comprises a waste processing chamber (4), a processing medium feeding port with an upper part sealed by a cover (18). The upper part of the waste processing chamber is provided with a processing gas inlet and a waste discharge port. A stirrer (5) driven by a driving device (6), which is arranged inside. A processing gas supply device (1) to supply the processing gas into the processing chamber is provided. The processing gas supply device is connected to the processing gas inlet of the waste processing chamber through a gas inlet pump.    USE - Used as a device for processing swill into organic fertilizer.    ADVANTAGE - The device uses processing gas, which is fermented by the organic substance to accelerate the fermentation of organic substances, e.g. food waste, and processes the food waste into gas, water and organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for processing swill into an organic fertilizer.    Processing gas supply device (1)    Waste processing chamber (4)    Stirrer (5)    Driving device (6)    Cover (18)
NOVELTY - Biodiesel preparing involves adding natural oil and short-chain fatty alcohol in a container in a mol ratio of 1:15-30. The natural oil is plant oil, animal fat or their mixtures. The plant oil is deoxidized and dehydrated to obtain natural oil. The short-chain fatty alcohol is methanol, ethyl alcohol or their mixtures. Modified calcium oxide as catalyst is added into the container for stirring to obtain a product. The calcium oxide is modified with halohydrocarbon. An organic solvent is also used in the preparation of biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel with improved yield, where the biodiesel has high catalyzing efficiency.    DETAILED DESCRIPTION - Biodiesel preparing involves adding natural oil and short-chain fatty alcohol in a container in a mol ratio of 1:15-30. The natural oil is plant oil, animal fat or their mixtures. The plant oil is deoxidized and dehydrated to obtain natural oil. The short-chain fatty alcohol is methanol, ethyl alcohol or their mixtures. Modified calcium oxide as catalyst is added into the container for stirring to obtain a product. The calcium oxide is modified with halohydrocarbon. An organic solvent is also used in the preparation of biodiesel. The organic solvent is methanol, ethyl alcohol, methylbenzene, n-hexane, cyclohexane, petroleum ether, petroleum solvent, ketone or ester solvent. The obtained product is stirred at 50-115 for 1-4 hours. The stirred product is cooled to room temperature. The cooled product is filtered by quantitative filter paper to remove solid catalyst to obtain filtrate. The filtrate is kept in a separating hopper for stewing to alcohol/oil two-phase layer to separate lower layer i.e. biodiesel.
NOVELTY - Method for pre-processing sweet sorghum stalk, involves cutting off and tearing the sweet sorghum stalk, performing effusion treatment for the obtained product, removing the residues from the treated product and dehydrating the obtained product to obtain sweet sorghum juice.    USE - The method is useful for pre-processing sweet sorghum stalk for producing fuel (claimed).    ADVANTAGE - The method improves the recovery rate of the sugar and thus improves productivity.
NOVELTY - Processing biodegradable organic waste gas by combining low temperature plasma and aerobic microorganism, comprises: passing the organic waste gas that is hard to be degraded through a low temperature plasma reactor; partially oxidizing the organic compound contained in the organic waste gas into easily degradable organic compound under the action of the low temperature plasma produced by the injection of low energy, and further converting the organic compounds into carbon dioxide, water, and other inorganic compounds under the action of aerobic microorganism.    USE - The method is useful for processing biodegradable organic waste gas.    ADVANTAGE - The process makes the total purifying efficiency of the organic compounds e.g. benzene, methylbenzene, dimethylbenzene and phenol in the waste gas reach over 90%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for processing biodegradable organic waste gas, comprising a low temperature plasma rector, a biological processing reactor, a gas collecting cover, a wind pipe and a chimney, where the organic gas that is hard to be degraded produced by the polluted source is collected by the gas collecting cover and transferred to the low temperature plasma rector via the wind pipe so that the organic gas is partially oxidized to easily degradable organic gas, and allowing the degradable organic gas to enter into the biological processing reactor and converting into carbon dioxide, water, and other inorganic compounds that are directly discharged into air via the chimney.
NOVELTY - Fermentation and material distribution device comprises a material mixer, a discharging extensible belt conveyor arranged below the material mixer outlet, a reversible material distribution belt conveyor, a material distribution traveling crane and a support. The material mixer and the discharging extensible belt conveyor are fixed on the support, and the reversible material distribution belt conveyor is arranged on the material distributing traveling crane and below the discharging extensible belt conveyor.    USE - The fermentation and material distribution device is useful for organic fertilizer.    ADVANTAGE - The device: greatly reduces more consumption of fuel oil by the forklift material distribution, and reduces the forklift tail gas pollution in the work environment; realizes the continuous and automatic material distribution, reduces the labor intensity, reduces the working staff in the organic fertilizer fermentation area, relives the harm of the fermentation tail gas to the body, and realizes the unmanned operation of the material distribution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the fermentation and material distribution device.
NOVELTY - The cutting apparatus has a direct current pulse signal generator, which outputs discontinuous saw-tooth wave current signal; a control valve installed on an electrolysis gas outlet pipe of the electrolysis water tank; and a micro-computer intelligent controller, which automatically controls gas generation amount and use amount of cutting oxygen according to the thickness of a steel plate and inputs corresponding control signal to the driving device of the stepping motor. The micro-computer intelligent controller is connected with the control valve through the stepping motor.    USE - Water energy steel structure cutting apparatus.    ADVANTAGE - Cutting fuel burns without discharging greenhouse gases. Cutting apparatus is environment-friendly, used safely and conveniently, and has good economical value, social benefit and easy application and popularization.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the circuit structure of the water energy steel structure cutting apparatus. (Drawing includes non-English language text).
NOVELTY - The method involves performing atmospheric on-line catalytic pyrolysis in a fluidized bed by taking agricultural wastes such as straw and corn cobs as biomass raw materials and taking a catalyst and quartz sand as bed materials. A pyrolysis product such as heavy oil, light oil and water phase component are respectively passed through three condensers with temperature range of 100-150 degrees centigrade, 45-55 degrees centigrade and 0-5 degrees centigrade. The on-line catalytic pyrolysis temperature in the fluidized bed is 400-650 degrees centigrade.    USE - Method for producing liquid fuel.    ADVANTAGE - The method enables avoiding the process of vaporizing, modifying and condensing the biological oil with high oxygen content in an inexpensive manner.    DETAILED DESCRIPTION - The catalyst is HZSM-5, MCM-41 and a fluid catalytic cracking (FCC) porous catalyst.
NOVELTY - A modified methanol comprises (pts.wt.) methanol (80-90) and methanol modification additive (3.16-15.38) including isopropanol (50-90), cyclohexylamine (30-20), aviation kerosene No. 1 (5-10), zinc peroxide (0.1-0.9), dimethyl carbonate (1-10), isooctyl nitrate (4-15), fatty acid methyl ester (3-10) and 2,6-di-tert-butyl-p-cresol (0.1-0.9).    USE - A modified methanol.    ADVANTAGE - The cyclohexylamine is compounded with the 2,6-di-tert-butyl- p-cresol so that the anti-corrosion swelling property of the modified methanol is stronger. The isopropanol is compounded with the fatty acid methyl ester so that the water resistance of the methanol is improved for more than 2 times. The methanol has no low-temperature layering and emulsification layering.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the modified methanol, comprising:    (A) producing an activating agent by mixing isopropanol with fatty acid methyl ester;    (B) producing a catalytic combustion additive by mixing aviation kerosene No.1 with zinc peroxide;    (C) producing a catalytic combustion agent by mixing the catalytic combustion additive with isooctyl nitrate;    (D) producing an anti-corrosion swelling agent by mixing cyclohexylamine with 2,6-di-tert-butyl-p-cresol;    (E) mixing the activating agent with the catalytic combustion agent and the anti-corrosion swelling agent to obtain a methanol modification additive; and    (F) mixing the methanol modification additive with methanol, sealing, stirring, and standing.
NOVELTY - Alcohol-based fuel additive comprises (in parts by wt) ferrocene (3-8), isobutanol (20-30), n-octyl alcohol (15-20), sodium peroxide (2-8), hexamethylenetetramine (25-35) and crude benzene (10-20).    USE - The alcohol-based fuel additive is useful for preparing alcohol-based blended fuel (claimed).    ADVANTAGE - The fuel additive is environmental-friendly, and the prepared blended fuel: has simple manufacturing method; low energy consumption, thus the concentration of generated sulfur dioxide and nitrogen oxides are low; high safety; high combustion value with the average flame temperature being 1100 degrees C, and the cost of alcohol-based blended fuel with the additive is 43.5% lower than the liquefied gas and 42% lower than diesel oil.
NOVELTY - Straw fuel formed by mixing straw powders with gangue powders and then extruding, is claimed.    USE - Used as a straw fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the straw fuel, comprising: naturally drying various straws, grinding them into a coarse straw powder of less than 15 meshes, passing the coarse straw powder to a fine grinder for grinding into a powder of greater than 35 meshes, then mixing the fine straw powder (95-98%) with gangue powder (2-5%), and introducing the mixture into a molding machine for extruded molding to obtain the product.
NOVELTY - Preparation of organic slow-release fertilizer, involves air-cooling raw materials chosen from (in parts weight) organic ingredients (25-50), enhancement ingredients (3-10), slow-release solid ingredients (5-10), liquid (3.5-9), trace elements (0.5-5), inorganic nutrients (55-75) and additive (2-7), and pelleting the mixture to obtain the product. The organic ingredients comprise fulvic acid (2-5), bacterium or animal wastes (15-35), treated sewage mud (5-10) and amino acid (5-10).    USE - The method is useful for preparing organic slow-release fertilizer for fruit trees.    ADVANTAGE - The fertilizer increases average yield of fruit trees by 10-20%.    DETAILED DESCRIPTION - Preparation of organic slow-release fertilizer, involves air-cooling raw materials chosen from (in parts weight) organic ingredients (25-50), enhancement ingredients (3-10), slow-release solid ingredients (5-10), liquid (3.5-9), trace elements (0.5-5), inorganic nutrients (55-75) and additive (2-7), and pelleting the mixture to obtain the product. The organic ingredients comprise fulvic acid (2-5), bacterium or animal wastes (15-35), treated sewage mud (5-10) and amino acid (5-10). The enhancement ingredients comprise agent as synergist (5-15). The slow-release solid ingredients comprise montmorillonite powder (2-5), kaolin (1-5), magnesium ammonium sulfate in solid form (1-4), nitrification inhibitor in solid form (0.02-0.1), urease inhibitor in liquid form (2-6) and polyaspartic acid in liquid form (2-6). The trace elements comprise zinc sulfate (0.1-1), manganese sulfate (0.1-1), sodium borate (0.1-1), copper sulfate (0.1-1) and ferrous sulfate (0.1-1). The inorganic nutrients comprise ammonium nitrate (2-7), ammonium sulfate (2-7), double superphosphate (5-25) and potassium sulfate (10-32). The additive comprises plaster of paris (1-7) and smectite (1-5).
NOVELTY - A high-energy liquefied mixed gas comprises (wt.%) liquefied gas (99-99.5) and solvent (0.5-1).    USE - Liquefied mixed gas used as domestic coal gas and for replacing acetylene to finish cutting process at high quality.    ADVANTAGE - The mixed gas has improved thermal efficiency without peculiar smell, good cutting effect, no pollution, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of liquefied mixed gas by putting methanol (90-95 wt.%) in a reactor and stirring at normal temperature; continuously stirring, slowly adding ethanol (5-10 wt.%), and mixing for 5-10 minutes to obtain uniformly mixed liquid; stopping stirring, standing for 8-12 minutes, and stirring for 3-6 minutes to obtain solvent; injecting liquefied gas into liquefied gas spheres and sealing the spheres; and injecting solvent into the liquefied gas spheres.
NOVELTY - An alcohol-based liquid fuel comprises (in weight%) methanol (80-90), ethanol (3-4), swill-cooked dirty oil (6.5-15), potassium hydroxide (0.2-0.4) and acetone (0.3-0.6).    USE - Alcohol-based liquid fuel is used for industrial boiler, fuel stove and heating equipment.    ADVANTAGE - The alcohol-based liquid fuel is safe, economical, renewable energy source, non-toxic and environmentally-friendly, and is prepared by easy and simple process with high calorific value (more than 7000 calories) without generating harmful gas and residual solution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alcohol-based liquid fuel, which involves adding acetone into ethanol, swill-cooked dirty oil, potassium hydroxide and methanol orderly at normal temperature and pressure, dissolving the acetone before and after the addition and keeping aside the materials.
NOVELTY - Biomass pellet fuel composition, which is prepared by: processing (in wt.%) maize straw (70-75) (less than 10% of water content) and rice husk (24-30) into a fine powder, adding calcium oxide powder(0.5-1) and mixing uniformly, is claimed.    USE - The biomass pellet fuel composition is useful for biomass combustion devices.    ADVANTAGE - The composite biomass pellet fuel: ensures good combustion, has high ash fusion point and low coking tendency in comparison with the conventional corn straw biomass pellet fuel.
NOVELTY - The method involves obtaining solid object in a gasification chamber (8), and gasifying the solid object by supplying thermal energy. Raw-synthesis gas is supplied from an outlet of the gasification chamber over a collector (6) of a synthetic gas-collecting receiver (5). A gas chamber (54) breaks particle of the solid object from the gasification chamber to the collecting receiver directly connected with an outlet of the gasification chamber at the collector during directional deflection of gas, where the directional deflection of gas is caused by an indicator arrangement (15).    USE - Method for producing synthetic gas i.e. methanol, from gasifiable solid object in a coal or biomass gasification plant.    ADVANTAGE - The method enables separating the dust particles form the synthetic gas and mixing the gas in the gas chambers, thus ensuring quality of the synthetic gas, and reducing operating and subsequent processing cost of the coal gasification plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing a synthetic gas manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gasification plant.    Synthetic gas-collecting receiver (5)    Collector (6)    Gasification chamber (8)    Indicator arrangement (15)    Gas chamber (54)
NOVELTY - Insect pest and disease-resistant organic fertilizer is composed of (in wt.%): tea seed cake meal (35-40), herba patriniae (10-15) and chicken manure (49-51).    USE - Insect pest and disease-resistant organic fertilizer used for vegetables (claimed).    ADVANTAGE - The insect pest and disease-resistant organic fertilizer has stable and long fertilizer effect, ecological and eco-friendly characteristic, no odor and high insect pest controlling, plant diseases preventing and antimicrobial activities, and is convenient in use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing the insect pest and disease-resistant organic fertilizer, which involves:    (A) composing (in wt.%): tea seed cake meal (35-40), herba patriniae (10-15) and chicken manure (49-51);    (B) inoculating microbial inoculum according to 0.15-0.25wt.% of main material;    (C) using the product as a fermentation material to perform a compost fermentation, where fermentation cycle is 20-25 days;    (D) obtaining the fermented and cured organic fertilizer;    (E) airing the fermented and cured organic fertilizer naturally for 3-4 days;    (F) placing and drying the fertilizer in a low-temperature drying box at 30-60 degrees C to obtain product with water content of 25-30%; and    (G) crushing the dried organic fertilizer to obtain the insect pest and disease-resistant organic fertilizer.
NOVELTY - The water-cooling plasma reactor device has a reaction chamber (10), an apparatus (30) for protecting pollution line which is connected to the reaction chamber, an electrode, a cooling water circulating part (50) for circulating the cooling water for cooling the electrode. The exhaust gas is flowed in within the reaction chamber and the electrode is prepared within the reaction chamber. The cooling water circulating part comprises a cooling water inlet line and a cooling water outlet line which are prepared with the double pipe.    USE - Water-cooling plasma reactor device for purification of exhaust gas.    ADVANTAGE - The water-cooling plasma reactor device has a processed reaction chamber, an apparatus for protecting pollution line which is connected to the reaction chamber, an electrode, a cooling water circulating part for circulating the cooling water for cooling the electrode, and hence ensures improved and efficient water-cooling plasma reactor device.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a water-cooling plasma reactor device.    Reaction chamber (10)    Gear chambers (20a,20c)    Apparatus (30)    Process gas supply line (33)    Cooling water circulating part (50)
NOVELTY - The invention relates to a process for treating forest wastes and to a plant for carrying out said process. According to the invention, the process consists, in a first stage, in subjecting the forest biomass to extractive solvolysis in a ratio of 1:6...1:12, depending on the nature of the material to be processed, with fermentation food ethanol, in a concentration of 50...70% with 0.5% acetic acid, at the ambient temperature, by percolation and pressure shocks, for 2...6 h, followed by extraction, centrifugal separation and pressing, wherefrom there results a purified fluid extract having 2...20% bioactive compounds which are dosed and packaged as such or are stabilized on adequate supports, as well as a spent wet residue and, after humidity correction to 65...70% is passed to the second stage of fungal destructuration by inoculation with 2...3% mycelia of lignolytic fungi, at a C/N ratio value of 24:1...35:1, wherefrom there are obtained mushroom crops and a remaining microporous substrate which is conditioned and used as fodder or as a component of a natural fertilizer. The claimed plant comprises a step dryer (2), a grinding mill (3 or 4), a basin (5), some percolation and pressure shocks extractors (6), a centrifugal separator (7), a worm press (8), the extract being passed through a dosing and packaging module (12 or 13) and the residue being passed through a sterilizer (17), an inoculation enclosure (18), a mushroom field (19), some enclosures (20) for conditioning and drying the microporous composite, some storage rooms (23) for fodder premix and some storage rooms (24) for fertilizers and heat-insulating organic substrates.
NOVELTY - An accurate and shorter acetylation method for measurement of fuel ethanol percent in fermented liquid, involves supplementing 14-22% (weight/volume) of deteriorated sugar solution in water with 0.05-0.07% of urea, 0.01-0.015% of disodium hydrogen phosphate and 0.025%-0.05% of hydrated iron oxide, sterilizing the solution at 15 psia for 15 minutes and cooling at room temperature, adding 0.025-0.05% of active dry yeast in the solution, fermenting the content at 30-35 degrees C for 72 hours, adding 2 ml of pure acetic anhydride and 40-60 ml, preferably 50 ml of 1 N sodium hydroxide and titrating excess of sodium hydroxide against N/2 hydrochloric acid using phenolphthalein as indicator till last drop of hydrochloric acid gives off a pink color. Image 0/0
NOVELTY - An eletriptan hydrobromide having alpha -form polymorphic nature is prepared by reducing (((R)-1-methylpyrrolidin-2-yl)methyl)-5-((E)-2-(phenylsulfonyl)-vinyl)-1H-indole in the presence of a metal catalyst and hydrogen in an organic solvent, isolating the eletriptan hydrobromide monohydrate, and converting the eletriptan hydrobromide monohydrate to eletriptan hydrobromide alpha -form.    USE - Process for preparation of eletriptan hydrobromide (claimed).    ADVANTAGE - By conducting hydrogenation using Raney nickel as catalyst, a tremendous amount of economy has been achieved. The process is environmentally friendly since hydrogenation is proceeding in the absence of an acid. It achieves formation of alpha -polymorph of eletriptan hydrobromide with high yield and purity.    DETAILED DESCRIPTION - Preparation of an eletriptan hydrobromide having alpha -form polymorphic nature involves reducing (((R)-1-methylpyrrolidin-2-yl)methyl)-5-((E)-2-(phenylsulfonyl)-vinyl)-1H-indole in the presence of a metal catalyst and hydrogen in an organic solvent, isolating the eletriptan hydrobromide monohydrate, and converting the eletriptan hydrobromide monohydrate to eletriptan hydrobromide alpha -form.
NOVELTY - Conversion of a biomass to a biochar involves reacting the biomass in a hydrothermal carbonization apparatus; separating and collecting products of the biomass reaction, where the products include carbon dioxide (CO2)-rich gas, biochar, and biocrude; and recycling the biocrude back to the hydrothermal carbonization apparatus.    USE - For conversion of biomass to biochar (claimed).    ADVANTAGE - The method produces a high quality biochar with high carbon and low oxygen contents; and provides higher biochar yield and reduction in the carbonization temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for converting a biomass to a biochar comprising a hydrothermal carbonization apparatus for reacting a biomass and converting the biomass into biochar, biocrude and CO2-rich gas; an exhaust valve for releasing the CO2-rich gas; a separator for separating the biochar and the biocrude; and a fluid line for recycling the biocrude back to the hydrothermal carbonization apparatus.
NOVELTY - An adsorption agent contains silver, and beta type zeolite which is hydrophobic zeolite. The beta type zeolite supports silver by ion exchange.    USE - An adsorption agent used for odorization agent removal in fuel gas of high dew point conditions (claimed).    ADVANTAGE - The adsorption agent can remove sulfur compound from fuel gas containing sulfur compounds effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an odorization agent removal method in fuel gas of high dew point conditions involving letting odorization agent containing fuel gas in very high dew point conditions pass through beta type zeolite which supports silver by ion exchange.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of test equipment of odorization agent removal method in fuel gas of high dew point conditions. (Drawing includes non-English language text).    Town-gas pipe (1)    Desulfurizer (2)    Branch pipe from town-gas pipe (3)    Tertiary-butyl mercaptan standard-gas pipe (5)    Test adsorption agent filling container (10)
NOVELTY - A fuel cell system (5) comprises a hydrogen recovery apparatus (60) that selectively recovers hydrogen from the fuel off gas of a fuel cell (50) to generate the hydrogen-containing gas whose hydrogen concentration is higher than the fuel off gas. A three-way valve (100a) stops supply of the fuel gas to an adsorber (40,41). A hydrogen supply unit (100c) supplies the hydrogen-containing gas to the adsorber when supply of the fuel gas is stopped by the three-way valve.    USE - Fuel cell system.    ADVANTAGE - Energy loss at the time of detaching ammonia of an adsorber is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the structure of a fuel cell system. (Drawing includes non-English language text.).    Fuel cell system (5)    Adsorbers (40,41)    Fuel cell (50)    Hydrogen recovery apparatus (60)    Three-way valve (100a)    Hydrogen supply unit (100c)
NOVELTY - The tool has an electric drive source receiving power supply and driving a tool. A fuel battery generates electric power by oxidization reaction between fuel and oxidant i.e. air. An air supply unit supplies air to the fuel battery as oxidant. The air supply unit is utilized as a drive source cooling unit that feeds cooling air to the electric drive source. An airflow guide unit steers a part of airflow that is generated by the air supply unit toward the fuel battery. The air supply unit is arranged on a fan (13) to generate airflow by rotation.    USE - Electric tool.    ADVANTAGE - The tool ensures that air is reliably supplied to the fuel battery as oxidant, and that the fan supplies air for the fuel battery, thus avoiding low output of the fuel battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electric tool.'(Drawing includes non-English language text)'    Fan (13)
NOVELTY - Aerobic rotary fermentation bin comprises a support seat having a riding wheel, a motor and a reduction box. The riding wheel is provided with a transversely cylindrical fermentation bin. The internal part of the fermentation bin is provided with continuously spiral threads, where the external ring part of the fermentation bin is provided with a gear transmission mechanism which is meshed with a reduction box gear.    USE - The aerobic type rotary fermentation bin useful for primary aerobic fermentation of garbage compost.    ADVANTAGE - The aerobic type rotary fermentation bin: is simple in structure with good reliability, environment friendly, easy to control the fermentation, convenient to use and maintain; has low failure rate; and produces less noise.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the aerobic type rotary fermentation bin.
NOVELTY - Natural gravity dehydration compost tank comprises three walls, where one is opened, the side wall has multiple vertical narrow seams, and the ground has multiple longitudinal water discharging channels having a certain slope.    USE - The compost tank is useful for rapidly discharging high moisture content material.    ADVANTAGE - The compost tank: rapidly discharges the moisture from side leakage and downward leakage; improves the compost material moisture condition; and advances the compost process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the natural gravity dehydration compost tank.
NOVELTY - A heating and insulation fermenting tank comprises tank body made up of tank bottom and tank ledges and having U-shaped section. The tank ledges comprise external ledge layer, ledge insulation layer, middle layer, smoldering sandwich layer and internal ledge layer. Multiple smoke discharging holes communicated with smoldering sandwich layer are formed at outside of upper part of the tank ledge. The smoke discharging holes are connected with smoke discharging channel located at outside of tank body.    USE - Fermenting tank for heating and insulation livestock and poultry manure in cold region (claimed).    ADVANTAGE - The livestock and poultry manure and straws containing about 25% of moisture are filled and heated by smoldering action in smoldering sandwich layer. The temperature of livestock and poultry manure and straws is kept by insulation layer without using electricity and coal, such that request of microorganism for fermenting temperature is met in cold region, thus reducing the cost.    DETAILED DESCRIPTION - Heating and insulation fermenting tank comprises tank body made up of tank bottom and tank ledges and having U-shaped section. The tank ledges comprise external ledge layer, ledge insulation layer, middle layer, smoldering sandwich layer and internal ledge layer. Multiple smoke discharging holes communicated with smoldering sandwich layer are formed at outside of upper part of the tank ledge. The smoke discharging holes are connected with smoke discharging channel located at outside of tank body. Multiple air holes communicated with smoldering sandwich layer are formed at outside of lower part of the tank ledges. And air doors are arranged on air holes.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a heating and insulation fermenting tank.
NOVELTY - The furnace has an internal container (2) whose outer wall is in communication with an intercommunication mutual pressure device (6) that is provided with an air supplying port (7). An inner wall of the internal container is provided with exhaust holes (8). A lower part of the device is provided with an oxygen supply pyrolysis fermentation balancer (5) that is stretched into an interior part of the device. The fermentation balancer is provided with air spray holes (9). An insulating layer (10) is arranged between the internal container and an external barrel (1).    USE - Intercommunication mutual pressure biomass gasification furnace.    ADVANTAGE - The furnace ensures better air producing speed and enables production of air within 3-5 minutes with sustained combustion time of 2-3 hours, thus saving energy. The furnace is environment-friendly. The furnace consumes 1-1.5 kg biomass during every hour of operation without causing potential safety hazard. The furnace is small in volume and convenient to use. The furnace enables automatic discharge of slag.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an intercommunication mutual pressure biomass gasification furnace.    External barrel (1)    Internal container (2)    Oxygen supply pyrolysis fermentation balancer (5)    Intercommunication mutual pressure device (6)    Air supplying port (7)    Exhaust holes (8)    Air spray holes (9)    Insulating layer (10)
NOVELTY - The device has an air exchange processing box (12) whose outer surface is provided with a heat insulating layer (13). The processing box is provided with a locking cover (10) that is filled with a heat insulating material (11). A draft fan (7) and an air distribution pipe (6) are arranged on the locking cover and connected with the processing box. A connection pipeline (5) is led from a gasifying furnace (3) directly, connected to the processing box and fixed on the locking cover of the processing box. The connection pipeline is provided with a heat insulating layer.    USE - Straw gasifying device.    ADVANTAGE - The device maintains gasifying gas at high temperature by heat insulation of the air exchange processing box and the connection pipeline. The device analyzes vapor condensation and tar oil in gasifying gas slowly without blocking the pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasifying device.    Gasifying furnace (3)    Connection pipeline (5)    Air distribution pipe (6)    Draft fan (7)    Locking cover (10)    Heat insulating material (11)    Air exchange processing box (12)    Heat insulating layer (13)
NOVELTY - The system has a drying process unit and a gasification-purification unit connected with each other. The drying process unit comprises a vibrating screen, a crusher, a pressure filter and a drying device. The gasification-purification unit comprises a loading device, a gasification furnace, a purification device and a gas-storing cabinet. The gasification furnace is connected to an ash handling equipment. Waste hot gas and part gas are generated from the gasification furnace and communicated to the drying device through a pipeline.    USE - System for Chinese medicinal dregs drying and thermal gasification process.    ADVANTAGE - The system is simple in structure and inexpensive, and reduces pollution. The system has high water ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for Chinese medicinal dregs drying and thermal gasification process.'(Drawing includes non-English language text)'
NOVELTY - The system has a tar oil collection tower whose outlet is connected to a liquid tar oil conveying device that is connected to a gasifying furnace. The liquid tar oil conveying device comprises a base that is provided with a tar oil pump and a heat insulating layer. One end of the tar oil pump is connected to a tar oil heating container through a heat insulating pipe and another end is connected to a venturi nozzle inlet. An inner wall of the tar oil heating container is provided with a temperature sensor.    USE - High-temperature pyrolysis system for biomass gas tar oil.    ADVANTAGE - The system can recycle the waste tar oil effectively, and improves utilization rate of the tar oil. The system is easy to produce with low production cost, and has wide range of application.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high-temperature pyrolysis system.'(Drawing includes non-English language text)'
NOVELTY - Production system of refuse-derived fuel comprises a drier, a primary crusher, a blender mixer, a fine crusher and a molding machine connected with each other in an order by a transmission device.    USE - Used as a production system of refuse-derived fuel.    ADVANTAGE - The system: has a rapid molding capacity; produces the fuel particles with a sufficiently high density; has a continuous feeding capacity; and produces the waste derived fuel from municipal solid waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the production system of refuse-derived fuel.
NOVELTY - The furnace has a kitchen range (1) arranged at a top part of a furnace cover (3) that is internally provided with an upper furnace body (4). An upper end of a furnace wall (16) is provided with air inlet holes (5) that are arranged around the furnace wall. A retaining plate lifting rod (11) is provided with a vertical north at a place contacted with the furnace wall and externally sleeved by a casing pipe (12) connected with the furnace wall. A side of the retaining plate lifting rod is provided with multiple equal spaced tooth for positioning of a lifting rod clamping spring (9).    USE - Biomass furnace for gasification and burning of firewood.    ADVANTAGE - The furnace produces strong fire without smoke, dust and smell. The furnace ensures that the wood charcoal is produced by the raw material after gasification and burning process is burned and utilized, so that the furnace has high-efficiency, and better energy-saving effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass furnace.    Kitchen range (1)    Furnace cover (3)    Upper furnace body (4)    Air inlet holes (5)    Lifting rod clamping spring (9)    Retaining plate lifting rod (11)    Casing pipe (12)    Furnace wall (16)
NOVELTY - The furnace has a wind inlet ring (12) connected with an outside part and provided on a shoulder part of a furnace body (11). The inlet ring is connected with a fan (13) by a wind inlet pipe (14), and an ash mouth (20) is arranged at a lower part of a gasification room (18). A burning room is formed at an upper part of a fire outlet ring (17) and divided into a large burning room (23) and a small burning room (24), where the large and small burning rooms are connected with each other. One of the burning rooms is connected with a smoke discharge channel (25) connected with the outside part.    USE - Multifunctional low-emission biomass half gasification furnace. Can also be used for washing vegetables.    ADVANTAGE - The furnace sufficiently and completely burns the fuel, thus improving thermal efficiency of the furnace and use ratio of the energy sources. The furnace is easy to light. The furnace diversifies the functions of the furnace, and can replace a solar water heater.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a multifunctional low-emission biomass half gasification furnace in partial section.    Furnace body (11)    Wind inlet ring (12)    Fan (13)    Wind inlet pipe (14)    Fire outlet ring (17)    Gasification room (18)    Ash mouth (20)    Large burning room (23)    Small burning room (24)    Smoke discharge channel (25)
NOVELTY - Producing methane-containing biogas from biomass, comprises subjecting the biomass to hydrolysis and open acidification and methanogenesis, where the biomass is supplied in the form of combustion gases by open hydrolysis during the acidification of carbon dioxide.    USE - The biogas is useful for operating an internal combustion engine (claimed).    ADVANTAGE - The simple process produces the biogas in high productivity.
NOVELTY - A graphite oxide is reduced using polyvinyl alcohol solution, and deionized water is separated, to form graphene sheet.    USE - Manufacture of graphene sheet. Uses include but are not limited to field effect transistor, lithium-ion battery, nanochemical sensor, ultrahigh sensitive biosensor, molecular sensor, artificial muscle-type actuator, and filler for high-performance polymer nanocomposite material.    ADVANTAGE - The graphene sheet is environmentally-friendly, and is manufactured efficiently and easily.
NOVELTY - For producing an alcohol from a metabolite comprising 2-keto acid, and carbon dioxide as a carbon source, a recombinant microorganism (M1) capable of using hydrogen or formate for reduction of carbon dioxide, is used.    USE - For producing an alcohol selected from 1-propanol, isobutanol, 1-butanol, 2-methyl-1-butanol, 3-methyl-1-butanol and 2-phenylethanol (preferably isobutanol) from carbon dioxide as the carbon source; the alcohols are useful as biofuels (all claimed).    ADVANTAGE - The recombinant microorganism produces greater than 100 (preferably 120) mg/l of isobutanol and greater than 150 (preferably 180) mg/l of 3-methyl-1-butanol in 40 hours from sugar. The microorganism can utilize man-made (electrically generated) reducing mediators (hydrogen or formate) without relying on inefficient photoenergy conversion to produce the alcohols.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing a biofuel involving culturing the microorganism (M1) in the presence of a suitable carbon source and reducing agent, and isolating the biofuel.
NOVELTY - Phyllosilicate.    USE - The phyllosilicate is useful as cation exchanger for decontamination of organic pollutants (claimed).    ADVANTAGE - The phyllosilicate efficiently decontaminates organic pollutants, and environment friendly.    DETAILED DESCRIPTION - Phyllosilicate of Formula I: A4-nBnZ8YqO20(X)4.    A=sodium, potassium or any combination;    B=a (12-18C) alkyldecylamonium;    Y=selected from aluminum, magnesium, iron or any combination;    Z=selected from silicon, aluminum, iron (III), titanium or any combination;    X=selected from fluoride, hydroxide, oxygen, chlorine or any combination;    n=between 1-4; and    q=between 4-6.    INDEPENDENT CLAIMS are:    (1) use of phyllosilicate as cation exchanger for decontamination of organic pollutants; and    (2) a process for obtaining a phyllosilicate, comprising: (a) protonation of amino groups alkyldecylamonium (12-18C); (b) addition to the solution of step (a) a mica of formula II: A4Z8YqO20(X)4; (c) addition to the product obtained in step (b) in a liquid medium and subsequent centrifugation; and (d) drying the solid obtained in step (c) at temperatures above 15 degrees C.
NOVELTY - Method for producing xylitol, involves using mixture of hemicellulosic sugars.    USE - The method is useful for producing xylitol which is used as byproduct in ethanol production.    ADVANTAGE - The xylitol is produced at purity of approximately 100% from equivalent mixture of D-xylose, L-arabinose and D-glucose with minimal production of L-arabinitol byproduct. The method is cost-effective and can be performed within short period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microorganism capable of converting mixture of sugars by fermenting the sugar to xylitol with little or no arabinitol in the final fermentation broth, where the sugars are chosen from xylose, arabinose and their combinations; and    (2) bioprocess for converting mixture of sugars.
NOVELTY - An aminoguanidine compound and ( beta )-diketone compound (III) are reacted to manufacture pyrimidinyl pyrazole compound (Ia) or (Ib).    USE - Manufacture of pyrimidinyl pyrazole compound.    ADVANTAGE - The pyrimidinyl pyrazole compound is economically manufactured without affecting the environment.    DETAILED DESCRIPTION - An aminoguanidine compound or its salt and ( beta )-diketone compound of formula (III) are reacted to manufacture pyrimidinyl pyrazole compound of formula (Ia) or (Ib).    R1,R3=1-4C alkyl;and    R2=H or 1-4C alkyl.
NOVELTY - Air inside a passenger compartment of a vehicle which is equipped with a secondary battery or a fuel cell to drive wheels via a motor is harmonized by supplying methanol (AA) and an oxidizing gas (BB) to a catalyst (CC), combusting methanol and harmonizing the passenger compartment using the generated heat (EE). The methanol is produced from the carbon dioxide (GG).    USE - Air conditioning of motor vehicle e.g. electric vehicle.    ADVANTAGE - The method enables efficient air conditioning of motor vehicle, and durability of motor vehicle and battery in motor vehicle are improved. The carbon dioxide emitted from factory is efficiently recycled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for utilization of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the air conditioning of motor vehicle. (Drawing includes non-English language text)    Methanol (AA)    Oxidizing gas (BB)    Catalyst (CC)    Heat (EE)    Carbon dioxide (GG)
NOVELTY - Method comprises saccharifying a biomass feedstock in a liquid medium in a vessel to form a sugar solution having a concentration of at least 15%, and converting the sugar solution to a product, in the same vessel, utilizing an enzyme and/or a microorganism.    USE - The method is useful for processing biomass feedstocks (e.g. plant biomass, animal biomass and municipal waste biomass) to produce useful products, such as fuels.    ADVANTAGE - In the method, the multiple processing steps, e.g. saccharification, fermentation and distillation, are conducted in a single tank with reduced process times and cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system comprising a tank, a delivery system configured to deliver a biomass feedstock, a saccharification agent, and a liquid medium to the tank, a mixer configured to mix the delivered biomass feedstock and saccharifying agent, and a vacuum distillation system in communication with the tank, configured to distill a product from the contents of the tank.
NOVELTY - An isolated polypeptide comprising a 111 or 97 amino acid sequence (SEQ ID NO: 1 or 2) fully defined in the specification, or amino acid sequence exhibiting at least 70% homology to SEQ ID NO: 1 or 2, is new. The polypeptide (a) increases activity of a polysaccharide hydrolase, (b) binds to a polysaccharide, and (c) is deficient of polysaccharide hydrolase activity.    USE - The isolated polypeptide is useful for degrading polysaccharide into monosaccharide, which is used as biofuel (all claimed), and as affinity tags.    ADVANTAGE - The method (M2) is cost-effective and enables large scale production of biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition comprising the above-mentioned polypeptide, where the polypeptide comprises glycoside hydrolase 45 (GH45) domain or pollen-allergen (Grp 2/3) domain derived from bacterial expansin or expansin-like protein;    (2) method (M1) of degrading a polysaccharide, involves adding the isolated polypeptide to a polysaccharide material; and    (3) method (M2) of producing a biofuel from the polysaccharide, involves performing the above-mentioned method (M1), incubating at least one of polysaccharide hydrolase, hydrolysis catalyst, acid or microorganism with the polysaccharide material to obtain monosaccharide, and fermenting the monosaccharide to obtain biofuel using a fermenting microorganism.
NOVELTY - Sewage gas generating system comprises a fermenting system, a desulfurizing system and a generating system. The fermenting system comprises a steel acidifying tank, a fermenting tank and a solar heating system. A bottom part of the acidifying tank is provided with a sewage slag tube of the fermenting tank. The position of the acidifying tank is higher than the fermenting tank. The solar heating system comprises a heat absorbing plate for absorbing solar energy and a hot water tube heated by the heat absorbing plate. The hot water tube is spirally installed in the fermenting tank.    USE - Used as a sewage gas generating system.    ADVANTAGE - The sewage gas generating system: is provided with a solar heating system and mechanical stirring system for fermenting tank, which increase and stabilize the gas yield; has easy discharge and management; and has a good design, installation, use, maintenance, raw material supply and waste material recovery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sewage gas generating system.
NOVELTY - Polygonal cultural substrate processing involves collecting coarse powder of organic material and reproducible offal of subsidiary agricultural product, where the product includes coconut shell, waste pills of processed northern wood and other straws and roots having high content of hard cellulose. Biological organic compost is produced, where coarse powders of the organic material are crushed by a crushing machine and then the material is fermented to obtain black and mature product.    USE - Method for processing a polygonal cultural substrate for biodynamic controlled-release fertilizer (claimed).    ADVANTAGE - The polygonal cultural substrate processing method enables to produce low cost substrate, where the substrate can adsorb and maintain water to resist drought, prevent plant roots from heat radiation and has wind resistance and rain resistance features.    DETAILED DESCRIPTION - Polygonal cultural substrate processing involves collecting coarse powder of organic material and reproducible offal of subsidiary agricultural product, where the product includes coconut shell, waste pills of processed northern wood and other straws and roots having high content of hard cellulose. Biological organic compost is produced, where coarse powders of the organic material are crushed by a crushing machine and then the material is fermented to obtain black and mature product. The biological organic compost is dried and stored. Stored biological organic compost (60 parts), attapulgite adhesive powder (10 parts) and siliceous rock grains (30 parts) are immersed in 3% soluble composite nutrient solution. The mud shaped materials are stirred uniformly, where soluble adhesive is added to the mixture in ratio of 3-5:1. The mixture is pressed into mold shape, where the mixture is placed in the tile or screen shaped die and then the mold is dried in a drying room.
NOVELTY - The method involves forming a concentrator pattern on a surface of a rolling rod. An electrode sheet is wound in the rolling rod, and a tube type supporter electrode is molded above the concentrator pattern. Heat is applied to an inner surface of an electrode sheet, and the rolling rod is separated from the electrode sheet. Drying paste is coated on the concentrator pattern, and a current collecting part is formed in a side of the electrode sheet. A conductive material is formed in a side of a concentrator sheet.    USE - Method for manufacturing a supporter electrode i.e. fuel anode of a solid electrolyte fuel cell (all claimed).    ADVANTAGE - The method enables readily forming the current collecting part on an inner surface of the tube type supporter electrode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid electrolyte fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a supporter electrode manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - A biomass and waste continuous quick microwave cracking device comprises feeding hopper, storage tank, and microwave reactor with material propelling device, which are connected in turn. The microwave reactor is connected with groups of microwave generators. The microwave reactor has cracking gas exhausting opening and solid residue exhausting opening.    USE - A biomass and waste continuous quick microwave cracking device.    ADVANTAGE - The device is simple in structure, rational in design, and good for utilizing biomass and waste resource on site.
NOVELTY - Method of producing hydrogen from biomass, involves subjecting substrate to enzymatic reaction in the presence of microorganisms.    USE - The method is useful for producing hydrogen from biomass and purifying wastewater.
NOVELTY - Methane and solid forming fuel are co-produced from herbal wood fiber raw material by crushing wood fiber to grain diameter of less than 40 mm; performing methane fermentation at controlled solid concentration of 20-40%; drying obtained methane slag to moisture content of 6-20%; secondarily crushing the dried methane slag to grain diameter of less than 5 mm; compressing and hot-forming; and cooling and packing obtained fuel.    USE - Method for co-producing methane and solid forming fuel from herbal wood fiber raw material (claimed).    ADVANTAGE - The method can solve problem on processing of methane slag, thus realizing whole energy utilization of resource.
NOVELTY - An unpowered pyrolysis reactor comprises upper and lower spiral feeders separately provided with biomass hopper and solid heat carrier hopper; and a U-shaped pyrolysis reaction device including dropping-type gas pipe, parallel lifting pipe and lifting-type reaction pipe. A discharge hole of upper spiral feeder is connected with a conveying pipe of lower spiral feeder. A discharge hole of lower spiral feeder is connected with the gas pipe. An upper end of reaction pipe has reaction outlet. The reaction pipe and gas pipe are separately provided with an observation hole.    USE - Unpowered pyrolysis reactor used for biomass and solid heat carrier, particularly solid substance with uniform particles and particle size of 1.8-2.2 mm (claimed).    ADVANTAGE - The reactor realizes uniform pyrolysis temperature of biomass raw materials and full pyrolysis reaction, thus, improving oil production rate and oil quality, energy resource use ratio and operational service life of equipment; and reducing the volume of equipment and operational cost.
NOVELTY - A biological coal is generated by using a computer system for detecting water content of urban sludge in a pipeline, adding fly ash to an urban sludge pipeline via fly ash pipeline in terms of the detected water content, enabling the fly ash and urban sludge to mix and react to absorb the water, controlling the water content of the mixture of a material outlet after the reaction to 1-5%, adding liquid deodorant to the mixture to blend in a blending tank, controlling the water content of the blended urban sludge to 8-10%, and making into particles of different graduations through a granulator.    USE - Method for generating biological coal (claimed).    ADVANTAGE - The method reduces the stacking area of the fly ash of the power plant while the urban sludge is solved. The volatile percentage of the produced biological coal receiving basis is 27-35%. The low-position heating quantity is 3000-4000 kcal/kg, similar to that of the coal. Continuous combustion can be realized completely.
NOVELTY - Preparation of liquid fuel with biomass comprises mixing biomass powder, catalyst and hydrogen supplying solvent to form raw material slurry; feeding slurry in reactor; performing pyrolysis, dissolving and hydrogen transferring reactions; separating gas, liquid and solid to obtain liquefied generating gas, liquefied generating oil and slag; cooling liquefied generating gas to form layers of dried gas, condensed oil and condensed water; and distilling liquefied generating oil to obtain rough distillation product and circulation solvent distillation product.    USE - Preparation of liquid fuel with biomass.    DETAILED DESCRIPTION - Preparation of liquid fuel with biomass comprises pre-processing biomass material by grinding, drying and forming powder; hydroprocessing solvent to form hydrogen supplying solvent; mixing powder, catalyst and hydrogen supplying solvent to form raw material slurry; feeding raw material slurry in reactor; performing pyrolysis, dissolving and hydrogen transferring reactions; separating gas, liquid and solid to obtain liquefied generating gas, liquefied generating oil and slag; cooling liquefied generating gas form layers of dried gas, condensed oil and condensed water; distilling liquefied generating oil to obtain rough distillation product and circulation solvent distillation product; extracting solvent in circulation solvent distillation product to obtain ideal hydrogen carrier and non-ideal hydrogen carrier; mixing and refining condensed oil, rough distillation product and non-ideal hydrogen carrier; and fractionating to acquire qualified fuel oil product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a process for preparing liquid fuel with biomass.
NOVELTY - The coupling device has fermenting tank whose lower side of liquid surface is provided with a high frequency ultrasonic vaporizer. An atomization catcher collects the atomization on the liquid surface of the fermenting tank to obtain ethyl alcohol liquor. The catcher uses structure of spraying-filling tower coupling. A device concentrates and recovers the collected ethyl alcohol liquor.    USE - Biomass fermentation-separation coupling device used for preparing ethyl alcohol (claimed).    ADVANTAGE - The device can separate ethyl alcohol during fermenting process and reduce the influence of ethyl alcohol. The ethyl alcohol can be separated with high efficiency and with less energy consumption. The manufacturing cost of the ethyl alcohol can be reduced.    DETAILED DESCRIPTION - The fermenting raw material is obtained from cellulose hydrolase. An INDEPENDENT CLAIM is included for method for preparing ethyl alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fermentation-separation coupling device. (Drawing includes non-English language text)
NOVELTY - Producing ethanol and silica involves washing and peeling rice straw with deionized water to remove dust. The obtained material is heated in hydrogen chloride solution at 130-150 degrees C for 30 minutes. The heated material is dried in oven at 70-100 degrees C, and then the dried material is crushed in a grinder. The crushed material is hydrolyzed in a bioreactor with enzymatic cellulose and hemicellulose fraction. The hydrolyzed material is filtered and then fermented with Saccharomyces cerevisiae, Pichia stipitis and other species.    USE - Method for producing ethanol used as fuel, and silica.    ADVANTAGE - The method enables to produce ethanol and highly pure amorphous silica.
NOVELTY - Producing ethanol involves obtaining casein whey fraction from milk and cheese. The fraction is obtained by centrifuging materials at 4-10 degrees C at pH 4-5, and filtering the material by ultrafiltration membrane. The filtered material is dried and lyophilized, and then processed with beta - galactosidase in presence of fungi or bacteria. The fungi or the bacteria are Aspergillus niger, A. oryzae, A. foetidus or A. phoenecia.    USE - Method for producing ethanol used as fuel.    ADVANTAGE - The method enables to produce ethanol in a simple manner.    DETAILED DESCRIPTION - Producing ethanol involves obtaining casein whey fraction from milk and cheese. The fraction is obtained by centrifuging materials at 4-10 degrees C at pH 4-5, and filtering the material by ultrafiltration membrane. The filtered material is dried and lyophilized, and then processed with beta - galactosidase in presence of fungi or bacteria. The fungi or the bacteria are Aspergillus niger, A. oryzae, A. foetidus, A. phoenecia, Kluyveromyces marxianus, K. lactis, K. fragilis pseudotropicalis, Candida, Saccharomyces, Lactobacillus bulgaricus, L. thermophilus, Streptococcus lactis or Bacillus. Serum is used as carbon and nitrogen source in the medium. The obtained material is hydrolyzed at 40-70 degrees C. The hydrolyzed material is processed with ethanol or ammonium sulfate and then lyophilized, and then processed with beta - galactosidase. The obtained product is fermented with Saccharomyces, Kluyveromyces, Pichia, Rhodotorula or Zygosaccharomyces, Hansenula to obtain the desired product.
NOVELTY - Xylosidase/arabinosidase comprising fully defined 332 amino acid (SEQ ID NO: 2), as given in the specification, is new.    USE - The xylosidase/arabinosidase is useful: for preparing feed additive, saccharifying hemicellulose or arabinoxylan, and producing ethanol (all claimed); bio-conversion of cellulose; and in the field of e.g. chemical, textile, food, bio-energy and medical industries.    ADVANTAGE - The xylosidase/arabinosidase: has beta -D-glucosidase and alpha -L-arabinofuranosidase activity; and maintains high activity at low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a recombinant vector comprising the nucleotide coding sequence of the xylosidase/arabinosidase;    (2) a recombinant strain containing the recombinant vector;    (3) preparing the xylosidase/arabinosidase bi-functional enzyme, comprising culturing recombinant strain and separating the target protein, where the specific method comprises (i) performing polymerase amplification reaction by primer to obtain the nucleotide coding sequence of the xylosidase/arabinosidase bi-functional enzyme to form the recombinant expression vector of xylosidase/arabinosidase bi-functional enzyme, (ii) inducing the recombinant expression vector into the expression host cell to express xylosidase/arabinosidase bi-functional enzyme in thalli, and (iii) separating and recovering xylosidase/arabinosidase bi-functional enzyme; and    (4) the composition containing xylanase and the xylosidase/arabinosidase bi-functional enzyme.
NOVELTY - Organic pesticidal fertilizer comprises (in parts) chinaberry bark (8-15) and the plant stems and leaves (85-92).    USE - The fertilizer is useful for chinaberry bar.    ADVANTAGE - The fertilizer improves soil fertility, yield and the quality of the crop, and thus it is suitable for many crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic pesticidal fertilizer, comprising: (i) crushing the chinaberry bar via a 100-mesh sieve; (ii) drying the plant stems and leaves, cutting to be 1-2 inches long; (iii) uniformly mixing the crushed chinaberry bar and the dried plant stems and leaves; (iv) placing the mixture obtained in the step (iii) into a fermentation tower to ferment for 7-8 days; (v) removing the fermented fertilizer, drying until the water content is 8-10%; and (vi) granulating the fermented fertilizer obtained in the step (v), packing, and preserving in a storage container.
NOVELTY - The device has charging hopper whose discharging end connected with bag garbage breaking machine that connected with sorting box main portion through chuting hopper. The inner side of hopper is provided with humidifying water distribution pipeline. The hopper and pipeline constructs spray humidifying unit. The reclamation comprehensive treatment system has organics fertilizer-making unit, inorganic brick-making unit, waste plastic-particle making unit and metal recycling unit which are respectively connected with discharging unit of sorting recycling system.    USE - Device for treatment, reclamation and recycling of municipal solid waste.    ADVANTAGE - The sorting and reclamation efficiency of the device are improved.    DETAILED DESCRIPTION - The device has sorting box main portion whose inner side is provided with mechanical rotating drum screening unit. A magnetic force sorting unit and gravity sorting unit are connected in series. The bottom of sorting box main portion is provided with discharging unit. The sides of sorting box main portion are connected with air blower through wind intake pipe and wind outtake pipe. The wind outtake pipe is connected with whirlwind deduster that connected with exhaust fan whose wind outlet is connected with charging hopper through wind returning pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of device for treatment, reclamation and recycling of municipal solid waste.
NOVELTY - A cleaning solvent contains mixture of 4-10C saturated hydrocarbon, 14C saturated hydrocarbon and 15C saturated hydrocarbon.    USE - Cleaning solvent is used for cleaning polymerization reactor of butyl rubber (claimed).    ADVANTAGE - The cleaning solvent is manufactured efficiently with excellent workability and reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cleaning method of polymerization reactor of butyl rubber, which involves pumping a solvent to a reactor, cleaning the reactor, and returning the solvent from the reactor to a storage tank. The solvent in the storage tank is heated to 100-250 degrees C by pumping the solvent to a heater through another outlet, steamed in a flash drum to change the solvent to gaseous solvent and condensed to liquid through a condenser, the liquid is injected into the storage tank, and the remaining high-concentration glue is discharged in the flash drum out from the bottom of the tank under high pressure to produce byproducts.
NOVELTY - Ash fusion point of biomass fuel is improved by preparing composite additive (pts. wt.) comprising kaolin (5-20), acidic argil (0-15), kieselguhr (0-15), bentonite (0-10), coal (0-20), and coal gangue (0-25); and crushing biomass fuel and composite additive, adding composite additive into the biomass fuel, uniformly mixing by direct mixing method, and greatly improving ash fusion point (Ts) of the biomass fuel. The amount of additive is based on 100 pts. of ash in biomass fuel.    USE - Method for improving ash fusion point of biomass fuel.    ADVANTAGE - The method has simple operation and low cost.
NOVELTY - Producing biological clean fuel comprises crushing or cutting up fruits; mixing the crushed or cut fruits with an alkaline compound; separating oil from solid mixture; and heating the oil mixture. The fruits are oil palm fresh fruit, stem of oil palm fresh fruit or manioca fruit. The alkaline compound can be dissolved in glycerol. The oil mixture is oil palm fresh fruit, stem of oil palm fresh fruit or manioca fruit.    USE - Method for producing biological clean fuel (claimed).    ADVANTAGE - The method can prepare fuel having low viscosity, low flow point and low cold filtering point; reduces wax distillation; and has attraction economically as the high extracting ratio (yield).
NOVELTY - Comprehensive application technology of biological fermentation of the biogas project, where the engineering comprises gathering and decomposing tank, material feeding tank, integrated fermenting tower, discharged material collecting tank, depositing tanks, separating tank, purifying tank and relative control systems and devices, excrement and straws can be converted into methane, biological organic fertilizer and water for agricultural irrigation by biological fermentation technology and relative device to obtain zero emission.    USE - The comprehensive application technology of biological fermentation of biogas project.    ADVANTAGE - The comprehensive application technology of biological fermentation of biogas project has excellent operation status.
NOVELTY - Water is added to acid residue produced during concentration of phosphoric acid for diluting, to obtain 8-12% of diluted phosphoric acid containing phosphorus pentoxide. The diluted phosphoric acid is neutralized using calcium carbonate with density of (1.15-1.2)x 103 kg/m3 to obtain a neutralized slurry. The neutralized slurry is settled after clarifying, and the obtained clear liquid is used for producing food-grade calcium hydrophosphate. The obtained thick slurry is centrifugally washed to produce fertilizer-grade calcium hydrophosphate.    USE - Recycling of acid residue produced during concentration of phosphoric acid.    ADVANTAGE - The method enables efficient utilization of acid residue of concentrated phosphoric acid, provides food-grade calcium hydrophosphate and fertilizer-grade calcium hydrophosphate with high added value, and reduces environmental pollution.
NOVELTY - Catalase catalyst comprises bismuth ferrite.    USE - Catalase catalyst for generating strong oxidizing hydroxyl radical oxydase substrate for detecting and analyzing hydrogen peroxide content in food, organisms and environmental samples; and for degrading and mineralizing organic pollutant, e.g. organic dyestuff, endocrine disrupters, antibiotic or organochlorine pesticide (claimed).    ADVANTAGE - The method used is simple, low cost, and stable chemical activity. The catalyst can be magnetically recycled, thus it can repeatedly be used. It overcomes problems of labor and time consuming, high cost, instability of catalyst in using process and difficulty of recycling when composing catalase catalyst in prior art.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalase catalyst by dissolving ferric nitrate and bismuth nitrate at molar ratio of 1:1 into ethylene glycol monomethyl ether solution, in which molar ratio of ethylene glycol monomethyl ether solution and iron atoms in ferric nitrate is 8-600:1 preferably 10-30:1 and most preferably 20-1; stirring for 5-60 minutes at 25-60 degrees C; adjusting pH of solution to 4-7 using 0.1-6 mol/l nitric acid; adding coordinating agent into solution such that molar ratio of coordinating agent and iron atoms in ferric nitrate is 0.1-5:1 preferably 1-3:1, and most preferably 1:1; adding dispersing agent such that molar ratio of dispersing agent and iron atoms in ferric nitrate is 5-100:1 preferably 10-20:1 and most preferably 15:1; stirring for 10-100 minutes at 25-150 degrees C to obtain black brown sol; keeping at 100 degrees C for 5-40 hours to obtain gel; roasting gel in electric furnace for 5-50 minutes; and delivering to muffle furnace and keeping for 2-10 hours at 400-600 degrees C to obtain grain catalase catalyst bismuth ferrite.
NOVELTY - Production of substitute natural gas is carried out using a system comprising an air cooling-type methanation reactor to preheat and carry out methanation, a water cooling-type methanation reactor as a main reactor to carry out methanation of carbon monoxide, and a heat insulating methanation reactor to overheat saturation steam. The water cooling-type methanation reactor has carbon monoxide conversion ratio of 60-80%.    USE - Production of substitute natural gas.    ADVANTAGE - The method enables economical and efficient production of substitute natural gas, with high yield and reduced energy consumption.
NOVELTY - An aluminum-lithium multi-element alloy contains aluminum, lithium and other metal chosen from bismuth, gallium, zinc, mercury, indium, calcium and lanthanum. The total content of aluminum and lithium is 80-99 weight%. The content of other metal is 1-20 weight%.    USE - Aluminum-lithium multi-element alloy is used for producing hydrogen used as fuel for fuel battery, underwater submarine, torpedo and aircraft.    ADVANTAGE - The aluminum-lithium multi-element alloy is manufactured efficiently and economically with excellent workability and productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of aluminum-lithium multi-element alloy, which involves mixing alloy raw material by ball grinding under argon atmosphere at 500 degrees C, and smelting at more than 700 degrees C.
NOVELTY - Synthesizing naproxen comprises: (a) dissolving 2-bromo-methoxyl naphthalene and cyanoacetic acid salt derivative into solvent, and under the catalysis of palladium catalyst and organic phosphine ligand, performing decarboxylation coupling reaction to obtain the naphthalene derivative; and (b) performing hydrolysis on the naphthalene derivative to obtain naproxen.    USE - The process is useful for synthesizing naproxen (claimed).    ADVANTAGE - The process has simple and easy operation, wide material sources, and low cost. Moreover, during the synthesis, only inorganic salt and carbon dioxide are generated; thus, the process is safe and environment-friendly.    DETAILED DESCRIPTION - Synthesizing naproxen comprises: (a) dissolving 2-bromo-methoxyl naphthalene and cyanoacetic acid salt derivative of Formula (I) into solvent, and under the catalysis of palladium catalyst and organic phosphine ligand, performing decarboxylation coupling reaction to obtain the naphthalene derivative of Formula (II); and (b) performing hydrolysis on the naphthalene derivative of Formula (II) to obtain naproxen.    M=alkali metal or alkaline earth metal.
NOVELTY - Acetylated decoloration of resveratrol dimer is performed by distilling pyridine solvent in depressurized manner; de-watering and purifying pyridine solvent; grinding resveratrol dimer; drying and de-watering the powder; adding the powder into the solvent; adding acetylated reagent; putting the mixture away from sunlight at 4-10 degrees C; adding water into the reaction system to separate out the reactant; filtering; washing away residue; and drying at 50 degrees C to obtain the acetylated resveratrol dimer.    USE - Method for acetylated decoloration of resveratrol dimer (claimed).    ADVANTAGE - The method has high product transformation rate (more than 95%), mild reaction condition, short reaction time, repeated solvent, and low preparation cost. It is environment-friendly and the prepared acetylated resveratrol dimer has improved sterilization effect, enhanced bioactivity, improved drug absorbability and enhanced drug effect.    DETAILED DESCRIPTION - Acetylated decoloration of resveratrol dimer comprises distilling pyridine solvent in depressurized manner; de-watering and purifying pyridine solvent; grinding the resveratrol dimer; drying and de-watering the powder; adding the powder (5-10 mass%) into the pyridine solvent to be dissolved; adding acetylated reagent; putting the mixture at a position away from sunlight at 4-10 degrees C to be mixed for reaction for 12-24 hours; adding water into the reaction system to separate out the reactant; filtering; washing away the residue by using water; and drying at 50 degrees C to obtain the acetylated resveratrol dimer.
NOVELTY - A system of a fuel cell stack (1100) comprises: multiple fuel cell sub-stacks (1102) electrically coupled to one another, where the multiple fuel cell sub-stacks includes multiple fuel cells electrically coupled to one another enclosed in a sub-stack vessel; where each of the multiple fuel cell sub-stacks is replaceable online.    USE - As system of a fuel cell stack (claimed) useful in electrochemical conversion for electrical energy generation.    ADVANTAGE - The fuel cell structure utilizes a cathode which allows operation below 800 degrees C with preferred operating temperature of 650 degrees C, thus decreases severity of any molten salt corrosion taking place and reduces the tendency for the reverse Boudouard reaction to take place; hence reduces cell efficiency and allows the designer freedom to adjust the horizontal distances between plates to allow for different feed stocks which have differing reactivity's and require greater or lesser residence time in the anode zone. The fuel cell structure has longer reaction zones due to height to width aspect ratio of the anode compartments, thus decreases the extent of the reverse Boudouard reaction in each cell, and lowers its efficiency; and has a pyrolysis zone and allows the use of feedstocks with some volatile components.    DESCRIPTION OF DRAWING(S) - The figure shows a diagrammatic view of a fuel cell stack having multiple sub-stacks that are replaceable online.    Fuel cell stack (1100)    Fuel cell sub-stacks (1102)    Old or malfunctioned fuel cell sub-stack (1104)    New sub-stack (1106)    Thermal insulation (1110)
NOVELTY - Converting high free fatty acid (FFA) source material into alkyl esters, comprises reacting a mixture of the source material with an esterification reagent comprising acid catalyst and alcohol for a sufficient time in a reactor vessel, to produce alkyl esters.    USE - The method is useful for converting high free fatty acid (FFA) source material into alkyl esters, where the alkyl esters are methyl esters (claimed), which are useful as biofuel.    ADVANTAGE - The method provides a single-step conversion of the high FFA materials in FOGs to their alkyl esters.
NOVELTY - Solid fuel comprises composition containing dry seeds or cake of fruits chosen from Ricinus communis, Triadica sebifera, Jatropha curcus, Brassica rapa var. nippo-olifera, Palmae, Zea mays and Prosopis glandulosa (70 wt.% or more), where the cake is obtained by heat compression molding process.    USE - The solid fuel is useful for generating electric power of 15-30 MJ/kg (claimed).    ADVANTAGE - The fuel has specific gravity of 0.3-0.6 g/cm3 and size of 15-3500 cm3, and retains stability even when 5 wt.% or less amount of the cake is pulverized.
NOVELTY - A fuel reforming system comprises a reformer that produces fuel gas that includes hydrogen by reforming a reforming by a steam reforming reaction using reforming water; supply amount regulating means for regulating an amount of the reforming water supplied to the reformer; pressure detecting means for detecting a gas pressure in the reformer; and correcting means for correcting the amount of supplied reforming water with the supply amount regulating means based on a fluctuation amount in the gas pressure detected by the pressure detecting means.    USE - The fuel reforming system is used for regulating an amount of reforming water supplied to a reformer that produces fuel gas that includes hydrogen (claimed).    ADVANTAGE - The fuel reforming system is capable of optimally controlling the supply amount of reforming water without using a detector such as a flow meter that detects the steam flow rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a control method of a fuel reforming system that regulates an amount of reforming water supplied to a reformer that produces fuel gas that includes hydrogen by reforming a reforming fuel by a steam reforming reaction using the reforming water.
NOVELTY - Hydrogen gas generator (100) comprises: a container (110); and a capillary structure (120), disposed between the container and a flexible solid fuel (140), where the container is capable of accommodating liquid water, and the liquid water accommodated in the container is capable of being transferred to the flexible solid fuel by the capillary structure to react with the flexible solid fuel to generate hydrogen gas.    USE - The hydrogen gas generator is useful in a fuel cell (claimed) for electronic apparatuses e.g. notebook computer and mobile phone, or transportation means including vehicles or ships.    ADVANTAGE - The hydrogen gas generator utilizes liquid water that transfers hydrogen gas to the solid fuel durably and stably releases hydrogen gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell comprising the hydrogen gas generator, a cell pile and a guiding structure connected between the hydrogen gas generator and the cell pile and capable of transferring the hydrogen gas generated by the reaction of the flexible solid fuel and the liquid water to the cell pile.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a hydrogen gas generator.    Hydrogen gas generator (100)    Container (110)    Capillary structure (120)    Elastic bag like body (130)    Solid fuel (140)
NOVELTY - Pyrolytic installation for utilization of solid domestic waste, comprises: (a) vertically placed tubular chambers for the thermal decomposition of solid domestic waste with charging and discharging devices; and (b) devices of heating the solid domestic waste with the use of its own pyrolytic gas.    USE - The pyrolytic installation is useful for utilization of solid domestic waste (claimed).    DETAILED DESCRIPTION - Pyrolytic installation for utilization of solid domestic waste, comprises: (a) vertically placed tubular chambers for the thermal decomposition of solid domestic waste with charging and discharging devices; and (b) devices of heating the solid domestic waste with the use of its own pyrolytic gas, where pyrolytic installation comprises the tubular pyrolytic camera, perforated by slit openings, which is placed in the tubular chamber of the collection of pyrolytic gas, and the latter is placed in the external tubular chamber of external heating; heating of solid domestic waste for guaranteeing their thermochemical decomposition is realized both due to the supply of the hot flue gases, which come from the gas burner, into the internal cavity of tubular pyrolytic camera, and due to the supply of hot exhaust gases from the gas-turbine electrical apparatus to the cavity between the tubular pyrolytic camera and the external tubular chamber, covered with thermal insulation layer.
NOVELTY - The preparation involves passing a heat transfer medium through the second passageway of a heat exchanger (170). Heat is transferred from a hot flue gas passing through the first passageway of the heat exchanger to produce a heated heat transfer medium. The flue gas exiting the heat exchanger is then vented. The heat transfer medium is passed to first and second torrefaction zones (120,130) to provide at least a fraction of the heat of reaction for each torrefaction zone.    USE - Preparation of biomass feedstream for gasification for production of syngas.    ADVANTAGE - Allows utilization of biomass gasification processes and equipment that are economically practical for use at medium-scale to small-scale installations, including direct sources of biomass such as agricultural operations in farms and factories in which biomass materials are starting materials and/or by-products.    DESCRIPTION OF DRAWING(S) - The drawing shows the simplified flow diagram of the preparation of biomass feedstream for gasification.    Milling zone (100)    Feed bin (110)    First and second torrefaction zones (120,130)    Knockout drum (150)    Heat exchanger (170)
NOVELTY - The device has heating chamber that is enclosed in thermal insulation chassis. Heat exchanger is provided to cool ashes or heat heat-transfer agent for heating or supplying hot water. The heating chamber is provided with upper low-temperature section in form of electrical resistance winding for heating of biomass to 450-600C and lower high-temperature section in form of electrical heating direct furnace for heating of biomass to 950-1000C. Tubular channels are arranged in internal space of retort for output from device of conversion gaseous products from retort.    USE - Device for thermal conversion of granulated biomass into carbon mono-oxide and hydrogen.
NOVELTY - The method involves providing an injection molding kernel (13), on which an interconnector material (14) and an inner-side electrode (11) are applied, where the kernel is made of plastic material. The injection molding kernel is placed in injection molds (25a, 25b). An electrolyte-mass (10a) is injection-molded for formation of an electrolyte body (10). The injection molding kernel is removed according to a type of a casting method such as a thermal method and fusion nuclear technology. The thermal method is implemented by burning of plastic material.    USE - Method for manufacturing a solid oxide fuel cell (claimed).    ADVANTAGE - The method enables manufacturing an electrolyte body, electrodes that are necessary in inner-and/or outer sides of the electrolyte body and inter-connector layers in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid oxide fuel cell that is manufactured by the method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross sectional view of a solid oxide fuel cell that is manufactured by the method.    Electrolyte body (10)    Electrolyte-mass (10a)    Electrode (11)    Injection molding kernel (13)    Interconnector material (14)    Injection molds (25a, 25b)
NOVELTY - A hydrogen producing apparatus (1) has a reaction chamber (3) in which a hydrogen producing substance (5) which reacts with solution capable of reacting and producing hydrogen is accommodated, a liquid feeding unit (6) provided in chamber for feeding the solution to hydrogen producing substance, and a discharging unit (7) for discharging hydrogen produced by chamber, connected to hydrogen supply portion. The substance (5) is interrupted from atmosphere of chamber, with partition component (8), and hydrogen produced in reaction chamber is circulated to reaction chamber.    USE - Hydrogen producing apparatus is used for fuel cell system (claimed).    ADVANTAGE - The hydrogen producing substance is reliably interrupted from atmosphere of reaction chamber, and hydrogen is circulated. The partition component is easily destroyed and has simple structure. The unused hydrogen producing substance does not contact external moisture content.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of hydrogen producing apparatus.    Hydrogen producing apparatus (1)    Reaction container (2)    Reaction chamber (3)    Holding component (4)    Hydrogen producing substance (5)    Liquid feeding unit (6)    Discharging unit (7)    Partition component (8)
NOVELTY - A high-pressure hydrogen manufacturing system (2) has a water electrolysis cell (10), a storage tank (12) for storing oxygen gas emitted from cell, and storage tank (11) for storing hydrogen gas emitted from cell. A deformable pressure absorption material (60,80) enclosed with predetermined gas is provided in storage tanks (11,12).    USE - System is used for manufacturing high-pressure hydrogen used as fuel for fuel cell.    ADVANTAGE - The generation of differential pressure is prevented. The oxygen side storage tank and hydrogen side storage tank have reduced size due to reduced size of air layer volume formed in storage tanks.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of high-pressure hydrogen manufacturing system.    High-pressure hydrogen manufacturing system (2)    Electrolysis cell (10)    Hydrogen side storage tank (11)    Oxygen side storage tank (12)    Pressure absorption materials (60,80)
NOVELTY - Producing biogas by fermentation of pressed juice produced from biomass in a bioreactor, comprises: (a) introducing the pressed juice in a bioreactor (10), which exhibits a filling material-packed bed; (b) withdrawing the fermented pressed juice from the bioreactor; (c) removing a partial amount (A, B, C, D) of the filling material from the surface of the bioreactor; (d) supplying the partial amount of the filling material in to the surface of the bioreactor, in which the pressed juice is introduced into the bioreactor; and (e) repeating the steps (c) and (d).    USE - The method is useful for producing biogas.    ADVANTAGE - The method avoids the mixing of the fermented and the fresh pressed juice, thus it increases the rate of degradation of the fermented substance for the production of biogas.    DETAILED DESCRIPTION - Producing biogas by fermentation of pressed juice produced from biomass in a bioreactor, comprises: (a) introducing the pressed juice in a bioreactor (10), which exhibits a filling material-packed bed made from many filling materials; (b) withdrawing the fermented pressed juice from the bioreactor; (c) removing a partial amount (A, B, C, D) of the filling material from the surface of the bioreactor, in which the fermented pressed juice is withdrawn from the bioreactor; (d) supplying the partial amount of filling material in to the surface of the bioreactor, in which the pressed juice is introduced into the bioreactor; and (e) repeating the steps (c) and (d). The fed partial amount of the filling materials are applied to that surface of the filling material-packed bed, which is set against the flow direction of the pressed juice in the bioreactor.    DESCRIPTION OF DRAWING(S) - The figure 3 shows a schematic process flow for the bioreactor (Drawing includes non-English language text).    Bioreactor (10)    Inlet (20)    Outlet (30)    Conveyor device (40)    Partial amount of the filling material (A, B, C, D)
NOVELTY - The method involves reforming a carbonaceous feedstock e.g. biomass, to produce synthesis gas comprising hydrogen and carbon monoxide. A portion of the synthesis gas is subjected to Fischer-Tropsch conversion such that a portion of the hydrogen and carbon monoxide is catalytically converted into product comprising liquid hydrocarbons. A Fischer-Tropsch tailgas comprising component e.g. carbon monoxide, hydrogen, methane and carbon dioxide, is separated from the product. A portion of the tailgas is combusted to provide a portion of heat for reforming additional carbonaceous feedstock.    USE - Method for producing liquid hydrocarbon from synthesis gas. Can also be used for ethanol, methanol and mixed alcohol.    ADVANTAGE - The method enables using renewable and sustainable carbonaceous materials for production of synthesis gas, sequestration of carbon dioxide in multiple ways and locations and reduction in the amount of waste for disposal and amount of waste tailgas, thus facilitating environment-friendly production of the synthesis gas conversion product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for production of conversion products from synthesis gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biorefinery for producing synthesis gas conversion products.    Feed handling and/or drying apparatus (200)    Mixing apparatus (300)    Reforming apparatus (400)    Steam generation apparatus (500)    Synthesis gas conversion apparatus (700)
NOVELTY - Liquid fuel composition comprises a hydrocarbon fuel and a wax crystal nucleator comprising an olefin block copolymer or a polymer with a melting temperature (Tm) greater than 100 and density of less than 0.90 g/cm3.    USE - The liquid fuel composition is useful as diesel fuel, jet fuel, heating oil, biofuel and biodiesel (claimed).    ADVANTAGE - The cost-effective liquid fuel composition have improved low temperature viscosity characteristics and performance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) modifying a low temperature flow characteristic of a liquid hydrocarbon, comprising adding one or more olefin block co-polymers to the liquid hydrocarbon; and    (2) a lubricating oil comprising a viscosity modifier, where the viscosity modifier comprises an olefin block copolymer, where the olefin block copolymer comprises 3 or more blocks having different compositions.
NOVELTY - The radiator has a water sleeve (7) i.e. rectangular shell, equipped with a power radiating device. A side of the water sleeve is equipped with a water path. The power radiating device is provided with a power inductor (1), a motor driving power device (2), an insulated-gate bipolar transistor power switch (6) and a control circuit board (3). A lead terminal of the power inductor is extended from the side of the water sleeve. The power inductor is mounted at bottom of the water sleeve. Water pipes (5) are respectively fixed at front and rear sides of the water sleeve.    USE - Electric conversion water cooling radiator for a fuel cell generating system.    ADVANTAGE - The radiator enables the water path to realize electric conversion and radiate a driver for high-power regenerative fuel cell generating system. The radiator is light and compact in structure. The power radiating device and the control circuit board are laid on ground, so that a space electromagnetic interference is reduced. The driving circuit is arranged close to the power device, so that the arrangement ensures reliability and responding speed of the power device. The radiator has high reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an electric conversion water cooling radiator.    Power inductor (1)    Motor driving power device (2)    Control circuit board (3)    Water pipes (5)    Insulated-gate bipolar transistor power switch (6)    Water sleeve (7)
NOVELTY - The system has fuel cell unit (1) for generating electricity through executing electrochemical reaction on fuel. A re-composing unit (2) re-composes natural gas, water and air into hydrogen-rich gas used as fuel. A mixing unit (3) mixes air with residual fuel from fuel cell unit, and combusting unit (4) combusts mixture from mixing unit. A heat-exchanging unit (5) executes heat-exchanging between air and exhaust from combusting unit. The heat-exchanging unit comprises ports for inletting air, expelling exhaust and sending hot air into fuel cell unit respectively.    USE - Solid oxide fuel cell for generating electricity by executing electrochemical reaction on fuel burning residual fuel.    ADVANTAGE - Since the heat-exchanging unit executes heat-exchanging between air and exhaust from combusting unit, the efficiency of solid oxide fuel cell system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of solid oxide fuel cell system.    Fuel cell unit (1)    Re-composing unit (2)    Mixing unit (3)    Combusting unit (4)    Heat-exchanging unit (5)
NOVELTY - Improving mid-temperature anaerobic digestion effect by mixed fermentation of sludge and maize straw comprises selecting common maize straw, crushing via a mechanical crusher, screening, weighing, soaking the maize straw powder into running water, putting into a constant temperature water bath pot for treating at 30 degrees C; mixing the pre-treated wet maize straw with sludge; and putting the mixture into a mid-temperature anaerobic digestion reactor for digestion.    USE - Process for improving mid-temperature anaerobic digestion effect in sewage treatment plant.    ADVANTAGE - The carbon/nitrogen ratio of the raw material for mid-temperature anaerobic digestion is proper. Gas yield is improved. Methane content in the generated gas is improved.
NOVELTY - A light oil composition has sulfur content of 10 ppm or less, flash point of 60 degrees C or more, carbon residue content of 0.03 %mass or less in 10% bottom oil, temperature difference of 95% distillation temperature and initial boiling point of 120 degrees C or more in distillation curve, polycyclic aromatic concentration of 6 volume% or less, and light oil oxidation parameter (X) of 0 or less, calculated by specific formula.    USE - Light oil composition is used for biodiesel fuel composition (claimed) for diesel engine.    ADVANTAGE - The light oil composition has excellent oxidation stability.    DETAILED DESCRIPTION - A light oil composition has sulfur content of 10 ppm or less, flash point of 60 degrees C or more, carbon residue content of 0.03 %mass or less in 10% bottom oil, temperature difference of 95% distillation temperature and initial boiling point of 120 degrees C or more in distillation curve, polycyclic aromatic concentration of 6 volume% or less, and light oil oxidation parameter (X) of 0 or less, calculated by the formula: X=0.064x IBP+0.08x T50-0.1 31x T95-0.035x PAH+9.66 (I), where IBP is initial boiling point (in degrees C) in distillation curve, T50 is 50% distillation temperature (in degrees C) in distillation curve, T95 is 95% distillation temperature (in degrees C) in distillation curve and PAH is polycyclic aromatic content (in volume%). An INDEPENDENT CLAIM is included for oxidation-stability determination method of light oil composition.
NOVELTY - Vortex, laminar flow and pulse flow anaerobic reactor comprises a tank body comprising an upper gas collecting cover (13) arranged on the middle of the tank body (3) and a lower gas collecting cover (15) arranged on the inner lower side, a return pipe (17) arranged on the middle of the lower gas collecting cover and water distributors (1) arranged on the bottom of the tank body to input sewage.    USE - The anaerobic reactor is useful for organic sewage treatment.    ADVANTAGE - The anaerobic reactor: improves the sewage treatment efficiency by increasing the sewage reaction speed; has rapid starting time and high loading capacity; is economical; produces methane and water, thus the device is environmental friendly; and overcomes the shortcoming of the existing upflow anaerobic sludge blanket reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the vortex, laminar flow and pulse flow anaerobe reactor.    Water distributor (1)    Middle of the tank body (3)    Upper gas collecting cover (13)    Lower gas collecting cover (15)    Return pipe (17)
NOVELTY - The fuel cell system has fuel gas supply system which supplies hydrogen as fuel gas with respect to fuel cell. The oxidant gas supply system supplies oxygen as oxidant gas with respect to fuel cell. The electric power is supplied to load apparatus, while performing temporary blocking of connection to load apparatus after increasing the supply of flow volume and pressure of hydrogen. The supply of electric power from fuel cell to load apparatus is restarted, when restoration of electric generating capacity of fuel cell is detected.    USE - Fuel cell system for recovering electric generating capacity of fuel cell.    ADVANTAGE - The fall of electric generating capacity is detected easily by detecting the negative cell voltage regardless of amount of oxygen supply. The fall of power supplied to the fuel cell system can be suppressed. The possibility of stopping the electric power supply to load apparatus can be prevented reliably. The deterioration of cathode side catalyst electrode layer can be suppressed. The abnormal electric potential produced by carbon oxidation of cathode side catalyst electrode layer can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow chart illustrating the process for controlling electric power generation of fuel cell system. (Drawing includes non-English language text)
NOVELTY - The flanged cylindrical object (100) has a main cylindrical portion having open ends. An oblong shaped collar (120) is formed in the outer periphery of the main cylindrical portion. The collar is formed between a center portion and a lower end of the main cylindrical portion. A scale (113) and an electrode insertion thin layer are formed in the main cylindrical portion.    USE - Flanged cylindrical object for microscale experiment kit (claimed) used in e.g. school for performing microscale experiment such as electrolysis of water and electrolysis of various electrolyte solutions e.g. sodium sulfate aqueous solution and copper chloride aqueous solution. Can also be used for conducting microscale experiments such as reaction between metal and metal ion, acid and base experiment, oxidation-reduction reaction and electrolysis of fulminating gas.    ADVANTAGE - The cylindrical object is fixed stably by mounting the collar in a cover and the microscale experiment is conducted successfully. The insertion of electrode in the object is performed easily with a small force. The short circuit between electrodes is prevented effectively and the student is able to conduct a microscale experiment simply. The generated gas volume is measured simply using the scale. The rotation of cylindrical object is prevented by the collar for enabling easier decipherment of the scale. The standardization and uniformity of the conducted experiment are achieved by fixing the electrode insertion position. The gas ratio is observed easily from the height of gas volume collected in the flanged cylindrical object.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microscale experiment kit.    DESCRIPTION OF DRAWING(S) - The drawing shows the top, front, side and bottom views of the flanged cylindrical object.    Flanged cylindrical object (100)    Connector (111)    Scale (113)    Insertion portion (117)    Collar (120)
NOVELTY - A skid-mounted case is internally provided with a gas storing bag whose gas outlet is connected with gas inlet of an air compressor through a gas amount control valve. The gas outlet of the compressor is connected with gas inlet of a desulfurizing tank whose gas outlet is connected with a gas inlet of carbon dioxide collection tank. The methane gas outlet of carbon dioxide collection tank is connected with a methane compression tank through a pressurizing pump. An automatic controller is respectively controlled with the gas compressor and the pressurizing pump.    USE - Low-pressure purifying device for skid-mounted biological gas with explosion proof effect for purifying marsh gas.    ADVANTAGE - The marsh gas can be collected, purified, compressed, stored and used safely and the space is saved. The device is provided with explosion proof function. The device can be optionally moved, detached and transported. The operation is simple and convenient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the low-pressure purifying device.
NOVELTY - The purifier has support base plate (2) that is connected to inner wall of device pipeline (3) by bolt (4). One end of a basalt fiber beam (1) is formed by binding the rubber tubes in thermal shrinkage manner and is mounted on a support plate base through quick connector (5) along the radial direction of device pipeline. Another end of the basalt fiber beam is arranged at the bottom side of the device pipeline.    USE - Purifier of sewage transmission pipeline.    ADVANTAGE - The purification process of sewage can be performed efficiently by forming film on the pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the purifier.    Basalt fiber beam (1)    Support base plate (2)    Device pipeline (3)    Bolt (4)
NOVELTY - The machine has a roller mould extruding device that is arranged below a feeding hopper. A resistive filament is arranged at the roller mould extruding device. The roller mould extruding device is matched with the pipe at one end of a pedestal bracket. An electrical motor and second belt wheel are arranged in the pipe. The first belt wheel is connected with the third belt wheel. A discharging hopper is arranged at the tail end of the pipe.    USE - Biomass fuel molding machine.    ADVANTAGE - The biomass fuel production is efficiency is improved, and environmental protection is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the biomass fuel molding machine.
NOVELTY - The machine has stand (2) which is arranged at upper portion of machine base (1). Stirring cylinder (3) is fixedly mounted at upper portion of stand. Cylinder main shaft is transversely mounted in middle portion of cylinder. Motor (4) and extruding machine are mounted on machine base. Material inlet is arranged at upper portion of machine and is interconnected to material outlet at lower portion of stirring cylinder via a material channel (5). Motor is respectively connected to stirring cylinder belt pulley (8) and extruding machine belt pulley via belts.    USE - Biomass fuel granulating machine used in agricultural region.    ADVANTAGE - The rationally designed machine is compact, easy and simple to handle. The manufacturing cost of the machine is low. The machine is especially suitable for small-scale biomass fuel granulating work of various agricultural regions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel granulating machine.    Machine base (1)    Stand (2)    Stirring cylinder (3)    Motor (4)    Material channel (5)    Stirring cylinder belt pulley (8)
NOVELTY - The dry distillation emulsifying device has a combined sludge intermediate storage part (200), a rear end exhaust pipe (210), a switching valve (115) equipped in a tank exhaust pipe (110) and an on-off valve equipped in the rear end exhaust pipe in order to be connected in the tank exhaust pipe of the dry distillation tank. The rear end exhaust pipe which is a chimney combined in the back-end of the sludge intermediate storage part (200) is provided.    USE - Dry distillation emulsifying device for facilitating exhaustion of sludge.    ADVANTAGE - Reduces the evacuation rate of sludge by ejecting after production. Improves operability since the temperature is discharged after the temperature of the sludge of the high temperature is lowered. Enhances temperature of the sludge intermediate storage part in which sludge is ejected and which is stored. Prevents adhesion of liquid sludge to the sludge intermediate storage part and the exhaustion of sludge is facilitated which further improves operability.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial illustration of the state where the sludge intermediate storage part is installed in the dry distillation emulsifying device.    Tank exhaust pipe (110)    Switching valve (115)    Intermediate storage part (200)    Sludge intermediate storage part (200)    Rear end exhaust pipe (210)
NOVELTY - The device has degrading digestion filter tank (1) whose top is provided with viewing hole (2). Two sides of upper portions of filter tank are water inlet (3) and outlet (4) respectively. The middle portion of tank is provided with filling layer (5). A water guide pipe (6) made of cement, plastic or metal is passed through filling layer and tank. The opening (7) at upper end of guide pipe is higher than liquid level and faced to viewing hole. The opening (8) at lower end of guide pipe is located under filling layer and connected with water outlet in horizontal direction.    USE - Sewage re-treatment device for septic tank.    ADVANTAGE - The sewage re-treatment device can be constructed at low-cost. The sewage of built septic tank can be post-treated, and the quality of the sewage can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sewage re-treatment device.    Degrading digestion filter tank (1)    Viewing hole (2)    Water inlet (3)    Water outlet (4)    Filling layer (5)    Water guide pipe (6)    Openings of water guide pipe (7,8)
NOVELTY - Collecting oily microalgae comprises: adding chitosan (2-30 mg/l)-lewis acid (3-9 mg/l) flocculant into an oily microalgae culturing solution, quickly mixing at a speed of 200-500 revolutions per minute for 1-5 minutes, then slowly mixing at a speed of 20-70 revolutions per minute for 20-40 minutes, allowing the solution to stand for some time, precipitating the microalgae culturing solution for 15-60 minutes, removing the suspension, pouring the microalgae flocculant, centrifuging and further dehydrating at 3000-5000 revolutions per minute to obtain microalgae mud.    USE - The method is useful for collecting oily microalgae.    ADVANTAGE - The method is simple and economical. The dehydration rate of the algae mud is more than 98%, and thus meets the production demand of the biofuel oil, and integrates the flocculant and the catalyst.
NOVELTY - Biogas generator part of a solar constant-temperature biogas generator comprises a tank wall made of a polystyrene foam thermal insulation material, and an organic glass fiber reinforced plastic material with water resistance and corrosion resistance and capable of increasing the strength of the biogas generator is adhered to the inner wall and the outer wall.    USE - Used as a biogas generator part of a solar constant-temperature biogas generator.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a solar heat collecting and heating part of a solar constant-temperature biogas generator, where the hot water heated by a solar heat collector is stored in a solar hot water insulation water box, when the biogas slurry in the biogas generator lowers to 53 degrees C and is needed to be heated, a temperature control box generates an operating signal for making a circulating pump start working, the hot water is used for heating the biogas generator by a radiating pipe under the action of the circulating pump, and the temperature control box generates a signal for making the circulating pump stop working, when the temperature in the biogas generator reaches a set value of 55 degrees C; and    (2) working condition of a yard sewage pump of a solar high-temperature biogas generator, where the sewage pump is arranged in a digestion tank, the excrement is pumped into the bottom of the biogas generator from the digestion tank, and the excrement is stirred in the process of pumping into the biogas generator for preventing separation of the biogas slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biogas generator part of a solar constant-temperature biogas generator.
NOVELTY - Active polypeptide with endoglucanase, comprising fully defined 336 amino acids (SEQ ID NO:2) (I), as given in the specification and located at 25-336th position, is new.    USE - The polypeptide is useful for degrading: trisaccharide substrate methylumbelliferone-cellobiose (claimed); and cellulose in e.g. filter paper and cellotriose, cellulose bioconversion, chemical industry, textile industry, food industry, biofuel, feed additive and medicine industry.    ADVANTAGE - The specific activity of the polypeptide which uses sodium carboxymethylcellulose as the substrate reaches up to 158.8 U/mg.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a gene encoding the polypeptide, where the nucleotide coding sequence contains the DNA sequence located at the position No.72-1008 of fully defined 1008 nucleotides (SEQ ID NO:1), as given in the specification; and    (2) preparing the polypeptide.
NOVELTY - The apparatus has dry sludge particle conveyor which is arranged between discharging opening of sludge drier and feeding opening of mixer. Oversize combustible substance conveying machine is arranged between discharging opening of garbage disposal apparatus and feeding opening of oversize substance crusher. Combustible particle conveyor is arranged between discharging opening of crusher and feeding opening of mixer. Straw agricultural waste crushing section conveyor is arranged between discharging opening of straw waste crusher and feeding opening of mixer.    USE - Apparatus for producing composite solid waste derived fuel for cement plant, power generation plant and garbage disposal plant.    ADVANTAGE - The composite solid waste derived fuel can be produced easily without polluting environment by sludge and garbage.    DETAILED DESCRIPTION - Mixed material conveying machine is arranged between discharging opening of mixer and feeding opening of forming machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for producing composite solid waste derived fuel.
NOVELTY - The device has casing whose top portion is provided with water inlet. A bottom portion of water box is provided with occlusion connector. A top cover is provided with ozone discharging pipe and water feeding opening. An ozone water discharging opening is formed in water box. A mixer container is provided in gas-liquid mixer, for mixing ozone and water. A gas liquid separator is provided with separator container. The power supply anode is connected with anode of electrolysis unit. The power supply cathode is connected with cathode of electrolysis unit.    USE - Water electrolysis device.    ADVANTAGE - A water electrolysis device having simpler structure can be provided at low energy consumption. Cost of water electrolysis device can be reduced.    DETAILED DESCRIPTION - The lower portion of casing is provided with anode titanium power supplying hole plate, beta lead dioxide (PbO2) anode catalytic plate, solid polyelectrolyte membrane, cathode catalytic plate, cathode titanium power supplying hole plate, and cathode water collecting groove. The cathode water collecting groove is provided with a hydrogen gas water discharging pipe.The top portion of water box is provided with top cover.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the water electrolysis device.
NOVELTY - The lamination sheet manufacturing method involves forming green sheets (1,2) using doctor blade method from slurry containing powder, binder, and solvent. A green-sheet laminated body is formed by stacking the green sheets, and vacuum-packed. Hot-pressing is performed to the vacuum-packed green-sheet laminated body.    USE - Method of manufacturing lamination sheet use in producing fuel cell (claimed).    ADVANTAGE - Delamination of the lamination sheet is restrained by performing hot-pressing.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the hot press apparatus.    Hot press boards (4a,4b)    Pressurization syringe (5)    Heating chamber (6)    Mount frame (10)
NOVELTY - A fuel additive in the engine fuel of petrol- or diesel-fuelled engines for reducing the emission of harmful substances, comprises mixture of isoalkanes in liquid state and synthetic motor oil.    USE - In the engine fuel of petrol- and diesel-fuelled engines for reducing the emission of harmful substances (claimed); and in biodiesel fuels, where the harmful substances are nitrogen oxides, carbon monoxide, and hydrocarbon derivatives.    ADVANTAGE - The fuel additive reduces the emission of harmful substances such as nitrogen oxides, carbon monoxide, and hydrocarbon derivatives; improves the energy efficiency of engines; increases the service life of the engines; reduces fuel consumption; and shows additional advantage of cleaning and maintaining the injector system and the exhaust system.
NOVELTY - Light-colored glycerol purifying involves performing physical adsorption and evaporation of light-colored glycerol. The light-colored glycerol is acidified by using acetone i.e. propanone, where propanone is treated with glycerol to obtain 2,2-dimethyl-((1,3)-dioxolan-4-yl)-methanol. 2,2-Dimethyl-((1,3)-dioxolan-4-yl)-methanol is treated with propanone to obtain a product. Water and acid are added into the obtained product for purifying to obtain the finished product.    USE - Method for purifying light-colored glycerol.    ADVANTAGE - The method enables to purify the light-colored glycerol with high degree of purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the light-colored glycerol purifying method. (Drawing includes non-English language text).
NOVELTY - The stove has a stove chamber (12) whose upper part is provided with a long-neck cracking cylinder (3) and a combustion chamber (1) that are vertically connected with each other in through manner. An internal side or external side of the chamber is provided with a fire keeping device (11). A side of a middle-lower part of a stove body is provided with a feeding hopper (6) or a feeding opening connected with the chamber. A secondary wind inlet chamber (10) and a secondary wind inlet preheating chamber (13) are arranged in the body. The cracking cylinder is a round cylinder.    USE - Biomass low-carbon cooking-warming stove.    ADVANTAGE - The stove avoids blocking of pipeline or stove hole due to condensation and settlement and has better adequate combustion. The stove effectively avoids tar and condensed water pollution, improves heating efficiency, and avoids smoke when the material is fed by opening a cover. The stove ensures that fire cannot be extinguished when fine material is added with insufficient oxygen, saves energy, and reduces carbon emission to make low-carbon life.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass low-carbon cooking-warming stove.    Combustion chamber (1)    Long-neck cracking cylinder (3)    Feeding hopper (6)    Secondary wind inlet chamber (10)    Fire keeping device (11)    Stove chamber (12)    Secondary wind inlet preheating chamber (13)
NOVELTY - The box has a cylinder whose upper part is provided with a sealing cover. A tamping rod passes through the sealing cover. A rubber sealing sleeve is provided at a joint of the tamping rod and the sealing cover. A branch is arranged on the tamping rod at one end in the cylinder. An upper part of the tamping rod is provided with a handle.    USE - Combustion box for a straw gasification furnace.    ADVANTAGE - The box prevents combustible gas in the cylinder from flowing out due to opening of the sealing cover and charging and tamping of materials in an inner side of the cover, thus ensuring that combustible gas generated in the cylinder enters a cooking range through an air outlet pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a combustion box.
NOVELTY - The device has a diffusion pipeline whose end is connected with a water seal device. An igniter is located on an outlet end of the diffusion pipeline. The water seal device comprises an outer cover that covers an upper part of a water storage container. A lower part of the outer cover is provided with multiple water holes. The outer cover is provided with a gas outlet port and a diffusion port. An outlet port of a combustible gas pipeline is located in a space enclosed by the water storage container and the outer cover. A pull rod is installed at top part of an inner cover.    USE - Biomass gas diffusion device for use in a biomass gasification reaction system (claimed).    ADVANTAGE - The device intends to instantly exhaust combustible biomass gas from a biomass gasification reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas diffusion device.
NOVELTY - The device has two adjacent liquid tanks (1,2) that are connected to each other. An anode (3) is placed in one tank and a cathode (4) is placed in other tank. The plates (6) are provided on the top of anode and cathode. A liquid-absorbent sheet (7) such as blotting paper, pulp sheet is provided between the plates. The liquid (8) such as wastewater is supplied to the tank and current (5) is applied to the tank for separating hydrogen, oxygen and waste slug from the wastewater.    USE - Hydrogen and oxygen generation device.    ADVANTAGE - The waste slug, hydrogen and oxygen can be efficiently separated from the wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen and oxygen generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen and oxygen generation device.    Liquid tanks (1,2)    Anode (3)    Cathode (4)    Current (5)    Plate (6)    Liquid-absorbent sheet (7)    Liquid (8)
NOVELTY - A proton conductive membrane has metal oxide film (110) comprising one or more through holes (111) and polymer (120) which fills one or more through holes.    USE - Proton conductive membrane is used for manufacturing fuel cell (both claimed) e.g. direct methanol fuel cell and proton exchange membrane fuel cell.    ADVANTAGE - The proton conductive membrane having high ion conductivity and stability is manufactured, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of proton conductive membrane;    (2) fuel cell; and    (3) manufacture of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the proton conductive membrane.    Metal oxide film (110)    Through hole (111)    Polymer (120)
NOVELTY - Biomass is fermented, to produce, organic acid which is then concentrated, to produce 30% or more of concentrated organic acid. The concentrated organic acid is fraction-distilled, to obtain organic acid.    USE - Production of organic acid e.g. volatile fatty acid from biomass used for fuel.    ADVANTAGE - The method efficiently provides organic acids from land-based, freshwater-based, marine or biodegradable organic-containing biomass by using high-density cell culture method.
NOVELTY - Zearalenone (ZEN)-detoxifying Bacillus licheniformis, where a sample of the Bacillus licheniformis has been deposited in the Food industry research and development institute of Taiwan with an accession number Bioresource collection and research center (BCRC) 910458, is new.    USE - The Bacillus licheniformis strain is useful for: detoxifying ZEN; and degrading xylan, carboxymethyl cellulose and skim milk (claimed). Test details are described but no results given.    ADVANTAGE - The Bacillus licheniformis CK1 strain exhibits: xylanase, cellulase and protease activities of 20% higher than those in the wild type Bacillus licheniformis; good ZEN-detoxifying ability; non-hemolytic and non-enterotoxin producing ability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) detoxifying ZEN, comprising using the Bacillus licheniformis; and    (2) a Bacillus licheniformis CK1, where a sample of the Bacillus licheniformis CK1 has been deposited in the Food industry research and development institute of Taiwan with an accession number BCRC 910458.
NOVELTY - Integrated process for preparing renewable hydrocarbons, comprises: (a) providing renewable isobutanol and renewable ethanol; (b) dehydrating the renewable isobutanol, thus forming a renewable butene mixture containing at least one renewable linear butene and renewable isobutene; (c) dehydrating the renewable ethanol, thus forming renewable ethylene; and (d) reacting at least a portion of the renewable butene mixture and at least a portion of the renewable ethylene to form at least one renewable 3-16C olefin.    USE - The process is useful for preparing renewable hydrocarbons e.g. fuel, fuel additive, propylene, benzene, toluene and xylene (all claimed), where the fuels include gasoline, jet fuels and/or diesel fuels.    ADVANTAGE - The processes: is flexible, simple, economical and eco-friendly; and provides highly purified product streams having well defined, predictable chemical compositions that adapts to different biomass feedstocks readily and flexibly, and requires less additional processing and/or energy to separate.
NOVELTY - Process for hydroliquefaction of lignocellulosic biomass or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose and/or lignin comprises: (a) forming a suspension of the lignocellulosic biomass particles in a solvent, preferably a hydrogen donor solvent; (b) first hydroconversion of the suspension in at least one reactor containing a bubbling bed catalyst; and (c) second hydroconversion of at least a part of the effluent obtained in the step (b) in at least one reactor containing a bubbling bed catalyst.    USE - The process is useful for hydroliquefaction of lignocellulosic biomass or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose and/or lignin to produce fuel bases.    ADVANTAGE - The process provide the fuel bases with good thermal stability, good physical and chemical property and with good quantity. The process is easy to implement.    DETAILED DESCRIPTION - Process for hydroliquefaction of lignocellulosic biomass or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose and/or lignin comprises: (a) forming a suspension of the lignocellulosic biomass particles or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose and/or lignin in a solvent, preferably a hydrogen donor solvent; (b) first hydroconversion of the suspension in at least one reactor containing a bubbling bed catalyst and operating at a temperature of 300-440 degrees C, at a total pressure of 15-25 MPa, at a hourly mass rate of 0.1-5 h-1 and a ratio of hydrogen/charge of 0.1-2 Nm3/kg; and (c) second hydroconversion of at least a part of the effluent obtained in the step (b) in at least one reactor containing a bubbling bed catalyst and operating at a temperature of 350-470 degrees C, at a total pressure of 15-25 MPa, at a hourly rate of 0.1-5 h-1 and a rate of hydrogen/charge of 0.1-2 Nm3/kg.
NOVELTY - Releasing carbon dioxide from a carbon dioxide-rich capture material involves: providing a carbon dioxide-rich capture material; providing a metal oxide; and releasing carbon dioxide by reacting the metal oxide with a fuel in the presence of the carbon dioxide-rich capture material to produce a carbon dioxide-deplete capture material, the metal and gaseous carbon dioxide.    USE - For capturing and releasing carbon dioxide (claimed).    ADVANTAGE - The oxygen is supplied to the fuel in the form of a metal oxide, and avoids the need to purify air to obtain oxygen, thus economical. In the method, CO2 capture material and metal/metal oxide move from one reactor to the next together, thus simplifies the number and extent of fluid transfer conduits and operational control systems/devices necessary, and avoids need of separate flow controllers and piping for the CO2 capture material and metal/metal oxide recycling loops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for carbon dioxide (CO2) capture and release comprising: a capture reactor for receiving and reacting CO2-deplete capture material and CO2-containing gas to form a CO2-rich capture material; an oxidizing reactor for receiving and oxidizing metal to form a metal oxide; and a release reactor in fluid communication with the oxidizing reactor for receipt of metal oxide and capture reactor for receipt of the CO2-rich capture material, the release reactor forming a reaction bed in which the metal oxide and a fuel are reacted to form a CO2-deplete capture material, a metal, and gaseous CO2.
NOVELTY - The device has an upper gas outlet (10) and a lower gas outlet (11) that is connected with a gas intake joint of a gas flow control valve (201). A vortex air distributor, an oxygen increasing hole of an infrared electric heating starter (12) and an oxygen increasing hole of a purifier gas mixing chamber are connected with an output end of a vortex oxygen control valve (301). An input end of the vortex oxygen control valve is connected with a fan (501). Dolomite and calcite or haycite materials are placed in a cylinder type screen.    USE - Purification device for biomass gasification gas flow in an industry.    ADVANTAGE - The device improves reactive temperature of a gasification furnace to 1300-1600 degree centigrade in an oxidation cylinder, a reduction cylinder and a pyrolysis cylinder, and increases intensity of the gasification. The device quickly separates water in combustible gas of the biomass so as to provide gas with better quality. The device utilizes a screen type catalytic pyrolysis device to greatly reduce oil tar in combustible gas and waste water, thus reducing environmental pollution and having high production efficiency. The device utilizes a gas purifier for eliminating the oil tar, water and ash in the gas so as to improve calorific value of the gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a purification device.    Upper gas outlet (10)    Lower gas outlet (11)    Infrared electric heating starter (12)    Oil water vapor filtering separator (40)    Gas flow control valve (201)    Vortex oxygen control valve (301)    Fan (501)
NOVELTY - The furnace has a furnace body (2) whose lower part is provided with a combustion chamber (3) with an air inlet (4). An upper part of the furnace body is provided with a combusting and heating dry distillation chamber (6). An upper end of the dry distillation chamber is provided with a furnace cover (8). A furnace wall on an upper end of the combustion chamber is provided with an inverted closed conical tube (5). A furnace wall on a lower end of the dry distillation chamber is provided with another inverted closed conical tube (7) welded with the former inverted closed conical tube.    USE - Up-drawing fixed bed biomass gasification furnace.    ADVANTAGE - The furnace is simple and compact in structure and convenient to manufacture. The furnace can burn biomass fuel completely, and has better burning effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an up-drawing fixed bed biomass gasification furnace.    Furnace body (2)    Combustion chamber (3)    Air inlet (4)    Inverted closed conical tubes (5, 7)    Combusting and heating dry distillation chamber (6)    Furnace cover (8)
NOVELTY - The device has a heat tube exchanger (4) whose end is connected to a smoke inlet tube (5). The smoke inlet tube of the heat tube exchanger is connected to a wind inlet of a whirlwind dirt catcher (6). A water inlet tube (7) is connected to a water inlet of the heat tube exchanger. A water outlet of the heat tube exchanger is connected to an end of a steam tube (8). Another end of the steam tube is connected to a steam inlet (9) on a lower part of a furnace body (1).    USE - External heat tube exchanger device for a biomass gasification furnace.    ADVANTAGE - The device is simple and compact in structure and convenient to manufacture. The biomass fuel of the device can be effectively used for generating combustible gas. The device saves energy and reduces emission of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an external heat tube exchanger device.    Furnace body (1)    Heat tube exchangers (4)    Smoke inlet tube (5)    Whirlwind dirt catcher (6)    Water inlet tube (7)    Steam tube (8)    Steam inlet (9)
NOVELTY - The device has a water pipe (4) connected with a water inlet of a steam generator (3). A steam outlet of the generator is connected with an end of a steam pipe (5). Another end of the steam pipe is connected with an inlet at a lower end of a biomass gasification furnace (12). A fan (6) is connected with an end of a pipe (7) that is connected with a gas inlet of a gas pre-heater (8). A gas outlet of the gas pre-heater is connected with an end of a gas inlet pipe (10). Another end of the gas inlet pipe is connected with the inlet at the lower end of the biomass gasification furnace.    USE - Tail gas heat-exchange heating device for a biomass gas power generation unit of a biomass gasification furnace.    ADVANTAGE - The device is simple and compact in structure, and convenient to manufacture. The device efficiently utilizes biomass fuel to generate combustible gas, completely utilizes exhaust gas, saves energy, and reduces emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tail gas heat-exchange heating device.    Steam generator (3)    Water pipe (4)    Steam pipe (5)    Fan (6)    Pipe (7)    Gas pre-heater (8)    Gas inlet pipe (10)    Biomass gasification furnace (12)
NOVELTY - A mixed fluid supply pipe (35) supplies a mixed fluid to several separation membrane units (31-33). A separation fluid discharge pipe (37) discharges the separation fluid separated in the separation membrane units and respectively connected to the separation membrane units. A residual discharge pipe (39) respectively connected to separation membrane units, discharges the remainder fluid that is not separated in separation membrane units. The valves (41) are fitted in the mixed fluid supply pipe, separation fluid discharge pipe and residual discharge pipe.    USE - Separation membrane apparatus used for dehydrating concentration of water containing alcohol e.g. ethanol. Can also be used in natural gas separation, isomer resolution in petroleum plant, purge gas separation in ammonia-synthesis plant, oxygen separation in medical device, foodstuff industry and chemical processing plant.    ADVANTAGE - A separation membrane unit can be exchanged in the state of continuing operation of the separation membrane apparatus even when a failure arises in one separation membrane unit, and the failure can be corrected without stopping the apparatus. Since the mixed fluid flows into the inner surface of support pipe, the separation membrane units can improve the separation efficiency of mixed fluid.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view showing the connection state of three separation membrane units in the separation membrane apparatus. (Drawing includes non-English language text)    Separation membrane units (31-33)    Mixed fluid supply pipe (35)    Separation fluid discharge pipe (37)    Residual discharge pipe (39)    Valve (41)
NOVELTY - Wiping off treatment material comprises (a) fluid absorbing material capable of absorbing liquid with respect to solvent, where the fluid absorbing material is capable of dissolving high melting explosive (HMX), and (b) monoclonal antibody capable of binding with HMX, where the monoclonal antibody is immobilized in the fluid absorbing material. The chemical name of the HMX is octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine.    USE - The treatment material is useful for wiping off removal of organic nitric acid type explosive substances, preferably HMX (claimed).    ADVANTAGE - The treatment material removes organic nitric acid type explosive substances completely.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of wiping off removal of organic nitric acid type explosive substance, which involves dissolving solid powder of HMX in the solvent, adding the obtained solution to fluid absorption material, and forming a complex of HMX and monoclonal antibody using antigen-antibody reaction.
NOVELTY - Fertilizer composition comprises (in wt.%) an organic substance (31.34-32.40), an inorganic fertilizer (64.46-65.34) and microelements (2.93-3.88).    USE - The fertilizer composition is useful for flue-cured tobacco.    ADVANTAGE - The fertilizer composition: meets the requirements represented by China tobacco 103 in Luzhou tobacco district and hence the fertilizer is suitable for the flue-cured tobacco variety; increases the yield and improves the quality of the tobacco; increases the soil temperature, improves the soil and increases both production and income of the tobacco; reduces environmental pollution from fertilizer erosion; after being applied into the soil, rapidly activates beneficial microorganisms in the soil, enables them to breed rapidly and changes un-absorbable substances of the flue-cured tobacco to absorbable nutrients; and has persistent fertilizing effect.
NOVELTY - Solid farmyard flower fertilizer comprises dry bean residue, chicken manure and plant (fallen leaf) humus soil. The fertilizer is prepared by mixing uniformly dry bean residues (25-35%), dry chicken manure (15-25%), plant (fallen leaf) humus soil (35-50%) and fermentation agent (3-5%), adding water at 20-50 degrees C and air humidity of 60-80%, forming deposit, covering the mixture by a plastic film, fermenting for 48-72 hours, and spreading for natural drying.    USE - Used as solid farmyard flower fertilizer.    ADVANTAGE - The fertilizer utilizes easily available raw materials of low cost.
NOVELTY - The machine has a frame, decelerator, bearing element, large disc, shifting disc base, pressing cover, bracket, mold sleeve, pressing wheel, pressing wheel shaft, distributor, funnel, motor, heating coil and a discharging opening. The heating coils are arranged at sides of large disc.    USE - Double-disc biomass curing and forming machine.    ADVANTAGE - The power consumption of the machine can be reduced, and efficiency and yield of the machine can be improved. The temperature of the pressing disc can be controlled. Even line speed in production process can be attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the double-disc biomass curing and forming machine.
NOVELTY - The system has an air diffusion device which is located below level of a land treatment system and connected with a blower fan by a pipeline. The air is pressurized by an aeration fan and the pre-treated sewage is allowed into a soil treatment system and diffused to sewage system in the form of small bubble through air diffusion device.    USE - Manual pressurization oxygenation system for sewage land treatment.    ADVANTAGE - Good reoxygenation effect can be attained. High treatment efficiency and high mass transfer efficiency can be attained. The blockage problem of the land treatment system during operation can be avoided effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of manual pressurization oxygenation system.
NOVELTY - Anaerobic solid reactor comprises a reactor tank body (3) with cylinder form at the central part, frustum form at the upper part and inverted frustum form at the lower part. The upper part of tank body is equipped with a marsh gas discharging device and a draining device. The central part of tank body is equipped with a phase separating device (6), a current stabilizing device (7), a gas collecting and shell breaking device (4) and a reflux stirring and water in-letting device, and the lower part of tank body is equipped with a sludge discharging device (10).    USE - The anaerobic solid reactor is useful for generating marsh gas by using waste water and for the high solid content and high concentration organic wastewater treatment.    ADVANTAGE - The anaerobic solid reactor solves the problems of: influence of the sludge which cannot be mixed easily within the reactor, shortening of the sludge retention period and the crusting of surface sludge layer to the release of marsh gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic solid reactor.    Reactor tank body (3)    Shell breaking device (4)    Phase separating device (6)    Current stabilizing device (7)    Sludge discharging device (10)
NOVELTY - Anaerobic acidification can comprises a can body, where the upper part of the can body is provided with a gas collecting bonnet. An acidification region is equipped on the upper part of an inner cavity of the can body, and an anaerobic decomposing region is equipped on the lower part of the inner cavity of the can body. The top of the can body is provided with a feeding device. A material falling port of the feeding device is located at the top of the inner cavity of the can body, and a material distributing device is equipped below the material falling port.    USE - Used as an anaerobic acidification can.    ADVANTAGE - The acidification can: has short anaerobic period and high gas producing rate; and is simple in structure.    DETAILED DESCRIPTION - Anaerobic acidification can comprises a can body, where the upper part of the can body is provided with a gas collecting bonnet. An acidification region is equipped on the upper part of an inner cavity of the can body, and an anaerobic decomposing region is equipped on the lower part of the inner cavity of the can body. The top of the can body is provided with a feeding device. A material falling port of the feeding device is located at the top of the inner cavity of the can body. A material distributing device is equipped below the material falling port. A heavy object discharging device is equipped at the bottom of the anaerobic decomposing region. The anaerobic decomposing region has the lower part provided with sludge discharging device and the upper part provided with a floater discharging device. The can body is further equipped with a water inlet device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic acidification can.
NOVELTY - Sodium meta-aluminate and calcium hydroxide are added in water, reacted for 2-8 hours, cooled, filtered and washed to obtain solid calcium aluminate hydrate. The obtained solid calcium aluminate hydrate is calcined in muffler to obtain calcium-aluminum composite oxide solid base. The obtained calcium-aluminum composite oxide solid base is spread in the plasmid field, using air or nitrogen as medium and plasmid treatment is performed to obtain calcium-aluminum composite oxide solid base catalyst.    USE - Preparation of calcium-aluminum composite oxide solid catalyst used for manufacturing biodiesel (claimed).    ADVANTAGE - The method provides calcium-aluminum composite oxide solid catalyst, by a simple process. The biodiesel formed using calcium-aluminum composite oxide solid catalyst has excellent high activity and durability, and is environmentally-friendly.    DETAILED DESCRIPTION - A sodium meta-aluminate and calcium hydroxide are added in water in the molar ratio of 2:3, reacted at 30-100 degrees C for 2-8 hours, cooled, filtered and washed to obtain solid calcium aluminate hydrate. The obtained solid calcium aluminate hydrate is calcined in muffler at 200-1200 degrees C for 3-12 hours to obtain calcium-aluminum composite oxide solid base. The obtained calcium-aluminum composite oxide solid base is spread in the plasmid field, using air or nitrogen as medium and plasmid treatment is performed under working voltage of 10-45 V and regulating discharge clearance of 1-10 mm for 5-40 minutes to obtain calcium-aluminum composite oxide solid base catalyst.
NOVELTY - The hydrogen production has an electrolyzer which is connected to the water filling device, the hydrogen and oxygen outlets and to an electrolyte level sensor. The electrolyte level sensor is connected to the electro-valve, and is installed between the water filling device and electrolyzer. The water filling device is made in the form of tank with water. The bottom of the water filling device is placed above the electrolyte level sensor.    USE - Hydrogen production installation with electrolyte level control.
NOVELTY - A fuel ethanol is produced by saccharifying acorn powder and fermenting saccharified acorn powder with tannin tolerant yeast strain. The acorn powder saccharifying process includes two steps of liquefying high temperature amylase and saccharifying enzyme, starch, and cellulose in cellulose saccharified acorn powder.    USE - Method for producing fuel ethanol (claimed).    ADVANTAGE - The method takes the non-food acorn powder as raw material and directly ferments tannin tolerant ethanol fermented yeast to produce the fuel ethanol without the complex refining process of separating tannin. It simplifies the production process of the fuel ethanol, reduces the production cost, and improves the economy of the fuel ethanol in the production.
NOVELTY - The enhancer has feeding chamber (10) to which biogas generating pit material is sent to be fermented. A movable cover (17) is arranged above the methane storage chamber (9) to seal movable cover opening for ventilating and maintaining biogas generating pit (8). A fermentation chamber (12) is connected to water pressure chamber (14), and methane storage chamber is connected to methane storage cover (16). A solar photovoltaic system has a solar battery (1) connected to controller (3). An inverter (4) is connected to temperature raising device (7) in fermentation liquor.    USE - Enhancer for solar photovoltaic system mounted above biogas generating pit.    ADVANTAGE - The fermentation liquor in the biogas generating pit is uniformly stirred so as to uniformly stir the methane material and methane bacteria, to improve the digestion rate and to increase the production of methane. The temperature of fermentation liquor is increased properly, so that the production in the biogas generating pit is as high as growth and reproduction of the methane bacteria.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the enhancer for solar photovoltaic system.    Solar battery (1)    Controller (3)    Inverter (4)    Temperature raising device (7)    Biogas generating pit (8)    Methane storage chamber (9)    Feeding chamber (10)    Fermentation chamber (12)    Water pressure chamber (14)    Methane storage cover (16)    Movable cover (17)
NOVELTY - An alcohol is prepared by defoliating and cutting fresh sweet Sorghum stalks, adding water to ratio of 1:0.5, and pulping mixture to 60-100 meshes; adding 0.07-1.60 mol/L sulfuric acid, hydrolyzing at 100-150 degrees C for 1-2 hours, and saccharifying; neutralizing sweet Sorghum stalk slurry to obtain transparent sweet Sorghum juice; adding nutritive salt and activated yeast, fermenting at 26-30 degrees C, heating, warming, distilling, and collecting the distillate to obtain crude alcohol at 35-45 degrees C; and rectifying to further distill until alcohol concentration reaches not less than 95%.    USE - Method of preparing alcohol (claimed).    ADVANTAGE - The method can obtain more than 90 kg of 95% alcohol.
NOVELTY - Producing electricity by anaerobic fermentation of kitchen wastes, comprises: (a) sorting collected kitchen wastes and obtaining an utilizable kitchen wastes; (b) squeezing the utilizable kitchen wastes and separating into solid phase and liquid phase; (c) hydrating and removing impurities from solid phase and then mixing with liquid phase to perform anaerobic fermentation; and (d) performing anaerobic fermentation to obtain biogas and producing electricity to obtain the electric energy.    USE - The method is useful for producing electricity by anaerobic fermentation of kitchen wastes.    ADVANTAGE - The fermentation process is rapid, highly-efficient and stable, so that the natural anaerobic fermentation time is reduced, and biogas yield is improved. The method is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the process for carrying out the production of electricity by anaerobic fermentation of kitchen wastes (Drawing includes non-English language test).
NOVELTY - A soil firming agent comprises 50-60% sodium silicate, 2-5% absolute ethyl alcohol, 5-10% polyacrylamide, 5-10% hydroxymethyl cellulose, 8-15% sodium hydroxide, 8-15% potassium hydroxide, 2-5% magnesium hydroxide, 2-5% sodium fluorosilicate, 2-5% white alum, and 2-5% water reducer.    USE - A soil firming agent for directly processing soil into road deck (claimed).    ADVANTAGE - The product has low cost, simple construction, and excellent anti-fire and anti-earthquake performance is excellent, thus overcoming performance disadvantage of primary soil firming agent. It is regarded as deck, which satisfies demands of environment friendly, zoology, and power saving. The 7-day compressive strength can reach 5-10 MPa.    DETAILED DESCRIPTION - Soil firming agent for directly processing soil into road deck, comprises 50-60% sodium silicate, 2-5% absolute ethyl alcohol, 5-10% polyacrylamide, 5-10% hydroxymethyl cellulose, 8-15% sodium hydroxide, 8-15% potassium hydroxide, 2-5% magnesium hydroxide, 2-5% sodium fluorosilicate, 2-5% white alum, and 2-5% water reducer. It is processed by heating sodium silicate, absolute ethyl alcohol, polyacrylamide, hydroxymethyl cellulose, sodium hydroxide, potassium hydroxide, magnesium hydroxide, and sodium fluorosilicate to 80-100 degrees C in the reactor with a heater, a flow return condenser, and a stirrer. The liquid is cooled to 15-20 degrees C and added with 99% liquid sodium hydroxide, liquid magnesium hydroxide, liquid potassium hydroxide, and other raw materials. The mixture is stirred and reacted for 1-2 hours. Water reducer and practical high-speed composites are added and stirred under ambient temperature.
NOVELTY - Biological organic fertilizer for culturing red bayberries comprises the following components (in part by weight): animal excrement (40-60), fowl excrement (15-20), plant straw (15-30), EM strains (1-7), dough (2-5), seed herb (1-3), grass or leaf herb (1-3), and water soluble antibiotics (0.1-0.5).    USE - The biological organic fertilizer is used for culturing red bayberries (claimed).    ADVANTAGE - The organic fertilizer has reduced dosage, improved efficiency, expels injurious insects, kills ovum and parasite, prevents pollution of the red bayberries, and does not easily cause hardening of soil.
NOVELTY - Straw coal is produced by crushing straws, adding to carbonizing furnace and carbonizing for 30-50 minutes at 800-1200 degrees C under anaerobic state; cooling to 200-250 degrees C, adding loess, coal slime, sulfur fixing agent and paraffin and controlling weight ratios as follows: carbonized straws (100), loess (20-30), coal slime (20-30), sulfur fixing agent (0.1-0.7) and paraffin (0.1-0.7), and uniformly mixing; and sending to extruder, shaping and drying.    USE - Method for production of straw coal (claimed).    ADVANTAGE - The method makes full use of straws of crop, converts waste material into useful materials. The produced straw coal has good quality, high heat value of 5000 kilocalories, is safe, has no pollution, and exhibits energy consumption and environment protection.
NOVELTY - Activated sludge obtained during organosilicon wastewater treatment or activated sludge obtained by acclimating river water in downstream of 1000 m at drainage outlet of organosilicon wastewater is added into nutrient solution. Electric field of 8-28 mA is applied into nutrient solution and cultured. The nutrient solution contains dextrose, carbamide, ferric trichloride, dipotassium phosphate, monopotassium phosphate, microelement mother solution and water. Saturated activated carbon in organosilicon wastewater is added into nutrient solution and regenerated.    USE - Regeneration of activated carbon during organosilicon wastewater treatment.    ADVANTAGE - The regeneration of activated carbon is economically and quickly enabled without affecting environment and with reduced electrical energy.    DETAILED DESCRIPTION - Activated sludge obtained during organosilicon wastewater treatment or activated sludge obtained by acclimating river water in downstream of 1000 m at drainage outlet of organosilicon wastewater is added into nutrient solution. Electric field of 8-28 mA is applied into nutrient solution, cultured at 25-35 degrees C for 10-20 hours. The nutrient solution contains (in g) dextrose (1-5), carbamide (0.1-1), ferric trichloride (0.05-0.5), dipotassium phosphate (0.01-0.1), monopotassium phosphate (0.1-1), microelement mother solution (0.5-5 mL), and water (1000 ml), and has pH of 6.5-8.5. Saturated activated carbon in organosilicon wastewater is added into nutrient solution and regenerated at 25-40 degrees C for 8-16 hours to obtain regenerated activated carbon.
NOVELTY - Nanometer catalyst preparation involves using graphite oxide, chloroplatinic acid and ferric nitrate as reactant, where hydrazine hydrate is used as reducing agent. A reflux reaction is carried out under protection of nitrogen in water as reaction medium to prepare the nanometer catalyst.    USE - Method for preparing nanometer catalyst for fuel cell (claimed).    ADVANTAGE - The method enables to prepare the catalyst in a simple and cost-effective manner.
NOVELTY - Highly-clean gasoline comprises (in wt.%): carbinol etherified solution (8-12), aromatic hydrocarbons (35-40), 4-5C olefins (20-30) and 4-5C alkanes (20-30).    USE - Used as a highly-clean gasoline.    ADVANTAGE - The gasoline: has a simple and economical production, which manufactures gasoline with stable quality; utilizes by-products of factories; has good inflammability, high octane value and good anti-explosion performance; avoids the air pollution, since the gasoline does not comprise tetraethyl lead; reduces the hydrocarbons, carbon monoxide and nitric oxide content in tail gas of vehicle; maintains the fuel system of engine clean without accumulated carbon and mechanical abrasion, thus prolonging the service life of the vehicles; has high pulverization degree; burns the mixed air completely, which increases the power supply; and makes the vehicle to start easily with stable speed and good acceleration performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the highly-clean gasoline, comprising: adding carbinol etherified liquid, aromatic hydrocarbons, 4-5C olefins and 4-5C alkanes into a homogenizer and homogenizing.
NOVELTY - Preparing synthetic natural gas from straw gas comprises: e.g. (i) providing the straw gas in a compressor and pressurizing; (ii) filling the pressurized straw gas in a pre-heater and heating; (iii) synthesizing methane by introducing the straw gas in a carbon monoxide and hydrogen converter, and reacting in the presence of a nickel-based catalyst to obtain a converted mixture gas; (iv) cooling the converted mixture gas by a condenser; (v) filling the cooled converted mixture gas to obtain a mixture gas after gas-liquid separation; (vi) introducing the mixture gas in an adsorbing purifier.    USE - The synthetic natural gas is useful as energy source for an internal combustion engine or small gas turbine.    ADVANTAGE - The method improves the energy utilization efficiency of synthetic natural gas.    DETAILED DESCRIPTION - Preparing synthetic natural gas from straw gas comprises: (i) providing the straw gas in a compressor and pressurizing to 1-2 Mpa; (ii) filling the pressurized straw gas in a pre-heater, and heating to 300-320 degrees C; (iii) synthesizing methane by introducing the straw gas in a carbon monoxide and hydrogen converter, and reacting in the presence of a nickel-based catalyst to obtain the converted mixture gas containing main components as methane, carbon dioxide, water and impurities; (iv) cooling the converted mixture gas to 20-40 degrees C by a condenser to obtain a cooled converted mixture gas; (v) filling the cooled converted mixture gas to obtain a mixture gas after gas-liquid separation; (vi) introducing the mixture gas processed by the gas-liquid separator in an adsorbing purifier and removing the carbon dioxide, moisture, nitrogen, oxygen, carbon monoxide and impurities to obtain the synthetic natural gas with methane content greater than 95%.
NOVELTY - Device comprises a closed biogas tank comprising a feed port, a biogas outlet, a biogas liquid outlet, a residue outlet and a biogas circulating returning port. An ammonium water spraying decompression dephosphination device and a gas distribution station made of a desulfurizer filled with solid desulfurizing agent, an ammonium water circulating pump, a biogas tank residue and liquid circulating returning conveying pump, and a water sealing gas storage cabinet are matched.    USE - The device is useful for: producing biogas energy from waste organisms (claimed); and producing organic fertilizers for agriculture.    ADVANTAGE - The device: solves the problem of lack of natural gas supply; produces a large quantity of high-quality organic fertilizers for agriculture; converts wastes into wealth; and strengthens environmental protection and increases employment opportunities.    DETAILED DESCRIPTION - Device comprises a closed biogas tank as its main part, which is a ball (or a drum) made of reinforced concrete, capable of resisting the pressure of 1 kg/ sq.cm and comprising a feed port, a biogas outlet, a biogas liquid outlet, a residue outlet and a biogas circulating returning port. An ammonium water spraying decompression dephosphination device and a gas distribution station made of a desulfurizer filled with solid desulfurizing agent, an ammonium water circulating pump, a biogas tank residue and liquid circulating returning conveying pump, and a water sealing gas storage cabinet are matched.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for producing biogas energy from waste organisms.
NOVELTY - A low-carbon green clean petrol comprises (mass%) petroleum fuel (20-80), denatured alcohol fuel (10-75), and gasoline additive (1-10). The denatured alcohol fuel is prepared by catalytic reforming by a solid super-acid catalyst.    USE - A low-carbon green clean petrol.    ADVANTAGE - The low-carbon green clean petrol is stable in performance, strong in breakout force, easy for low temperature start, less energy consumption, clean and environment-friendly.
NOVELTY - Invention relates to biological treatment of waste water. The method for biological treatment of waste water with active sludge involves putting sludge suspension into anoxide, aerobic and anaerobic zones of the volume of the treated water in an aerotank. Further, the sludge suspension passes into a secondary settling tank where it is separated into purified water and thick active sludge. The anaerobic zone of the aerotank is merged with the residue fermentation process - obtaining volatile fatty acids, in which a portion of flocculi of active sludge drops to the bottom, thickens to concentration of about 40 g/l in several days and after the fermentation process, the residue is carried by the flow of liquid from the anaerobic zone.    USE - Chemistry.    ADVANTAGE - Deep removal of organic substances and biogenic elements - phosphorus and nitrogen from waste water.
NOVELTY - Composition contains organic binder and crushed waste wood. The organic binder used is fermented residue formed during anaerobic fermentation of organic animal wastes. Components are in the following ratio, wt %: waste wood 10-90, fermented residue - the rest.    USE - Chemistry.    ADVANTAGE - High environmental friendliness of the process of producing solid moulded fuel, broader capabilities of using animal wastes to produce moulded fuel and low financial expenses. 1 ex
NOVELTY - Recycling of tungsten carbide alloy comprises: (a) oxidizing the tungsten carbide alloy to obtain tungsten oxides and other metallic oxides; (b) grinding the tungsten oxides and other metallic oxides to obtain a powder; and (c) treating the powder with a carburizing mixture for reducing and carburizing the powdered tungsten oxides and other metallic oxides to obtain the purified tungsten carbide alloy powder.    USE - The method is used for recycling of tungsten carbide alloy (claimed).    ADVANTAGE - The method is cost effective and environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the method for recycling tungsten carbide alloy.
NOVELTY - A fuel cell (1) has an electrolytic membrane (101) pinchingly supported between a fuel electrode (102) and an oxidizing agent electrode (103), a fuel generating component (104) which discharges fuel to fuel electrode in planar shape, and an insulating layer (106) having fuel permeability, between fuel generating component and fuel electrode.    USE - Fuel cell.    ADVANTAGE - The fuel cell is compact and economical, and has high fuel efficiency and stability. The fall of output characteristics of fuel cell by variation in electromotive force is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of fuel cell.    Fuel cell (1)    Electrolytic membrane (101)    Fuel electrode (102)    Oxidizing agent electrode (103)    Fuel generating component (104)    Insulating layer (106)
NOVELTY - Producing syngas that reduces amount of carbon dioxide in a gaseous stream, comprises: maintaining a reaction chamber at 400-5000 degrees C and a pressure of greater than or equal to 1 bar; providing a carbonaceous material and water into the chamber; introducing a gaseous stream containing carbon dioxide to the chamber; and reacting carbonaceous material, water, carbon dioxide and reactants in the gaseous stream to reduce carbon dioxide to form a gas comprising carbon monoxide and hydrogen. The reacting step further results in none of carbonaceous material remaining as unreacted carbonaceous material.    USE - The process is useful for producing: syngas with reduced carbon dioxide content in the gaseous stream; and ethanol (claimed) as liquid fuels.    ADVANTAGE - The process: does not require the use of a catalyst, hence it is cost effective; and provides an overall reduction of carbon dioxide content present in gaseous streams exhausted or emitted from various power plants and types of industrial plants, including a cement plant.
NOVELTY - Producing hydrocarbons from algae comprises: culturing an alkenone-producing alga under a growth condition sufficient to produce alkenones within the alga; and converting the alkenones to hydrocarbons.    USE - The method is useful for producing hydrocarbons from algae, where the hydrocarbons are useful in liquid biofuel and gaseous biofuel (all claimed).    ADVANTAGE - The method: minimizes foreign species which would detrimentally affect yields of alkenones; and uses the algae cells, directly without first extracting the algae oil, for the production of biodiesel and green diesel, eliminating several costly steps for biodiesel and green diesel e.g. solvent extraction.
NOVELTY - Forming hydrogen storage structure involves providing a porous material (30) having micropores (33) and nanochannels (32), where the micropores have a size of less than 2 nm and volumetric ratio of larger than 0.2 cm3/g, and the nanochannels have width of less than 2.5 nm, and fractal networks formed of the nanochannels have fractal dimension closed to 3; oxidizing and etching the porous material; and forming metal particles (34) of diameter of less than 2 nm in the porous material.    USE - Forming hydrogen storage structure (claimed) useful in fuel-cell vehicles and portable electronics.    ADVANTAGE - The method constructs hydrogen storage structure with room-temperature hydrogen storage capability of almost 6 wt.%, which satisfies the on-board target criteria of US Department of Energy (DOE) in America by 2010. The oxidation treatment is used to increase the pore size, so that the metal particles can be homogenously dispersed into the pore structures of the template. Thus, the room-temperature hydrogen storage capacity of the structure is improved.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of hydrogen storage structure.    Hydrogen-absorbable porous material (30)    Mesopore channel (31)    Nanochannels (32)    Spherical or pillared micropores (33)    Metal nanoparticles (34)
NOVELTY - The method involves supplying fuel e.g. diesel, to a fuel reformer (110) for generating hydrogen. The hydrogen is supplied to a fuel cell stack (120) and an exhaust line (M2) for producing a mixture of the hydrogen and an exhaust, where the fuel cell stack converts the hydrogen into electricity. The mixture is supplied to a reduction unit (230) i.e. hydrogen selective catalytic reduction (H-SCR) unit, for converting nitrous oxide into nitrogen, where the reduction unit is placed on the exhaust line. Anode off gas from the fuel cell stack is supplied to the exhaust line.    USE - Method for reducing nitrous oxide emission from an internal combustion engine i.e. diesel engine, of a vehicle such as recreational vehicle and tractor trailer.    ADVANTAGE - The method enables utilizing the fuel cell stack to provide electrical power to the vehicle when the engine is not operated and utilizing a controller to control the reformate gas control valve and the anode off gas control valve, so that hydrogen is not supplied to the exhaust line, thus increasing quality and production efficiency of the fuel reformer to reduce nitrous oxide emission from the engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a nitrous oxide emission reduction system comprising a fuel reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a nitrous oxide emission reduction system for reducing nitrous oxide emission from a diesel engine.    Exhaust line (M2)    Fuel reformer (110)    Fuel cell stack (120)    Reduction unit (230)    Nitrous oxide emission reduction system (300)
NOVELTY - Removal of inorganic components from raw material for the production of clean materials, comprises: washing the raw material with aqueous solution that contains salt. The raw material is biomass, coal residues, wastes and/or sludges.    USE - The method is useful for the removal of inorganic components from raw material for the production of clean materials, where the raw material is biomass, coal residues, wastes and/or sludges (claimed), biomass of agro/forest/urban origin or even mixture of biomasses of different origin, from low quality coals comprising peat, lignite or sub-bituminous and/or bituminous coals, from urban and/or industrial origin residues and wastes and from sludges from sewage treatment plants, for the production of clean materials for thermochemical conversion aiming the production of energy and/or fuels, and the inorganic components are potassium, sodium, chlorine, sulfur and phosphorus and the heavy metals are zinc, mercury, copper, lead and chromium.    ADVANTAGE - The method: improves the properties of the raw materials and minimizes or even eliminates gas emissions and corrosion deposition and agglomeration problems that are caused during their thermochemical conversion; and provides low moisture, hydrophobic material, which is easy to be ground, and be mixed with various other materials at different ratios, easily applied in feeding systems used in commercial boilers for energy production and easily pelletized even combined with various other materials at different ratios at low energy consumption.
NOVELTY - An anaerobic reactor of horizontal flow fixed bed comprises a housing with a top cover. An air collecting pipe is arranged at the top of the housing. Multiple residue removing openings are formed at the bottom of the housing. Filter meshes are arranged at the discharging opening and the residue removing openings. Multiple guiding baffle plates and partition baffle plates are arranged inside the housing along the water flow direction at intervals. A fixed film carrier component is arranged between the partition baffle plates close to one side of feeding opening.    USE - Anaerobic reactor of horizontal flow fixed bed useful in anaerobic fermentation methane production of waste of livestock culture, organic wastewater in industry and urban sewage.    ADVANTAGE - Microorganisms are stably fixed on the carrier densely, thus ensuring stability and high efficiency of the air generation efficiency of the reactor. The reactor is heat resistant, acid resistant, alkali resistant, and good in molding performance.    DETAILED DESCRIPTION - An anaerobic reactor of horizontal flow fixed bed comprises a housing with a top cover. A feeding opening is formed below one end of the housing while a discharging opening is formed above the other end. An air collecting pipe is arranged at the top of the housing. Multiple residue removing openings are formed at the bottom of the housing. Filter meshes are arranged at the discharging opening and the residue removing openings. Multiple guiding baffle plates and partition baffle plates are arranged inside the housing along the water flow direction at intervals. A fixed film carrier component is arranged between the partition baffle plates close to one side of the feeding opening.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the anaerobic reactor of horizontal flow fixed bed.
NOVELTY - The preparation is formed from processed micro-biological fermentation of agricultural organic waste. In mass concentration in mg/l the preparation contains micro-elements of copper 3.0; cobalt 5.0; zinc 23.0, in a bonded form and in percent by mass of macro-elements of total nitrogen 4.0-7.0, ammonia nitrogen 2.5-4.0; phosphorus oxide 7.0-12.0 and potassium oxide 1.0-3.0 and 85-95 percent by mass of water. The biological and organic components are combined. The preparation can also contain in mg/l of humic acids, not less than 1000.0; gibberellins, not less than 17.0; auxins, not less than 2.5; cytokinins, not less than 200.0. The preparation also has fungicides and bactericides properties with mass concentration in mg of sulfur, not less than 0.5 and benzoic acid, not less than 29.0.    USE - In agriculture for production of bio-organic preparations for treatment of various plants from seed (tubers, bulbs) to growth in order to protect from disease and to increase yield.    ADVANTAGE - The process is highly effective and ecologically clean and production and labor costs are reduced.
NOVELTY - Semi-interpenetrating polymer network (I) comprising a linear thermoplastic polymer and a cross-linked network of a bismaleimide having a cardo group is new.    USE - (I) is useful in a membrane for: gas separation, preferably for separating carbon dioxide from other gases (which are nitrogen and/or methane); and upgrading biogas, upgrading natural gas and carbon dioxide capture from flue gas (all claimed).    ADVANTAGE - (I): has excellent gas separation properties; has increased selectivity and permeance of carbon dioxide over slower gases (nitrogen and methane), as it has specific interaction to carbon dioxide leading to facilitated transport of carbon dioxide; utilizes cost effective commercial polymers having exceptional thermal, chemical and mechanical stabilities, which endures the high temperatures and pressures prevalent in industrial applications; requires less cardo component in (I) for the same selectivity and permeance than in other cardo-based polymers, thus reduces cost; has significantly higher thermal stability and glass transition temperature than the pure thermoplastic polymer; and has significantly fewer defects and do not exhibit plasticization behavior. In (I): an increase in BMI-cardo compound concentration in (I) does not change the thermal stability and glass transition temperature appreciably; and there is no obvious phase separation between the BMI-cardo compound network and the thermoplastic polymer network.
NOVELTY - The installation comprises a furnace communicated with a pyrolytic chamber, which has an economizer that is connected by a steam pipeline with a serpentine section and situated in the furnace. An outline of adjustment with a pressure sensor is installed on the steam pipeline between the economizer and the serpentine section. An outline of adjustment with a temperature sensor is installed after the serpentine section.    USE - The installation is useful for pyrolysis of wood.
NOVELTY - The wetland includes a tank body comprising of a water collecting area, a mixed active medium area and a water distributing area from the bottom to top. The mixed active medium area includes a volcanic biological filter material. The water collecting area comprises a water collecting stone cage paved on the bottom of the tank body and a collector pipe penetrating through the water collecting stone cage.    USE - Volcanic biological filter material type constructed wetland.    ADVANTAGE - The volcanic biological filter material type constructed wetland allows the easy formation of a biofilm and is not easy to block. The wetland has good sewage treatment effect, and solves the problem that the treatment effect is low in the common wetland.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the volcanic biological filter material type constructed wetland.
NOVELTY - A recycled solid fuel comprises heat-mixed waste culture medium, discard resin and mushroom, mixed with a ferrule.    USE - A recycled solid fuel.    ADVANTAGE - Recycled solid fuel is obtained at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycle solid-fuel manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a recycled front view of the recycled solid fuel manufacturing apparatus.    Hopper (10)    Screw conveyer (20)    Conveyance path (22)    Steam discharge part (24)    Discharge port block (30)
NOVELTY - A raw material containing animal and vegetable fats is trans-esterified with lower alcohol using an alkali catalyst. The oil phase is washed with water, and water phase and oil phase are separated by filter separation. The separated oil phase is vacuum-distilled, and fatty acid lower alkyl ester is manufactured. The addition amount of water required for washing of oil phase is 5-20 parts mass with respect to 100 parts mass of oil phase.    USE - Manufacture of fatty acid lower alkyl ester used for biomass fuel.    ADVANTAGE - The fatty acid lower alkyl ester having high purity is manufactured at high yield.
NOVELTY - A sludge amount is decreased by alkali process which adds alkali to sludge and making sludge into alkaline, solubilization process which solubilizes sludge in state in which microorganisms are easy to degrade, and heat stirring process which directly carries out blow-in mixing of steam to sludge and heat-stirring sludge by predetermined pressure.    USE - Decrease of sludge amount.    ADVANTAGE - The method efficiently decreases amount of sludge. The adhesion of scale with respect to inner wall of solubilization apparatus and tube surface of sludge flow-path tube is suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) sludge amount decrease apparatus;    (2) biogas generation apparatus; and    (3) biogas generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the sludge amount decrease apparatus.    Sludge amount decrease apparatus (1)    Sludge source (2)    Sludge transfer apparatus (3)    Alkali supply tank (4)    Steam supply apparatus (5)
NOVELTY - The unit has a unit cell provided with an anode and a cathode. A hydrogen supply system supplies hydrogen to the anode of a fuel cell stack. A controller is provided with an air supply apparatus that supplies air to the cathode of the fuel cell stack. The air supply apparatus supplies hydrogen at different pressure to the anode of a voltage detector. The voltage detector detects open circuit voltage (OCV) of the unit cell and diagnoses whether malfunction is generated in the fuel cell stack.    USE - Fuel cell stack diagnosis system for use in an electric power system of a vehicle.    ADVANTAGE - The unit provides user convenience while repairing and exchanging the fuel cell stack with reliability, identifies the problem accurately in the location of the channel, prolongs the lifetime of the fuel cell stack, and presumes forecast time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for diagnosing a fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a method for diagnosing a fuel cell stack. '(Drawing includes non-English language text)'
NOVELTY - The method involves generating vibration in a discrete manifold (110) that is welded by using a manifold part. Frictional heat is generated on the discrete manifold. Fusion acid is supplied to connection point of the discrete manifold and fusion guide.    USE - Method for manufacturing a manifold for a fuel cell of a vehicle.    ADVANTAGE - The discrete manifold has excellent adhesive property, thus improving durability. The manifold avoids generation of foreign substance discharge according to driving time, and realizes individualization course during injection molding, so that turn around time can be shortened and mass productivity can be secured. The method enables improving the work environment, reducing the thickness, and improving the performance of a fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a manifold of a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating manifold manufacturing method.'(Drawing includes non-English language text)'    Discrete manifold (110)    Jig (120)
NOVELTY - Phosphate compounds, obtained by a process comprising reacting an insoluble phosphate source with an organic source, optionally in presence of a mineral acid or an organic acid, where the organic source is: (a) crude organic material having e.g. lignite, and peat; or (b) organic compounds extracted from the lignite, leonardite, peat, plant compost, lignosulfonates containing monovalent cations or algae, and have at least 10%, preferably at least 30% of free complexing functional groups, are new.    USE - The phosphate compounds are useful as a fertilizer. Tests details are described but no results given.    ADVANTAGE - The phosphate compound is more stable and simple to prepare.    DETAILED DESCRIPTION - Phosphate compounds, obtained by a process comprising reaction of an insoluble phosphate source with an organic source, optionally in the presence of a mineral acid or an organic acid, characterized in that organic source is constituted of: (a) crude organic material comprising lignite, leonardite, peat, plant composts, lignosulfonates containing no monovalent cations and algae, which is pretreated by an activation step for releasing at least 10%, preferably at least 30% of complexing functional groups present in the organic compounds; or (b) organic compounds extracted from the lignite, leonardite, peat, plant compost, lignosulfonates containing monovalent cations or algae, and have at least 10%, preferably at least 30% of free complexing functional groups, are new. An INDEPENDENT CLAIM is included for fertilizers containing the phosphate compounds
NOVELTY - Producing a fatty acid derivative (e.g. a fatty ester), comprises culturing a host cell in the presence of a carbon source, where the host cell is genetically engineered to overexpress a gene encoding a thioesterase, a gene encoding an acyl-CoA synthase, and a gene encoding an ester synthase, and the gene encoding the thioesterase and the gene encoding the acyl-CoA synthase are integrated into the genomic DNA of the host cell.    USE - The fatty acid derivative is useful as biofuel (claimed), which is useful as petroleum based fuels including transportation fuels (e.g. gasoline, diesel and jet fuel), heating fuels, and electricity-generating fuels.    ADVANTAGE - The method provides fatty acid derivative in an economical and energy-efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fatty acid derivative produced by the method;    (2) a genetically engineered microorganism comprising at least one of a gene encoding a thioesterase, a gene encoding an acyl-CoA synthase, and a gene encoding an ester synthase or an exogenous control sequence stably incorporated into the genomic DNA of the microorganism upstream of a gene encoding a thioesterase, and a gene encoding an acyl-CoA synthase, where the gene encoding the thioesterase and the gene encoding the acyl-CoA synthase are integrated into the genomic DNA of the microorganism, and the microorganism produces an increased level of a fatty ester relative to a wild-type microorganism; and    (3) a biofuel composition comprising the fatty acid derivative.
NOVELTY - The ion exchange vessel or bottle device comprises first and second ports for entry and exit of a feed fluid, and a strand (31, 32) of ion exchange material filling a region within the device to remove ions from the feed fluid.    USE - The ion exchange vessel or bottle device is useful in an exchange component of an electrodialysis device for treating an organic or biologically-derive fluid stream (all claimed).    ADVANTAGE - The ion exchange vessel or bottle device is easy-to-handle, has increased physical integrity, high dimensional flexibility, exchange capacity and durability, and is capable of efficiently treating the organic or biologically-derive fluid stream with high conductivity and good electrochemical and physical characteristics and without fouling or flow obstruction, and prevents the application of filled-cell constructions to treatment of organic or biologically-derived fluids.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an exchange component;    (2) a spacer for an electrodialysis device; and    (3) an electrodialysis device for treating an organic or biologically-derive fluid stream.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a spacer for a deionization device.    Anion exchange membrane (12)    Cation exchange membrane (14)    Strands (31, 32)    Flow cells. (100)
NOVELTY - Rifaximin in amorphous form having X-ray diffraction pattern as given in the specification, is new.    USE - For treating diarrhea caused by the bacterium Escherichia coli.    ADVANTAGE - The amorphous form of rifaximin is stable and has maximum solubility measurable in water. The higher solubility is an advantage for all pharmaceutical applications as a high solubility value enhances the drug bioavailability. The method enables to obtain stable rifaximin in amorphous form in a short time, without adding additional substances co-precipitating with rifaximin and with a very high yield. The method has low environmental impact, falling in the activity field of Green Chemistry, because the use of chemical solvents is not necessary. The amorphous forms obtained can be selected depending upon simple process parameters (energy and/or time) and it is possible to obtain exactly a specifically wished amorphous form. The amorphous forms of active compounds have a higher pharmacological activity; and the method allows obtaining stable amorphous forms in a short time. The amorphous form shows sensibly higher solubilities than the amorphous forms known up to now.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing rifaximin in amorphous form.
NOVELTY - A Microbacterium capable of using methane and deposited as CCTCC NO: M2010099, is new.    USE - The Microbacterium is used for manufacturing methane-absorbent organism, garbage treating agent, and a biological catalyst (all claimed). The microorganism is suitable as artificial source of methane.    ADVANTAGE - The Microbacterium has higher affinity to methane.
NOVELTY - Chryseobacterium capable of utilizing methane, with a preservation number of CCTCC No.M2010100, is new.    USE - The Chryseobacterium is useful for preparing a bio-absorbent of methane, a rubbish processing agent and a bio-catalyst (all claimed), and for artificial methane sources e.g. domestic waste landfills and rice fields.    ADVANTAGE - The Chryseobacterium: overcomes the low cell density of methane oxidizing bacteria, thus making the amplification culture of the cells easy and has high affinity to methane.
NOVELTY - The pigpen has walls built indoor at three sides. One side of the wall is provided with a fence (1) to form a colony house. Area of the house is 38-42 square meters, and distance between the fence and a front door is 100-160 cm. A feed trough (4) and a water trough are provided inside the house. A water dripper (6) is provided above the water trough. A backing layer (7) comprising a laminated chaff, saw dust, a rice bran and raw pig dung is provided on a ground in the house. A backing inlet-outlet is formed at bottom of the wall, where the wall is 50-110 cm high.    USE - Bed pigpen for fermenting pig excrement.    ADVANTAGE - The colony house is reasonable in structure, and the backing layer effectively ferments the pig excrement, so that the pigpen is clean, dry and suitable for the growth of pigs, and has better ventilation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a bed pigpen.    Fence (1)    Feed trough (4)    Water dripper (6)    Backing layer (7)    Ventilating fan (10)
NOVELTY - The process comprises converting the microalgae to carbon black by heating the algae in inert atmosphere, mixing the carbon black with auto-ignition substance, converting the carbon black to carbon nanotubes in a sealed chamber by subjecting the chamber to substance auto-ignition condition, and converting carbon rich waste to carbon nanotubes. The carbon rich waste consists of rubber, plastics, wood, jojoba shells and dry sewage. The carbon nanotubes are purified by dry or wet methods using ionic liquid and strong acids or oxidizing agents. The ionic liquid is a mixture of fatty acids.    USE - The process is useful for forming multiwall carbon nanotubes from microalgae, which is useful for production of biodiesel by converting organic molecules to lipids.    ADVANTAGE - The process is capable of efficiently and economically producing the carbon nanotubes with high purity and increased product yield and without any damage.    DETAILED DESCRIPTION - The process comprises converting the microalgae to carbon black by heating the algae in inert atmosphere, mixing the carbon black with auto-ignition substance, converting the carbon black to carbon nanotubes in a sealed chamber by subjecting the chamber to substance auto-ignition condition, and converting carbon rich waste to carbon nanotubes. The carbon rich waste consists of rubber, plastics, wood, jojoba shells and dry sewage. The carbon nanotubes are purified by dry or wet methods using ionic liquid and strong acids or oxidizing agents. The ionic liquid is a mixture of fatty acids and liquid at room temperature. The dry method uses heating the unpurified nanotubes to above 500 degrees C.    DESCRIPTION OF DRAWING(S) - The diagram shows scanning electron microscopic view of the formation of carbon nanotubes.
NOVELTY - 1,4-Butanediol is dehydrogenated under hydrogen atmosphere in presence of metallic oxide catalyst, to obtain gamma -butyrolactone. Then, gamma -butyrolactone is mixed with water and monomethylamine aqueous solution in a reactor, and then water is separated out from the reaction mixture after completion of the reaction, to obtain N-methyl pyrrolidone.    USE - Preparation of N-methyl pyrrolidone. Uses include but are not limited to polymer, semiconductor processing solvent, paint manufacturing solvent, metal surface-cleaning agent, pharmaceuticals, refining solvent and lithium battery-manufacturing solvent.    ADVANTAGE - The method efficiently provides N-methyl pyrrolidone which is environmentally friendly and halogen free in short period of time using simple process.
NOVELTY - The treatment system has a manure pit provided with a manure slurry electric pumping pipeline. The wall of a fermentation chamber is provided with an ordure conveying pipe connected with the electric pumping pipeline. The output end of the ordure conveying pipe is provided with a control valve and an electric control button arranged on the side of the output end. The electric control button can be operated to control the working circuit of the electric pumping pipeline.    USE - Treatment system for fermenting and conveying ordure from farm.    ADVANTAGE - Ensures convenient operation, and allows uniform laying of manure slurry in the fermentation chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a treatment system.
NOVELTY - The device (1) has a reactor (2) filled with a granular material (3) i.e. sand (5). A fluid supply system supplies fluid to the reactor for subjecting the granular material to fluidization in the reactor. An inlet of the reactor subjects the granular material in a fluidized bed. An outlet of the reactor subjects the granular material to gasification process. The supply system is provided outside the reactor. A recess is formed on the supply system and the reactor. The supply system is connected to a longitudinal axis of a sliding column. A cooling device cools the supply system.    USE - Gasification device for gasifying a granular material i.e. sand, in a biomass processing plant.    ADVANTAGE - The fluid supply system avoids contamination and pollution. The device is easy to maintain and clean, efficient, inexpensive and simple in structure, and has better heat exchanging effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for cleaning a fluid supply system of a gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gasification device.    Gasification device (1)    Reactor (2)    Granular material (3)    Air supply system (4)    Sand (5)
NOVELTY - A citron drug production increment fertilizer comprises (mass%) dry duck manure (10-16), dry cow manure (12-16), ammonium bicarbonate (12-14), nitrogenous fertilizer (10-12), potassium chloride (2-4), calcium magnesium phosphate fertilizer (10-12), peanut cake powder (6-8), wheat straw powder (2-4), corncob powder (8-10), calcium fertilizer (4-6), potash fertilizer (2-4), carbendazim (2-4) and neoprene (4-6).    USE - A citron drug production increment fertilizer.
NOVELTY - Pyrolytic device for directly converting straws into gasoline and diesel oil comprises screw feeder, pyrolytic reaction kettle with stirrer, two diffusion type cyclone separators, one of which is covered with water cooling jacket, sieve plate tower, bio-oil tank, steam-liquid separator, combustor, and pressure stabilizer. It is further provided with auxiliary devices such as drum dries and hammer crusher.    USE - Pyrolytic device for directly converting straws into gasoline and diesel oil.    ADVANTAGE - Waste plastic is used as additive to assist in the pyrolysis of straws of crops, reducing the pyrolysis temperature and improving the quality of pyrolytic oil (reaching the same quality of gasoline and diesel oil). The pyrolytic device is capable of completely converting biomass raw materials into high-quality biomass gasoline and diesel oil (yield=50%) through self-heating, efficient gas-solid separation, and direct condensation techniques. The biomass-derived gasoline and diesel oil can be burnt on an internal-combustion engine and can reduce emission of automobile exhaust. Bio-carbon with a yield of 30% and combustible gas with a yield of 20% obtained from the pyrolytic process can be used as heat source for pyrolysis; and the excess part can be burnt for power generation, where power generated can be used with commercial power grid to obtain extra economic benefits.
NOVELTY - Decomposition of water into hydrogen and oxygen mixed gas fuel comprises inputting water to steam generator to carry out vaporizing, and forming dry steam; sending dry steam to catalytic device, and using metal manganese catalyst in catalytic device to activate dry steam; sending activated dry steam to discharging device, and obtaining hydrogen and oxygen mixed gas with volume ratio of hydrogen to oxygen at 2:1 and small amount of dry steam which is not shocked electrically; and using steam and water separator to filter dry steam, and obtaining hydrogen and oxygen mixed gas.    USE - Method for decomposing water into hydrogen and oxygen mixed gas fuel (claimed).    ADVANTAGE - The produced fuel replaces fossil fuel, and the method saves energy and reduces discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the decomposition of water into hydrogen and oxygen mixed gas fuel.
NOVELTY - A rhodium-base catalyst comprises rhodium (Rh) active component (1-10 wt.%), and molecular sieve carrier of regular hexangular structure with hole diameter of molecular sieve of 1-30 mu m, hole volume of 1-5 cm3/g, and specific surface area of 100-1000 cm2/g.    USE - Rhodium-base catalyst used for preparing low carbon mixing alcohol by synthesis gas (claimed).    ADVANTAGE - The rhodium-base catalyst can improve switching rate of carbon monoxide and selectivity of the alcohol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of molecular sieve comprising dissolving three-section of polymer polyvinyl alcohol (3 g) in water (4.37mol), adding (mol) heteropoly acid (0.00021) and hydrochloric acid (0.0065), stirring at room temperature, adding ethyl orthosilicate (0.031 mol) to be stirred for 24 hours, switching to polymerization kettle, putting in drying case, setting temperature of drying case at 100 degrees C; and after 48h, cooling to room temperature, filtering, washing, drying, roasting solid in muffle furnace, with heating speed of 1 degrees C/minute, and temperature kept for 6 hours at 550 degrees C.
NOVELTY - Terrace type integrated vertical-flow forest wetland is obtained by (a) transforming a hillside land into terrace, and (b) constructing the terrace to terrace type integrated vertical-flow forest wetland (3), where plants and filler of terrace wetlands are same as artificial wetland, and upper and lower two stages of the terrace wetlands are in communication with forest surface flow wetland (4).    USE - The terrace type integrated vertical-flow forest wetland is useful for treating domestic sewage in rural areas.    ADVANTAGE - The vertical-flow forest wetland is cost-effective, convenient to use and simple, and treats domestic sewage with high purity and strong adaptability.    DETAILED DESCRIPTION - Terrace type integrated vertical-flow forest wetland is obtained by (a) transforming a hillside land into terrace, and (b) constructing the terrace to terrace type integrated vertical-flow forest wetland (3), where plants and filler of terrace wetlands are same as artificial wetland, and upper and lower two stages of the terrace wetlands are in communication with forest surface flow wetland (4). The sewage enters the forest surface flow wetland after being overflowed by the upward flow wetland (a) and upwards flow wetland (b) of the last stage of terrace wetland, and then enters the next stage of terrace wetland from the surface flow wetland for further treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of terrace type integrated vertical-flow forest wetland.    Collecting ditch (1)    Water dam (2)    Terrace type integrated vertical-flow forest wetland (3)    Forest surface flow wetland (4)    Waterproof vegetation (5)
NOVELTY - Deodorizing microbes in cow dung involves adding deodorization fungicide into wet cow dung in a mass ratio of 10-20%. The materials are mixed and kept for 3 days at 20-25 degrees C and then dried in presence of air.    USE - Method for deodorizing microbes in cow dung (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a special deodorization fungicide, which is prepared by utilizing distilled water, cow dung culturing substrate, bacteria culturing substrate, diluted bacteria liquid, mycetes and Saccharomyces.
NOVELTY - The system has a gas sensor array connected with an optical fiber Bragg grating demodulation device. The optical fiber Bragg grating demodulation device is connected with a transformer fault monitoring center. The gas sensor array is provided with multiple optical fibers Bragg gratings for absorbing carbon monoxide, carbon dioxide, hydrogen, ethylene, ethylene, methane or ethane. The optical fiber Bragg gratings are coated with a metal layer (1) i.e. gold layer. Another metal layer (2) i.e. Lanthanum pentanickel layer, is coated on the former metal layer.    USE - Transformer fault gas monitoring system.    ADVANTAGE - The optical fiber Bragg grating sensor has strong electromagnetic interference resistance, and can be used in environment with high electromagnetism. The system has high sensitivity and high resolution and is capable of monitoring multiple components of the transformer on line at the same time so as to greatly reduce the maintaining cost of the system and solve the problems of crossed sensitivity, slow oil-gas separation balance, and short service life of permeability film.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional perspective view of a transformer fault gas monitoring system.'(Drawing includes non-English language text)'    Metal layers (1, 2)
NOVELTY - The method involves removing the solvent from tar-contained solvent by a solvent regenerating kettle (6), and conveying the tar into a tar dissolving kettle (5). The solvent (12) is heated and is conveyed into an inlet and an outlet of the kettle (5). The tar-contained solvent (13) is regenerated by the kettle (6), and the fresh solvent is obtained from the kettle top for recycle. The tar is obtained from the kettle bottom, and the obtained tar is conveyed into the kettle (5) for dissolution, and the obtained tar solution is discharged into a tar solution collecting barrel (7).    USE - Tar dissolution method for extracting C4 hydrocarbon and C5 hydrocarbon.    ADVANTAGE - The method increases the operation temperature of the solvent to enlarge the boiling range of the solvent, and improves the fluidity of the tar in a pipe while achieving rational match between tar dissolution speed and solvent feed speed. The method employs an anchor agitator to reinforce the agitation effect and increase the dissolution speed. The method automatically switches on and off the valve when a waste rubber barrel is full, and improves the security and the humanization of the operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view representing the tar dissolution method.    Tar solvent heater (3)    Tar dissolving kettle (5)    Solvent regenerating kettle (6)    Tar solution collecting barrel (7)    Flow controls (8, 9)    Solvent (12)    Tar-contained solvent (13)
NOVELTY - Method of processing sewage and rainwater in village, involves (1) collecting sewage and rainwater channels from each house, (2) connecting the sewage and rainwater channels with main channel, (3) connecting outlet of the main channel to wetland or small reservoir, (4) planting livestock herbages on the wetland or in the small reservoir, (5) collecting a large-sized methane chamber for accumulating livestock manure and some straws and fermenting into methane, (6) and connecting the outlet with ditches filled with filter materials.    USE - The method is useful for processing sewage and rainwater in village.    ADVANTAGE - The method improves sanitary condition of the village, and living environment of farmers, and promotes health of people.    DETAILED DESCRIPTION - Method of processing sewage and rainwater in village, involves (1) collecting sewage and rainwater channels from each house, (2) connecting the sewage and rainwater channels with a main channel, (3) connecting an outlet of the main channel to a wetland or a small reservoir, (4) planting livestock herbages on the wetland or planting high-stem aquatic plants chosen from reed, duckweed or other plant absorbing pollutants in the small reservoir, (5) establishing a large-size methane chamber for accumulating livestock manure and some straws and fermenting into methane, using precipitated residue and liquid as fertilizer applied to fields to fertilize crops, and (6) arranging the outlet on the wetland as well as on the small reservoir, and connecting the outlet with ditches filled with filter materials, where the filter materials are sand and stone of different granularities.
NOVELTY - Treatment by precipitation of waste combustible and stacked composting materials as raw materials to obtain refuse derived fuel comprises: crushing the raw materials, preparing a stacking material body from the smashed materials, setting an air channel corresponding to the stacking material body, utilizing a ventilating device to pass through the air channel to ventilate the stacking material body, where the stacking composting materials generates heat to raise the temperature of the stacking body to reduce the water content of the material to satisfy the demands of the refuse derived fuel.    USE - The treatment method is useful for precipitating waste combustible and stacked composting materials as raw materials to obtain refuse derived fuel.    ADVANTAGE - The method: has less investment and operating cost, thus avoiding the wastage of resources, in comparison with the current thermal drying method.    DETAILED DESCRIPTION - Treatment by precipitation of waste combustible and stacked composting materials as raw materials to obtain refuse derived fuel comprises: crushing the raw materials, until the particle diameter of the material is lower than 80 mm, preparing a stacking material body from the smashed materials, setting an air channel corresponding to the stacking material body, utilizing a ventilating device to pass through the air channel to ventilate the stacking material body, where the ventilating condition that the stacking material body is placed for 7-10 days in a static way under 0.05-0.20 m3 of air/m3 of material per minute, where the stacking composting materials in the aerobic decomposing material of the microorganism contained in the stacking material body generates heat to raise the temperature of the stacking body to reduce the water content of the material from 40-50% to 15-25%, where the water content of the materials after being processed satisfies the demands of the refuse derived fuel.
NOVELTY - Repaglinide preparation involves preparing 4-carboxymethyl-2-ethyoxyl benzoate, (S)-3-methyl-1-(2-1-(piperidyl)phenyl) butyl amine and (S)-2-ethoxy-4-(2-(3-methyl-1-(2-1-(piperidyl)phenyl)-butylalkyl)-amino)-2-carbonylethylbenzoate by using organic solvent, alkali, (S)-3-methyl-1-(2-1-(piperidyl)phenyl) butyl amine and catalyst into active ester through carboxylic acid-carbonic acid mixed anhydride process. The obtained compound is hydrolyzed to obtain repaglinide.    USE - Method for preparing repaglinide (claimed).    ADVANTAGE - The method prepares the repaglinide with improved yield and low toxicity in a simple and eco-friendly manner.
NOVELTY - Luteolin preparation involves agitating and dissolving rutin in alkaline water at room temperature, where 6.3 equivalents of sodium formaldehyde sulfoxylate is also added as reducing agent. The reaction mixture is continuously heated at 100 degrees C for 12 hours, where the reaction mixture is cooled after finishing high performance liquid chromatography. Diluted sulfuric acid is also added for adjusting pH to 3-4 and then kept for 24 hours, where solid is separated, filtered and washed for removing salt contained in the product.    USE - Method for preparing luteolin (claimed).    ADVANTAGE - The method prepares the luteolin with high yield and high synthesis efficiency in a simple and eco-friendly manner.    DETAILED DESCRIPTION - Luteolin preparation involves agitating and dissolving rutin in alkaline water at room temperature, where 6.3 equivalents of sodium formaldehyde sulfoxylate is also added as reducing agent. The reaction mixture is continuously heated at 100 degrees C for 12 hours, where the reaction mixture is cooled after finishing high performance liquid chromatography. Diluted sulfuric acid is also added for adjusting pH to 3-4 and then kept for 24 hours, where solid is separated, filtered and washed for removing salt contained in the product. The washed product is dried for obtaining rough product, which is continuously crystallized with ethanol for obtaining purified luteolin.
NOVELTY - Serially extracting flavone and pectin from dried orange peels, comprises: (a) carrying out raw material processing; (b) carrying out alcohol extraction; (c) filtering and concentrating filtrate to obtain an extract having major ingredient that is hesperidin; (d) washing residues and adding 10-30 times of tap water to residues; boiling; and preserving heat and filtering; (e) further extracting pectin from the residues of (d) and filtering; and (f) blending the filtrates of (d) and (e) and concentrating; depositing by alcohol, and filtering; washing the residues, and drying to obtain pectin.    USE - The process is useful for serially extracting flavone and pectin from dried orange peels (claimed).    ADVANTAGE - In the process, the extraction solvent used is easy to recycle; the heat preserved extraction of pectin is capable of reducing energy consumption; and multiple components in the dried orange peels can be extracted and used.    DETAILED DESCRIPTION - Serially extracting flavone and pectin from dried orange peels, comprises: (a) carrying out raw material processing: cutting the dried orange peels for future use; (b) carrying out alcohol extraction: extracting general flavone of the dried orange peels through reflux using industrial alcohol; (c) filtering and concentrating filtrate to obtain an extract having major ingredient that is hesperidin through efficient liquid phase detection; (d) washing the residues after filtering by using water for 2-3 times, and adding 10-30 times of tap water to the residues; boiling the mixture and adjusting a pH value by hydrochloric acid to 1.5-2.0; and preserving heat and filtering; (e) further extracting pectin from the residues of (d) at 80-90 degrees C and filtering; and (f) blending the filtrates of (d) and (e) and concentrating the mixture; depositing by alcohol for 8 hours, and filtering; washing the residues by 60-70% of ethanol for 2-3 times, and drying at 45 degrees C to obtain pectin.
NOVELTY - The apparatus has electrolysis polar plates arranged in electrolysis chamber. A power output device (20) is connected with the electrolysis device (10), to provide the power to the electrolysis device. A mixing device (40) is arranged with mixing air inlet pipe (42) connected to hydrogen-oxygen output port (14) of the electrolysis device. A fuel inlet port (51) is connected to fuel output port (43) of the mixing device through conveying pipeline (15). An adjusting valve (53) of the spray gun device (50) is arranged to adjust the output amount of fuel.    USE - Hydrogen-oxygen fuel combustion apparatus.    ADVANTAGE - The hydrogen-oxygen fuel combustion can be performed efficiently and welding operation with respect to combustion apparatus can be performed effectively. The fuel burning operation can be effectively performed by the combustion apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen-oxygen fuel combustion apparatus.    Electrolysis device (10)    Hydrogen-oxygen output port (14)    Conveying pipeline (15)    Power output device (20)    Mixing device (40)    Mixing air inlet pipe (42)    Fuel output port (43)    Spray gun device (50)    Fuel inlet port (51)    Adjusting valve (53)
NOVELTY - The organic waste processor has a processing tank (3) for processing the organic waste by the microorganism in the internal space of the processor. Multiple process chambers (S1 to S4) of a processing tank main body are provided with partition walls (21,23,25). A vent (12) for ejecting the organic waste and an inlet (11) for injecting the organic waste are formed in the processing tank main body.    USE - Organic waste processor.    ADVANTAGE - The organic waste processor has a processing tank for processing the organic waste by the microorganism in the internal space of the processor, and thus ensures improved organic waste processor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an organic waste processor.    Processing tank (3)    Inlet (11)    Vent (12)    Partition walls (21,23,25)    Process chambers (S1 to S4)
NOVELTY - Biogas plant comprises: (a) a fermentation tank for a fermenting mass; (b) a storage- and a dosing device for a biomass with a storage container, which is designed with a flexible, anti-slipping insert for loading with the biomass, and exhibits an unloading edge, and a pulling device (3) for reducing the insert in the storage container, so that biomass resting on it is raised up to the unloading edge; and (c) a discharge conveying device for the biomass from the storage- and the dosing device into a filling port of the fermentation tank.    USE - The plant is useful for generating a combustible biogas through anaerobic fermentation of a fermenting substrate of an agricultural biomass including corn- and grass silage and/or organic wastes including manure and compost.    ADVANTAGE - The plant exhibits improved loading capacity with the fresh biomass and during the delivery of the biomass into the fermentation tank, and uses high dead-weight exhibiting storage container in slightly slanting position for self-emptying or moving.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Storage container (1)    Pulling device (3)    Front wall (12)    Rear wall (13)    belt (21)
NOVELTY - The method involves mixing a waste grease from which impurity is removed by pressure filtration and diesel oil according to certain ratio to obtain mixed fuel to be used as the fuel of dry distillation. Biochemical sludge is dry distilled under an airproof condition of no oxygen, no combustion and high temperature. The water in the biochemical sludge is transformed to vapor. A part of the biochemical sludge is transformed to combustible gas. Another part of the biochemical sludge is transformed to biological carbon.    USE - Method for integrally treating biochemical sludge and municipal waste grease in a municipal wastewater treatment plant.    ADVANTAGE - The method reduces the cost of dry distillation of the biochemical sludge and makes use of waste grease simultaneously.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a method for integrally treating biochemical sludge of a municipal waste grease in a municipal wastewater treatment plant.'(Drawing includes non-English language text)'
NOVELTY - System comprises multiple pumps and an evaporation/concentration unit, where multiple pumps are used to pump organic waste liquid into the evaporation/concentration unit. The organic waste liquid is evaporated and concentrated in the evaporation/concentration unit to obtain a concentrated solution. pH value of the concentrated solution is maintained to 5.5-6.5. The concentrated solution comprises ammonia nitrogen and organic nutrients. The concentrated solution is simply deposited and separated, and then supernatant is recycled.    USE - System for processing organic waste liquid (claimed).    ADVANTAGE - The organic waste liquid processing system enables to process the organic waste liquid in a simple, easy, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - System comprises multiple pumps and an evaporation/concentration unit, where multiple pumps are used to pump organic waste liquid into the evaporation/concentration unit. The organic waste liquid is evaporated and concentrated in the evaporation/concentration unit to obtain a concentrated solution. pH value of the concentrated solution is maintained to 5.5-6.5. The concentrated solution comprises ammonia nitrogen and organic nutrients. The concentrated solution is simply deposited and separated, and then supernatant is recycled. The condensed dirty water is obtained from the evaporation/concentration unit. The condensed dirty water is sent in a biochemical sewage treatment unit. The dirty water is biochemically processed to meet national related standard or water industrial recycling standard of enterprise, then the processed dirty water is recycled.
NOVELTY - Electrolyzer based on one nucleus-shell cell for the conversion of electrical energy into hydrogen. The nucleus-shell cell comprises three main components: (a) the nucleus of the cell, based on a highly dielectric material, which encases the electrode configuration; and (b) the shell, which envelops the dielectric nucleus and guarantees the sealing of the cell.    USE - The electrolyzer is used for the conversion of electrical energy into hydrogen (claimed).    ADVANTAGE - The use of a dielectric nucleus cell equipped with geometrical characteristics allows a clear separation between the membrane-electrode assembly (MEA) and the insulating compartment for facilitating device maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded view of the nucleus.
NOVELTY - The burner has a combustion chamber connected with a feeding pipe and an air outlet pipe. An air chamber placed between a cavity body and the combustion chamber. A gas chamber is connected with an air pipe. The air pipe is connected with an air adjustor. The combustion chamber is provided with an air inlet hole. Air enters into the air chamber through the air pipe and enters into the combustion chamber through an air hole to replenish required proper gas and adjust inner temperature of the combustion chamber. An air outlet pipe is transversely placed at center of the combustion chamber.    USE - Anti-clogging biomass gasification burner.    ADVANTAGE - The burner can adjust the inner temperature of the combustion chamber when the air inlet amount of the air pipe is adjusted through the air adjustor. The air inlet amount can be reduced when temperature of the combustion chamber exceeds 1000 degree centigrade, so as to prevent clinker from achieving a melting point due to high temperature and avoid formation of slag, thus avoiding difficulty for cleaning the slag and avoiding accumulated clinker, which interferes cyclone in the combustion chamber and influences the cyclone dust removing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an anti-clogging biomass gasification burner.
NOVELTY - The feeder has a conical pipe (9) located at a bottom of a storage bin (2). A vertical discharging shaft (1) is located in the storage bin. A vertical motor (6) is assembled at an upper end of the storage bin. A lower end of the storage bin is provided with a discharging rod (11). The vertical discharging shaft is driven by the vertical motor to rotate. A conical feeder (4) is placed in the pipe. An end of the pipe is provided with a transverse motor (7). Another end of the pipe is provided with a variable diameter auger (8). Top of the storage bin is provided with a charging opening (12).    USE - External biomass spiral feeder.    ADVANTAGE - The feeder allows biomass to pass the conical feeder, so that the flow area is gradually reduced and compressed and accumulation density is increased. The feeder realizes pressure separation and air lock of the combustion device or the gasification device. The feeder is prevented from influencing feeding process due to air leakage. The feeder avoids accumulation and blockage problems of biomass at the discharging opening.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an external biomass spiral feeder in partial section.    Vertical discharging shaft (1)    Storage bin (2)    Conical feeder (4)    Vertical motor (6)    Transverse motor (7)    Variable diameter auger (8)    Conical pipe (9)    Discharging rod (11)    Charging opening (12)
NOVELTY - The feeder (12) has a funnel-shaped feed bin (2) and a conical tube (9) that are combined to form a right angle. A vertical feeding shaft (1) is arranged in the feed bin. An upper end the feed bin is provided with a vertical motor (6). A lower end of the feed bin is provided with a feeding rod (11). The vertical feeding shaft is rotated by the vertical motor. A conical feeder (4) is arranged in the conical tube. An end the conical tube is provided with a transverse motor and another end is connected to a reducing auger (8). A top part of the feed bin is fixed with the feeder.    USE - Built-in biomass spiral feeder.    ADVANTAGE - The feeder adopts conical feeding mode, compresses biomass and reduces the flowing area while entering the conical feeder, thus increasing density. The feeder has a combustion device or the gasification device and the feeder that are isolated from pressure and are air locked, where leakage between the combustion device or the gasification device and the feeder is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a built-in biomass spiral feeder.    Vertical feeding shaft (1)    Funnel-shaped feed bin (2)    Conical feeder (4)    Vertical motor (6)    Reducing auger (8)    Conical tube (9)    Feeding rod (11)    Feeder (12)
NOVELTY - The system has multiple sets of separation devices arranged outside fluidized bed gasification reactors. The devices separate a reactant product of the fluidized bed gasification reactors into two grades. Each set of the separation device comprises a first separation device and a second separation device, a biomass raw material supply system for providing reaction raw material for the fluidized bed gasification reactors, and a gasification medium supply system for providing gasification medium to the fluidized bed gasification reactors.    USE - Biomass gasification parallel connection reaction system.    ADVANTAGE - The system ensures multiple parallel fluidized bed gasification reactors can synchronously react, thus improving yielding efficiency of fuel gas for multiple times and realizing controllability of flow rate of output fuel gas by controlling opening and closing of a fuel gas output pipeline of each fluidized bed gasification reactor. The other reactors are prevented from being influenced and repaired when one of the reactor or other assorted device is trapped in failure.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification parallel connection reaction system.
NOVELTY - The device has a rotating shaft positioned in a sleeve body and sleeved with a spiral blade. An end of a barrel body is provided with a slag inlet and another end of the barrel body is provided with a slag outlet. The barrel body is installed in an inclined manner. The slag outlet is higher than the slag inlet. The slag inlet of the barrel body is connected to a waste outlet at a bottom part of a biomass gasification furnace. A water tank is connected to the slag outlet. The slag inlet and the slag outlet are provided with valves, respectively.    USE - Sealed deslagging device for a biomass gasification furnace.    ADVANTAGE - The device discharges the falling ash by the push force of the spiral blade, and the inclined structure prevents leakage of smoke or reaction gas from the deslagging device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a sealed deslagging device.
NOVELTY - The system has a separation device arranged outside a fluidized bed gasification reactor. A gasification medium supply system is utilized for supplying a gasification medium to the fluidized bed gasification reactor. An emergency ash discharge device is connected with a separation device and another separation device. The emergency ash discharge device comprises an ash discharge pipe, a valve positioned on the ash discharge pipe and a lime-ash transmission device positioned on the terminal of the ash discharge pipe. The lime-ash transmission device is connected to a lime-ash treatment device.    USE - Biomass gasification reaction system.    ADVANTAGE - The separation device can be smoothly discharged by opening the valve of the emergency ash discharge device when the loop exit of the separation device is blocked, so as to ensure the normal operation of the system and the normal running of the reaction, improve the gas combustion efficiency, reduce the gas content of the burned gas, reduce the environmental pollution, ensure the silting treatment be more easy to perform, save a lot of maintenance time and avoid the long closing down of the system in a better manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification reaction system.
NOVELTY - The device has a driving device connected with a rotary shaft that is sleeved to a spiral blade. Periphery of the spiral blade is sleeved to a material feeding pipe that is provided with a material feeding port and a material discharging port. An air hole region is provided with multiple air holes and arranged between the material feeding port and the material discharging port. A sealing cover is sleeved at an outer side of the air hole region and provided with a wind inlet port. The wind inlet port is connected with a wind outlet port of a wind supplying device.    USE - Air curtain material feeding device for a biomass gasification reaction system (Claimed).    ADVANTAGE - The device prevents the fuel gas from leaking into the air. The device avoids problems caused by spontaneous combustion, explosion and poisoning caused by the fuel gas leakage, so that broken wood bits are blown to the material discharging port in an air curtain material feeding manner, so as to prolong the service life of the device. The device is prevented from being accumulated and blocked by the broken wood bits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification reaction system comprising a fluidized bed gasification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of an air curtain material feeding device.
NOVELTY - The device has a buffer chamber provided with an inlet. Bottom of a work chamber is provided with an outlet. The buffer chamber is installed above the work chamber. The buffer chamber and the work chamber are connected by locking devices e.g. narrow passageway and valve. An outlet at bottom of the work chamber is provided with a valve i.e. spherical valve and rolling cylinder valve.    USE - Biomass stokehold storing device for biomass vaporization reaction system (claimed).    ADVANTAGE - The device ensures smooth external material input and prevents leakage of the hot reaction gases in the reaction system such as fluidized bed vaporization reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass stokehold storing device.
NOVELTY - The device has a rotating shaft connected with a helical blade. A feeding pipe is arranged at outer side of the helical blade. The feeding pipe is provided with a feeding mouth and a discharge mouth. The device is provided with an airlock structure that is arranged between feeding mouth and discharge mouth of the feeding pipe. Density of biomass raw materials at the feeding pipe is greater than an adjacent place. The airlock structure is made from a section of a relatively thick rotating shaft that is thicker than an adjacent rotating shaft.    USE - Airlock feeding device for use in a biomass gasification reaction system.    ADVANTAGE - The airlock structure in the feeding device prevents fuel gas produced in the fluidized gasification reactor from leaking into air and casthouse store device by passing through the feeding device. The feeding device avoids dangers such as spontaneous combustion, explosion, human poisoning resulting from gas leakage, and protects device and raw materials, and ensures better safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an airlock feeding device in partial section.
NOVELTY - The system has multiple burning devices arranged on a discharge end surface of a heating furnace and furnace walls. A gas pipeline is provided with a gas general pipe and gas branching pipes. A gas inlet hole gas general pipe is arranged above an end part of the heating furnace. The burning devices are connected with a gas general pipe through gas branching pipes. The burning devices are arranged in a horizontal straight line. Each burning device is provided with a heat storage chamber that is arranged in a furnace wall and a burner and provided with multiple heat retainer processing holes.    USE - Biomass gas burning system.    ADVANTAGE - The system enables transmission mode of the biomass gas to distribute the biomass gas evenly to the burning devices. Arrangement of up and down staggered of the burning devices on a kiln wall ensures temperature of/in the heating furnace even and coincident, so that the arrangement is better for improving burning efficiency of the biomass gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas burning system.
NOVELTY - The system has a heating furnace provided with a combustion device and a gas pipe. A gas pipe of the heating furnace is directly connected with a biogas gasification reaction system. The biogas gasification reaction system is equipped with a biogas fluidized bed gasification reactor to prepare the biogas gas. A biogas raw material feeding device supplies biogas raw material to a biogas fluidized bed gasification reactor. A separation device with multiple levels is equipped with two separation units.    USE - Metallurgy steel heating furnace system for preparing biogas.    ADVANTAGE - The system saves the transportation cost and avoids environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a metallurgy steel heating furnace system.
NOVELTY - Recycling and purifying biogas liquid comprise collecting biogas liquid, pumping the liquid to the upper part of the tower box at the top of the high-level water tower, spraying liquid upward; making the liquid from the bottom of the tower box incline along the vacuum overflow weir and lift upward to driven the waterwheel, carrying out aerating and purifying; making the liquid from the waterwheel to the baffling tank, carrying out settling and removing impurity; and sending the liquid from the baffling tank to the solar vaporizer, and collecting purified water.    USE - Method for recycling and purifying biogas liquid (claimed).    ADVANTAGE - The method has convenient operation, and can save energy, protects environment, has economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system comprising a biogas liquid tank. The biogas liquid tank is connected with a sewage pump by the pipe. The output end of the sewage pump is connected with the nozzle above the tower box of the high-level water tower. A vacuum overflow weir is installed under the water outlet at the bottom of the tower box. The inclined surface of the vacuum overflow weir lifts upward to form a flip bucket. A waterwheel, a diversion channel and a baffling tank are installed in the back of the vacuum overflow weir corresponding to the flip bucket. The outlet of the baffling tank is connected with the solar vaporizer by the pipe. The solar vaporizer is connected with a water-collecting groove by the pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a system for recycling and purifying biogas liquid.
NOVELTY - The device has a feeder whose outlet is connected with the inlet of an air explosion rotating kettle. The outlet of the air explosion reacting kettle is connected with the inlet of a buffer kettle. The outlet of buffer kettle is connected with the inlet of a dewatering machine whose outlet is connected with the inlet of a forming machine.    USE - Device for preparing fuel from sludge and straw.    ADVANTAGE - The air explosion pressure is increased by a booster piston without using the pressurizing gas. The pressurizing energy consumption is low. The air explosion pressure is increased, and the production efficiency is improved. The material can be heated indirectly, the energy consumption is low, and the production cost of downstream product is reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing fuel from sludge and straw.    Boosting piston (6)    Tank main portion (7)    Discharge hole (8)    Valve (9)    Steam inlet (10)
NOVELTY - A reformer (620) has a modifier filled with a modification catalyst, and a heat exchanger for heating water by heat exchange with combustion gas produced in combustor, and generating water vapor. The heat exchanger has a waste gas flow path for circulating combustion gas, and water flow path for exchanging heat with waste gas and having water storage portion with large cross-sectional area in distribution direction. The reformer produces reformed gas having hydrogen by mixing water vapor and source gas containing hydrocarbon fuel.    USE - Reformer is used in modification unit used in fuel cell system (both claimed).    ADVANTAGE - The reformer prevents deterioration of catalyst, and has simple structure. The generation of caulking is prevented.    DETAILED DESCRIPTION - A reformer has a modifier filled with a modification catalyst, and a heat exchanger for heating water by heat exchange with combustion gas produced in combustor, and generating water vapor. The heat exchanger has a waste gas flow path for circulating combustion gas, and water flow path for exchanging heat with waste gas and having water storage portion with large cross-sectional area in distribution direction. The reformer produces reformed gas having hydrogen as main component by mixing water vapor and source gas containing hydrocarbon fuel, and contacting with modification catalyst heated by combustor. INDEPENDENT CLAIMS are included for the following:    (1) modification unit; and    (2) fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of structure of modification unit.    Burner unit (151)    Reformer (620)    Modification container (622)    Cooler (840)    Water retention portion (846)
NOVELTY - The system has a parallel assisting system provided with a biomass gasifying device (10) and a paraboloidal groove type solar thermal collector field (11). A working medium outlet is connected with a steam inlet (a) of a heater (1) through a steam outlet valve (9) of the parallel assisting system. A working medium inlet is connected with a water draining outlet (b) of the heater through a water draining inlet valve (8) of the parallel assisting system. An inlet of an air compressor (12) is provided with a tower type solar air pre-heating system air inlet valve (5).    USE - Heater system for a fire coal electric power plant.    ADVANTAGE - The system utilizes biomass energy and solar energy, so as to heat and feed water reliably. The system reduces steam pumping amount of a steam turbine of the heater. The system reduces coal consuming amount to generate power under condition of maintaining an unchanged electric energy production, so as to effectively reduce discharging amount of carbon dioxide and reduce environment pollution of the fire coal electric power plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a heater system.    Steam inlet (a)    Water draining outlet (b)    Heater (1)    Tower type solar air pre-heating system air inlet valve (5)    Water draining inlet valve (8)    Steam outlet valve (9)    Biomass gasifying device (10)    Paraboloidal groove type solar thermal collector field (11)    Air compressor (12)
NOVELTY - The combustor has an oven body (1) provided with an air quantity distributor (7) for thermally decomposing and gassing biomass fuel. A mechanical feed device is provided with a disk separator (3) and a helical conveyer (4) that are driven by an electric speed reducer. A jet head (5) is provided with a rotary air port for generating combustion flame by high temperature biomass gas. An inlet of the air quantity distributor is connected to an electric blast fan (8), and an outlet of the quantity distributor is connected to a primary air pipe (9) and a rotary air pipe (6).    USE - Gasification combustor for biomass fuel.    ADVANTAGE - The combustor is convenient to use and environment-friendly, and saves energy, and has high working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a gasification combustor for biomass fuel.    Oven body (1)    Disk separator (3)    Helical conveyer (4)    Jet head (5)    Rotary air pipe (6)    Air quantity distributor (7)    Electric blast fan (8)    Primary air pipe (9)
NOVELTY - The furnace has a hearth (6) provided with a conical or cylindrical furnace core (8) whose bottom part is installed with a furnace core tray (10), where a bottom part of the hearth contains a furnace bridge (11). The furnace bridge is connected with a furnace bridge pull rod (12). A lateral wall of a furnace body (1) is arranged at an upper part of the hearth and provided with a smoke discharge flue (13). An upper part of the body is provided with a firewood filling port (14), and a lower part of the body is provided with an oxygen feeding port (15).    USE - Dual purpose energy-saving type atomization furnace for burning firewood and coal.    ADVANTAGE - The furnace has concentrated fire power and better utilization effect, and ensures firewood or coal to be completely burnt without black smokes. The furnace is simple in structure, convenient to utilize, and the manufacturing cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a dual purpose energy-saving type atomization furnace.    Furnace body (1)    Hearth (6)    Furnace core (8)    Furnace core tray (10)    Furnace bridge (11)    Furnace bridge pull rod (12)    Smoke discharge flue (13)    Firewood filling port (14)    Oxygen feeding port (15)
NOVELTY - The facility has a multifunctional pyrolysis gasification furnace (1), a water cooling separator (28) i.e. sealed water tank, a dry fuel absorber (35), a mesh screen dust filter (39), an air compressor (43), a fuel storage tank (46) and a gas special oven (52) that are connected through a gas pipe. The furnace, the separator and a heat preservation water tank (59) are connected through a water pipe. An inner side of the furnace is provided with layers of spaces, where a top layer is a material storage chamber (2) and a bottom layer is an ash receiving chamber (15).    USE - Production facility for biomass pyrolysis gas.    ADVANTAGE - The combustible biosome is implemented with high-temperature anoxia pyrolysis in the gasification furnace to discharge mixture gas, and after water cooling separation process, dry fuel absorbing process and multilayer mesh screen filtering process, the facility allows water steam, tar gas, dust and impurity gas or impurity substance to be separated out, and high-purity combustible gas is pressed into a gas storage tank through a compressor for sedimentation and purification processes, thus obtaining pure combustible gas with high combustion value and colorless property, and the combustible gas is utilized as energy for cooking and generating, and the combustible gas is clean and recyclable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a production facility for biomass pyrolysis gas.    Pyrolysis gasification furnace (1)    Material storage chamber (2)    Ash receiving chamber (15)    Water cooling separator (28)    Dry fuel absorber (35)    Mesh screen dust filter (39)    Air compressor (43)    Fuel storage tank (46)    Gas special oven (52)    Heat preservation water tank (59)
NOVELTY - Method for oxidizing L-arabinitol to L-xylulose, involves (a) obtaining purified arabinitol dehydrogenase containing tetramer of a polypeptide, where the polypeptide comprises a 363 amino acid sequence (SEQ ID NO: 1) fully defined in the specification and amino acid sequence exhibiting at least 95% homology to SEQ ID NO: 1, and (b) contacting substrate containing arabinose to oxidize arabinitol with the arabinitol dehydrogenase.    USE - The method is useful for oxidizing L-arabinitol to L-xylulose which is used as biofuel and in other industrial food product.
NOVELTY - Conveyor (1) for collecting and transporting the biomass in an area of a dosing opening between a fodder mixer and a screw shaft (4), is claimed. The biomass is collected by oscillating and/or rotating toothed tracks (2) or other transportation aids (e.g. screw), and is pushed in the direction of the screw shaft.    USE - The conveyor is useful for collecting and transporting the biomass in an area of a dosing opening between a fodder mixer and a screw shaft (claimed).    ADVANTAGE - The conveyor prevents accumulation of the biomass in the dosing opening, and thus it allows receiving of the biomass in an adequate amount by the screw shaft.    DESCRIPTION OF DRAWING(S) - The figures 1 and 2 show a schematic representation of the conveyor.    Conveyor (1)    Rotating toothed tracks (2)    Housing lining (3)    Screw shaft (4)
NOVELTY - Producing a high carbon content biomass and biosolid slurry using an optimum carbon to water mass ratio comprises: providing an amount of biomass and an amount of biosolid to form a slurry mixture; and treating the mixture under a non-oxidative gas.    USE - The method is useful for producing a high carbon content biomass and biosolid slurry using an optimum carbon to water mass ratio.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for converting biomass into a higher carbon content, high energy density slurry, comprising: providing an amount of coal slurry, and adding a mixture of biomass and water containing up to 60% solids, where the mixture is heated under a non-oxidative gas to obtain a stable slurry containing 20-40 wt.% of carbon in the slurry; or providing a mixture of biomass and water containing up to 60% solids.
NOVELTY - Combined dual anaerobic process of biomethanation involves anaerobic digesters for biogas generation in dual phase using mixed or multiple solid feeds as substrates; culture preparation tank/unit (10) for preparing feed from non-digested feed material; filtration unit (11)/percolation unit for draining excess water from non-digested feed material; and manure preparation unit (12) for preparing manure from non digested feed material.    USE - For producing biogas and manure which is renewable energy source and sludge that could be used as fertilizer.    ADVANTAGE - The process reduces overall hydraulic retention time required for biomethanation process, and thus reducing size of biogas digester of equivalent capacity. The process describes solid state anaerobic fermentation, which increases efficiency of biomethanation process. The process describes dual biomethanation, where leachate from solid state methane digester is utilized in liquid state methane digester to maximize biogas production. The process produces less waste water than wet digestion systems and hence requires less equipment for managing this effluent stream. The process involves minimum auxiliary power/energy consumption. The solid state methane digester process is self sustaining producing, biogas, fuel and manure with minimum effluent slurry, thus solving the problem of waste disposal.    DESCRIPTION OF DRAWING(S) - The figure shows process flow diagram of dual phase digestion process using solid state digester.    Feed Storage Tank (1)    Solid State Methane Digester (2)    Reaction chamber of solid state methane digester (3)    Vertical perforated unit (tube) (4)    Liquid state methane digester (5)    Reaction chamber of liquid state methane digester (6)    Biogas storage vessel (7)    Inlet port for collecting percolate (8)    Outlet port for recycling the percolate (9)    Culture preparation tank (10)    Filtration Unit (11)    Manure Preparation Unit (12)
NOVELTY - Drying material (10), preferably sewage sludge, comprises applying, preferably ventilating a material in a layer to dry on a support surface (15). At least one upper layer (14) from the material is applied to the applied lower layer (12).    USE - The method is useful for drying material, preferably sewage sludge.    ADVANTAGE - The method is carried out in a drying device, which makes the material to be dried in to several layers to achieve a uniform layer thicknesses, thus it exhibits a uniform and efficient drying.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) drying device for carrying out the above mentioned method; and    (2) a biogas plant with the drying device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant during an introduction of a first material layer.    Material (10)    Lower layer (12)    Upper layer (14)    Support surface (15)    Machine (20)
NOVELTY - Peat material (6) is introduced into a reactor (16) and thermally treated under conditions where organic matter present in the peat material is at least partially pyrolyzed. The thermal treatment results in generation of gaseous reaction products (10) and coke (8). Coke is separated from the gaseous reaction products, which are passed from the reactor to a combustion process (13). Coke is recycled into the ground. The reactor is provided with reaction heat by passing flue gasses (11) generated in the combustion process into the reactor.    USE - Method for curtailing greenhouse gas emissions in fuel applications of peat.    ADVANTAGE - The method enables quick decomposition of peat, significantly reduces the amount of hydrocarbons released to the atmosphere during decomposition, and effective use of chemical energy contained in the volatile components of peat for energy production without increasing the greenhouse effect. The produced coke can be used as soil conditioning fertilizer. Overheating of fuel is prevented since the unreacted and in this stage still mainly dust-free fuel first contacts the hottest gas at the upper portion of hopper. At the lower portion of hopper, the gas is cooled to the temperature of fuel to be treated, thus avoiding local overheating even in case of already completed pyrolysis or drying reactions binding heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for curtailing greenhouse gas emissions in fuel applications of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the thermal treatment of peat as a continuous co-current process.    Peat material (6)    Coke (8)    Gaseous reaction product (10)    Flue gases (11)    Combustion process (13)    Reactor (16)
NOVELTY - A perfluorinated resin is prepared by copolymerizing of tetrafluoroethylene, two kinds of vinyl ether monomers having sulfonyl-fluoride-containing short pendant groups with different structures, and a vinyl ether monomer having a cyano-containing pendant group. The resin mainly contains difluoromethane-containing repeating unit (I).    USE - Perfluorinated resin is used for producing ion-exchange membranes used for manufacturing fuel cells e.g. high-temperature fuel cell (all claimed).    ADVANTAGE - The ion-exchange membrane containing the perfluorinated resin has high exchange capacity, excellent resistance to various chemical media, excellent durability, high electroconductivity, high mechanical strength, high dimensional stability and low membrane electrical resistance, and suitable for use in high-temperature fuel cells.    DETAILED DESCRIPTION - A perfluorinated resin is prepared by copolymerizing tetrafluoroethylene, two kinds of vinyl ether monomers having sulfonyl-fluoride-containing short pendant groups with different structures, and a vinyl ether monomer having a cyano-containing pendant group. The resin mainly contains difluoromethane-containing repeating unit of formula (I).    n=0-3, preferably 0;    a-c=3-15;    d,e=1-3;    x/(x+y+z)=0.2-0.7;    y/(x+y+z)=0.2-0.79;    z/(x+y+z)=0.01-0.1;and    M+=H, lithium ion, sodium ion, potassium ion, rubidium ion, cesium ion or ammonium ion, preferably sodium ion, potassium ion or ammonium ion.    An INDEPENDENT CLAIM is included for preparation of perfluorinated resin, which involves copolymerizing tetrafluoroethylene, vinyl ether monomer having phosphonate pendant group and sulfonyl fluoride monomer having short pendant group in presence of initiator at 10-100 degrees C, preferably 10-80 degrees C and reaction pressure of 2-10 MPa, preferably 2-6 MPa for 1-10 hours.
NOVELTY - The method involves performing vibration welding process by pressing a discrete manifold (110). The cascade deformation is generated in the discrete manifold, and a virtual model of the discrete manifold is implemented. A fusion groove is formed in the discrete manifold, and a fusion protrusion is inserted into the fusion groove.    USE - Vibration fusion method for manufacturing manifold of a fuel cell.    ADVANTAGE - The method effectively performs the vibration welding process, prevents the cascade deformation, increases the durability of the manifold of a fuel cell, and prevents the generation of leakage in the discrete manifold.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a vibration fusion method. '(Drawing includes non-English language text)'    Discrete manifold (110)    Jig (200)    Jig core (210)
NOVELTY - The apparatus has an exhausting unit (700) ejecting gas generated in an agitation vat (100). A rotary shaft (200) is arranged in an inner side of the agitation vat along a longitudinal direction. An air supply part supplies oxygen to an inner side of a driving part (400). A heater part (500) heats the agitation vat that rotates a wing (210). An outlet ejects organic waste formed in a side of the agitation vat. A demount member (300) is installed at an inner surface of the agitation vat. A scraper (211) is equipped in an end of the wing.    USE - Apparatus for disposing organic waste e.g. organic sludge, glassy waste and food waste.    ADVANTAGE - The apparatus dries the organic waste in a uniform manner, and performs outage treatment of the organic waste in an efficient manner. The apparatus reduces drying period, and blocks unnecessary energy damping. The apparatus reduces manufacturing cost and quantity of water for activity condition of microorganism. The apparatus is small in size, and reduces energy necessary for separate water supply of a deodorizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an organic waste disposing apparatus.    Agitation vat (100)    Rotary shaft (200)    Wing (210)    Scraper (211)    Demount member (300)    Driving part (400)    Heater part (500)    Exhausting unit (700)
NOVELTY - A biomass of lactic acid bacteria is increased by adding glutamic acid to the lactic acid bacteria fermentation nutrient medium.    USE - Method for increasing biomass of lactic acid bacteria (claimed).    ADVANTAGE - The method has simple and convenient operation, and is carried out under low pH condition.
NOVELTY - The method involves irradiating laser pulse (11) to to-be-measured gas (12) e.g. nitrogen gas. The Mie-scattering light (30) generated by irradiation of laser pulse is measured. The measurement state of laser pulse is monitored by meter (15A). The signal strength of Mie-scattering light is measured. Measurement data are permitted if the signal strength is in threshold-value. The permitted mie-scattering signal strength data are accumulated for preset time. The dust concentration of gas is calculated based on average value of Mie-scattering signal strength data.    USE - Method of measuring dust concentration in gas such as nitrogen (claimed) discharged from combustion installation such as biomass combustion furnace of biomass gasification system. Can also be used for measuring dust concentration in gas discharged from power generating plant, chemical processing plant, pressurization fluid bed boiler, gasifier, and in coke oven gas of turbine, gas engine, etc.    ADVANTAGE - The reliability of measurement of the dust concentration by Mie-scattering light in to-be-measured gas is improved by correcting the variation in the measurement of Mie-scattering light. Since the data of the laser pulse output value which is not appropriate can be excluded, the dust analysis in gas can be made in short time. The dust analysis in the gas is stably performed over long period of time by monitoring the optical axis of laser pulse. The measurement precision of dust analysis is improved by selecting appropriate laser pulse.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of combustion installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dust concentration measurement apparatus. (Drawing includes non-English language text)    Laser pulse (11)    To-be-measured gas (12)    Laser power meter (15A)    Mie-scattering light (30)    Photodetector (31)
NOVELTY - Preparing 2,2,5,5-tetrasubstituted hexane-1,6-dicarbonyl compounds (I) comprises reacting an ethylene compound (A) with a metal compound (B).    USE - The process is useful for preparing 2,2,5,5-tetrasubstitutedhexane-1,6-dicarbonyl compound (claimed), which is useful as intermediates in the synthesis of 3,3,6,6-tetramethylcyclohexane-1,2-dione. (I) is useful as drug in the treatment of various dermatological and inflammatory conditions comprising arthritis, colitis, psoriasis, acne vulgaris, and leukemia. No biological data given.    ADVANTAGE - The process provides higher yield. The process is safe and environmental friendly.    DETAILED DESCRIPTION - Preparing 2,2,5,5-tetrasubstituted hexane-1,6-dicarbonyl compounds of formula (R3-C(=O)-C(R1)(R2)-(CH2)2-C(R1)(R2)-C(=O)-R3) (I) comprises reacting a ethylene compound of formula (X-CH2-CH2-Y1) (A) with a metal compound of formula ((R3-C(O-)=C(R1)(R2))n Z(n+)) (B).    R1, R2 = H;    R3 = 1-6C alkyl, 1-6C alkoxy, 6-10C aryl or 6-10C aryloxy;    X, Y1 = leaving groups;    Z = cation; and    n = 1-4.    An INDEPENDENT CLAIM is included for the compounds prepared by the process.
NOVELTY - The system has first stage surface flow pattern wetland cell that is provided with polluted water inlet to which water outlet or end of other water processing unit is connected. The middle lower portion of water rinsing of each flow pattern cell is provided with rinsing holes at the top of water rinsing of first stage surface flow pattern cell. The end stage underflow cell is provided with discharge hole. Each stage constructed cell in series is distributed in level flow type and the bottom surface of the wetland cell has longitudinal slope of about 1%.    USE - Sewage treatment system of level baffling composite type wetland.    ADVANTAGE - Different types of wetlands can be combined according to the polluted water characteristics flexibly. The processing steps of sewage treatment system is blocked easily. The utilization rate of the sewage treatment system is improved. The polluted water can flow efficiently into each processing cell of the surface flow pattern wetland and discharge operation after finishing all the procedures are performed automatically.    DETAILED DESCRIPTION - A separating wall and different water excess structure are provided between each cell of multi-stage surface flow pattern constructed wetland cells and multi-stage surface underflow pattern constructed wetland cells cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the sewage treatment system.
NOVELTY - The cabin has fermentation cabin portion, and ventilation passages that are arranged on bottom of fermentation cabin portion. The ventilation passages extend from the center to both sides that are arranged on bottom of fermentation cabin portion. The central ventilation passage is connected with air supply fan. The feeding mechanism and discharge mechanism are arranged over fermentation cabin portion.    USE - Organic fermentation cabin for house refuse.    ADVANTAGE - The house refuse can be fermented completely and thoroughly, and hence the cabin can be operated conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic fermentation cabin.
NOVELTY - Method of preparing microbial fertilizer, involves preparing culture medium using chicken manure, bean pulp and wheat bran, preparing a composite strain by mixing brewer's yeast, Bacillus mucilaginosus, lactic acid bacteria, nitrogen-fixing bacteria, phosphate solubilizing bacteria and potassium solubilizing bacteria, adding composite strain to asepsis glucose solution, activating the strain, inoculating the activated strain to the culture medium, culturing the strain, and drying, pelleting and packing the obtained product.    USE - The method is useful for preparing microbial fertilizer for improving soil fertility and controlling insect pest of crops.    ADVANTAGE - The fertilizer provides drought resistance to crops, and fulfills requirement of organic food to crops.    DETAILED DESCRIPTION - Method of preparing microbial fertilizer, involves (a) preparing culture medium by mixing (in parts weight) chicken manure (80), bean pulp (15) and wheat bran (25) uniformly, spraying bean curd wastewater to the obtained mixture, and controlling the moisture content of the mixture to 28-36 weight/weight%, (b) preparing a composite strain by mixing brewer's yeast (10), Bacillus mucilaginosus (18), lactic acid bacteria (15), nitrogen-fixing bacteria (12), phosphate solubilizing bacteria and potassium solubilizing bacteria (8) uniformly, (c) adding composite strain (1) to 50 weight/weight% of asepsis glucose solution (3), and allowing the strain to activate for 30-45 minutes, (d) inoculating the activated strain (1.0-3.0 wt.%) to the culture medium, and mixing the culture uniformly, (e) covering the inoculated culture using a plastic film, culturing the strain for 12-20 days and mixing the culture once for every six days, and (f) drying, pelleting and packing the obtained product.
NOVELTY - A Pseudomonas strain XQ23 is separated, purified and obtained from sludge polluted by phenol, where the strain is stored in China center for culture collection on August 8, 2009 with preservation number CCTCC M 209175.    USE - Pseudomonas strain XQ23 for degrading multiple types of phenol compounds.    ADVANTAGE - The Pseudomonas strain XQ23 efficiently degrades multiple types of phenol compounds in short time.
NOVELTY - A biomass is liquefied by using subcritical or supercritical cyclohexane as medium and molecular sieve catalyst with zeolite as catalyst. The biomass oil is prepared by making biomass, cyclohexane and molecular sieve catalyst react with zeolite at 285-330 degrees C and pressure of 1.7-4.2 MPa. The mass ratio of biomass, cyclohexane and molecule sieve catalyst with zeolite is 5-40:15-112:0.2-4.    USE - Method for liquefying biomass (claimed).    ADVANTAGE - The method realizes efficient conversion of the biomass. The conversion rate and quality of converted products are enhanced as compared with conventional method.
NOVELTY - A bio-briquette is prepared by using psammophytes as main raw material, adding coal to improve and supplement heat, mechanically crushing, and grinding and forming; and adding secondary calcium base mineral slag for sulfur fixation, adding mineral adhesive to control forming procedure, uniformly agitating and pressing forming, or pelletizing and sieving, and air drying to obtain briquette product.    USE - A bio-briquette with psammophytes as base material.    ADVANTAGE - The bio-briquette has less investment and high yield during sand treatment process. Its preparation organically combines combustibility of psammophytes and desulfurization and adhesion property of secondary calcium base mineral slag to solve problems of bad economic benefit and large environment pollution of current mode of singly using the psammophytes. It solves recycle problem of large amount of calcium carbide slags and magnesium smelting slags emitted by high energy carrying industry each year, and solves problems of environment pollution and high energy consumption of current mode of using quick lime as sulfur-fixing agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of bio-briquette with psammophytes as base material.
NOVELTY - A biomass fuel is modified by quick heat treatment technique which comprises crushing biomass material to the particle with diameter less than 1 cm before heat treatment; performing quick heat treatment for 0.01-0.5 second at 300-500 degrees C under condition of limited oxygen supply of oxygen equivalence ratio less than 0.1 or no oxygen to collect and obtain heat modified biomass and little liquid by-product and associated gas; and crushing the heat modified biomass, using liquid by-product as adhesive, or adding other adhesive to form the mixed adhesive to prepare fuel.    USE - Forming method for modifying biomass fuel (claimed).    ADVANTAGE - The method can damage fiber structure of the biomass raw material to reduce flexibility to crush and grind more easily to prominently reduce crushing and forming energy consumption. It can improve heat value and stability of the formed fuel. Heat is not needed to add in the forming process with the liquid by-product as adhesive, so abrasion of mechanical equipment is relieved, durability of the formed fuel is improved, and preparation cost is decreased.
NOVELTY - A fuel is prepared by putting sludge and oil serving as heat conducting medium into heat processing field; storing the sludge and oil into respective tanks; fully mixing the sludge with the oil and pre-heating the mixture; heating the sludge-oil mixture in reduced pressure; regarding the oil as the heat conducting medium; fully mixing and contacting the oil with the sludge; fractionally distilling to remove moisture in the sludge; regarding the dry sludge as boiler fuel to provide heat energy needed for water vapor for system heating; and regarding the rest of dry sludge as fuel for sale.    USE - Method for preparing fuel from organic sludge (claimed).    ADVANTAGE - The method is operated at reduced pressure so that fire hazard can be precluded. The existence of oil has reduced corrosion from impurity in the sludge to the device and adds durability of device use. The process has no secondary pollution to the environment, and eliminates sludge processing problem.    DETAILED DESCRIPTION - Preparing fuel from organic sludge comprises putting sludge and oil serving as heat conducting medium into heat processing field; storing the sludge and oil into respective tanks; fully mixing the sludge with the oil and pre-heating the mixture through water vapor; heating the sludge-oil mixture in reduced pressure; regarding the oil as the heat conducting medium; fully mixing and contacting the oil with the sludge; fractionally distilling to remove moisture in the sludge by using boiling point difference of oil and water; regarding the dry sludge as boiler fuel to provide heat energy needed for the water vapor for the system heating; and regarding the rest of dry sludge as the fuel for sale.
NOVELTY - A boiler fuel is prepared by condensing flocculated sludge generated in environmental protection station using condensing cool; pumping condensed sludge into stirring tank, and adding dispersing agent for dispersing process; pumping processed sludge into pressing and filtering machine for dewatering; transferring dewatered sludge to roller cylinder drying machine to be dried; and doping the dried sludge into fuel coal to be mixed for use.    USE - Method for preparing boiler fuel (claimed).    ADVANTAGE - The method makes best of the feature of flocculated sludge in citric acid industry in high organic substance content and service as the boiler fuel after drying process, which recycles internal heat value and improves cleaning level of the enterprise.
NOVELTY - A membrane methane tank for treating organics, comprises traditional methane tank body, a feeding opening, a discharging opening, a polyvinyl chloride composite material membrane methane shield, and a gas outlet; where the feeding opening and the discharging opening are connected to the middle part of the traditional methane tank body; the upper half portion of the traditional methane tank is a polyvinyl chloride polymer membrane methane shield, which makes up one half of the methane tank body; and the membrane methane shield is connected to the traditional methane tank body.    USE - The membrane methane tank is useful for treating organics (claimed).    ADVANTAGE - The membrane methane tank has tightness and corrosion resistance that are improved. Moreover, the tank building cost is reduced; the gas generation time is prolonged; and the efficiency of treating the organics is improved. Additionally, it is convenient to popularize.    DETAILED DESCRIPTION - A membrane methane tank for treating organics, comprises traditional methane tank body, a feeding opening, a discharging opening, a polyvinyl chloride composite material membrane methane shield, and a gas outlet; where the feeding opening and the discharging opening are connected to the middle part of the traditional methane tank body; the upper half portion of the traditional methane tank is a polyvinyl chloride polymer membrane methane shield, which makes up one half of the methane tank body; the membrane methane shield is connected to the traditional methane tank body through bonding, by a pre-embedded element, or by locking, which forms an integrated body; and the top of the membrane methane shield is connected to the gas outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the membrane methane tank for treating organics.
NOVELTY - Self-repairing anti-rust aerosol lubricant comprises liquid-containing material, propellant and aerosol packing material, where the liquid material and propellant are filled in the matched aerosol packing material by special aerosol filling device.    USE - Used as a self-repairing anti-rust aerosol lubricant.    ADVANTAGE - The aerosol lubricant: makes a pair of friction component to operate self-repairing function; has fine anti-friction function; has good anti-wear ability to improve the load capacity friction; utilizes aversion agent to improve the safety; replaces the traditional mineral base oil by environmental base oil; is biodegradable and eco-friendly; and utilizes aerosol-type packaging that makes the product easy to use.
NOVELTY - Production of alcohol ether fuel comprises: (a) mixing two additives together and adding the mixture in a reactor (A), adding gasoline, and completely and uniformly dissolving the mixture; (b) adding butanol and isobutanol in a reactor (B) to carry out reaction for 40-60 minutes; and (c) respectively adding naphtha and petroleum benzene in a reactor (C), adding fuel in a preparation kettle, adding gasoline to the fuel preparation kettle, adding methanol to a fuel mixing kettle from the reactor (B) and reacting the raw materials for 35-45 minutes to obtain the product.    USE - The method is useful for producing alcohol ether fuel.    ADVANTAGE - The method: is environmental friendly and economical; and prepares a clean product with high burning value, excellent anti-detonating property, stability and good evaporation property.
NOVELTY - The system has feed inlet of hydrogen raw material gas separating tank connected with streams of heat exchangers (1). The top outlet of separating tank (2) is connected with streams of heat exchangers. The bottom outlet of separating tank is connected with feed inlet of lightness removing tower (3) by streams of heat exchangers. The outlet on tower bottom of lightness removing tower is connected with feed inlet of methane product tower (5). The outlet of tower top of methane product tower is connected with feed inlet of nitrogen exhaust gas tower (18).    USE - Skid type multifunctional purification treatment system for carbonyl synthesized raw material gas.    ADVANTAGE - The multifunctional purification treatment system is environmental friendly. Power consumption of purification treatment system can be reduced.    DETAILED DESCRIPTION - The carbon monoxide passage (24) is connected with outlet of tower bottom of nitrogen exhaust gas tower by pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows the circuit diagram of purification treatment system.    Heat exchangers (1)    Separating tank (2)    Removing tower (3)    Methane product tower (5)    Nitrogen exhaust gas tower (18)    Carbon monoxide passage (24)
NOVELTY - Pseudomonas sp. F14 (CCTCC M 2010103) of high efficient degradation of polycyclic aromatic hydrocarbons is obtained by fusing protoplast of Sphingomonas sp. (GY2B CCTCC M 206019) with Pseudomonas sp. (GP3A CCTCC M207166), is claimed.    USE - The strain is useful for processing polycyclic aromatic hydrocarbons (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for constructing strain, comprising (i) adding penicillin and ethylenediaminetetraacetic acid into Sphingomonas GY2B and Pseudomonas GP3A in logarithmic phase to shake culture, then adding lysozyme, centrifuging and then collecting the protoplasts, (ii) mixing Sphingomonas GY2B with Pseudomonas GP3A of the same volume, centrifuging, then collecting bacteria, adding high-permeability sucrose-maleate-magnesium chloride buffer solution (2 ml) and inducing the flow of sucrose-maleate-magnesium chloride buffer solution (18 ml) into the bacteria to fuse at 36 degrees C for 5 minutes, (iii) collecting bacteria after centrifuging, washing by using the high-permeability sucrose-maleate-magnesium chloride buffer solution, coating double-antibody-inter layer to regenerate medium, culturing at 30 degrees C for 7 days to grow bacterial colony, which is Pseudomonas sp. F14 (CCTCC M 2010103).
NOVELTY - A solid oxide fuel cell electric power generation system (1) comprises solid oxide fuel cells (2) which are arranged in series with respect to air flow and fuel flow, air which is supplied to downstream of solid oxide fuel cell, and fuel which is supplied to upstream solid oxide fuel cell with respect to air flow from downstream solid oxide fuel cell with respect to air flow.    USE - A solid oxide fuel cell electric power generation system.    ADVANTAGE - The solid oxide fuel cell electric power generation system is efficient and has an easy operational management of the system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the solid oxide fuel cell electric power generation system which has heat exchanger. (Drawing includes non-English language text).    Solid oxide fuel cell electric power generation system (1)    Solid oxide fuel cells (2)    Heat exchanger (3)    Piping (20)    Fuel waste gas derived by piping (30)
NOVELTY - The structure (1) has several metal board materials (2a-2g) that are laminated mutually by spot-welding adjacent metal board materials separately. The minimum clearance between nuggets by spot welding is defined by preset formula relating contact resistance value between metal board materials and in-plane resistance value of metal boards.    USE - Electric power feeding structure for electrolysis cell (claimed) used in water electrolysis apparatus.    ADVANTAGE - The electric current is diffused fully by defining minimum clearance between nuggets by spot welding, and the damage of electrolytic membrane resulting from high heat generation by current density can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolysis cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electric power feeding structure for electrolysis cell.    Electric power feeding structure (1)    Metal board materials (2a-2g)
NOVELTY - The electric power feeding structure (3) has a wall portion (31) that is formed with a honeycomb structure and provided in the direction orthogonal to the surface of a membrane electrode assembly. The wall portion is collapsed by the compression stress applied to the wall portion by the contact pressure between the electric power feeding structure and the membrane electrode assembly.    USE - Electric power feeding structure in oxygen electrode side and hydrogen electrode side of water-electrolysis apparatus (claimed) e.g. solid polymer membrane water-electrolysis (SPWE) apparatus used for generating hydrogen used as fuel of solid electrolyte fuel cell.    ADVANTAGE - The wall portion can absorb the compression stress, and the contact pressure of the electric power feeding structure and the membrane electrode assembly can be maintained in preset range, and the electric power feeding performance can be ensured. The contact pressure between the membrane electrode assembly and the sealing structure is made high, and the sealing performance is improved. Since the concentration of the stress added to the solid polymer membrane is suppressed, the damage of the solid polymer membrane is prevented. The manufacturing cost is reduced by suppressing the increase in the contact resistance between the electric power feeding structure and the membrane electrode assembly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) water-electrolysis apparatus; and    (2) manufacturing method of water-electrolysis apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the oxygen side electric power feeding structure.    Electric power feeding structure (3)    Wall portion (31)    Inner side panel (32)    Outer side panel (33)    Through-hole (34)
NOVELTY - Method for decomposing garbage, involves adding anaerobic bacteria to household garbage or organic garbage to accelerate decomposition and compressing the generated sewage gas.    USE - The method is useful for decomposing garbage which is used for generating power and producing fertilizer.    ADVANTAGE - The method is rapid, economical and environmentally-friendly.
NOVELTY - Flower fertilizer is prepared by adding the collected wastes of pericarp, leaves, bones, leftovers, tea dregs and medicinal dregs to a container, adding water and fermenting agent to the container and sealing for 2-3 days, adding hydrogen peroxide after the wastes are completely fermented into black liquid and absorbing odor, filtering dregs and adding water to dilute to 100 folds and filling into package, is claimed.    USE - Used as a flower fertilizer.    ADVANTAGE - The flower fertilizer: makes use of wastes as raw materials, hence the fertilizer is economical and environmental friendly; and has convenient preparation method, and less odor.
NOVELTY - Producing fertilizer composition, comprises (i) proportioning materials by fully mixing animal wastes with crushed straw, where the weight proportion of animal wastes is 10-30% of total weight of materials; (ii) adding organic matter decomposing inoculant according to amount of 0.3-0.5% of raw materials, and 1-3% of lime and uniformly mixing; (iii) insulating the semi-finished product obtained in the step (ii) at 60-70 degrees C for 12-24 hours; (iv) curing the semi-finished product obtained in the step (iii) for 5-20 days to obtain the product.    USE - The method is useful for producing organic fertilizer composition.    ADVANTAGE - The fertilizer composition has low pathogenic bacteria, and high fertility and good absorption rate.
NOVELTY - A Pseudomonas stutzeri YG-26 (CGMCC 4093), is new.    USE - The P.stutzeri YG-26 and immobilized thalli are useful in agent for removing phosphorus from water, preferably sewage water for preventing eutrophication of water (all claimed).    ADVANTAGE - The P.stutzeri YG-26 is environmentally-friendly, and performs sewage water treatment process economically and simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for immobilized thalli, which is obtained by embedding the P.stutzeri YG-26 (CGMCC 4093) using sodium alginate and polyvinyl alcohol.
NOVELTY - Preparing glycerol dithiocarbamates (DTCG) comprises adding a primary or secondary amine, in the presence of carbon disulfide, into a reaction medium comprising (a) a glycerol type polyol associated with a carbonate comprising diethyl carbonate, dimethyl carbonate, ethylene carbonate or propylene carbonate in the presence of a basic catalyst or (b) a five-membered cyclic carbonate in a solvent medium; and recovering formed DTCG.    USE - The glycerol type polyol is useful as solvent (claimed). The DTCG: has antifungal properties; is useful for treating cancer; and for trapping metals. No biological data given.    ADVANTAGE - The process is carried out in one step, is cost effective and eco-friendly for preparing DTCG with good yields, good regioselectivity and good chemoselectivity. The process can be easily dispose or reuse by-products.
NOVELTY - Humic acid biological organic fertilizer comprises (in wt.%) livestock and poultry manures (15-20), humic acid (50-55), organic ammonia (15-20), phosphate rock powder (10-15), potassium fertilizer (3-5), bacterial composition (2-3) and trace element (0.5-1).    USE - Used as a humic acid biological organic fertilizer.
NOVELTY - A biogas regenerative waste processing apparatus (100) has a oil separation unit (110), a drum screen tank (120), a septic tank (600), and an evaporation unit (700). The oil separation unit separates oil (20) from raw water (10). The tank (120) has a drum screen (121) for separating intermixture (30) from oil-separated raw water. The septic tank produces biogas (60). The evaporation unit evaporates processed water discharged from screen tank using biogas, and separates residue.    USE - Biogas regenerative waste processing apparatus.    ADVANTAGE - The apparatus efficiently and economically enables biogas regenerative waste processing without affecting environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas regenerative waste processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of biogas regenerative waste processing apparatus. (Drawing includes non-English language text)    Raw water (10)    Oil (20)    Intermixture (30)    Biogas (60)    Biogas regenerative waste processing apparatus (100)    Oil separation unit (110)    Drum screen tank (120)    Drum screen (121)    Septic tank (600)    Evaporation unit (700)
NOVELTY - The method involves fermenting nitrogen-rich manure in a digester (9, 10) to remove residues from biogas (17), where solid particles, liquid particles (16) and residual particles (8) are separated from the biogas. The liquid particles are added with ammonia in an ammonia stripper (3). The treated liquid is subjected to fermenting process.    USE - Method for producing biogas i.e. methane, by fermenting nitrogen-rich manure such as poultry manure, duck manure or goose manure (all claimed) that is utilized as a fertilizer in agriculture and horticulture fields.    ADVANTAGE - The method enables producing biogas by fermenting nitrogen-rich manure in an efficient and continuous manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for producing biogas i.e. methane, by fermenting nitrogen-rich manure such as poultry manure, duck manure or goose manure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for producing biogas by fermenting nitrogen-rich manure.    Ammonia stripper (3)    Residual particle (8)    Digester (9, 10)    Liquid particles (16)    Biogas (17)
NOVELTY - Manufacture of reformed bio-oil involves contacting biomass or bio-oil with microporous molecular sieve as catalyst.    USE - Manufacture of reformed bio-oil.    ADVANTAGE - The method efficiently provides bio-oil having high calorific value and stability.
NOVELTY - Method for producing hydrogen and methane gas, involves using byproduct of ethanol fermentation of marine algae.    USE - The method is useful for producing hydrogen and methane gas, which is useful as biofuel.    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - The apparatus (100) has a concatenated path (4) connected to a gasifier (2) to proceed synthetic gas, and an arc plasma reactor (6) reforming by-product or removing the by-product to generate another synthetic gas. The arc plasma reactor sprays arc plasma to reverse direction of flow direction of the former synthetic gas, and a slip-shape nozzle is formed in a non-thermal plasma reactor (8). A discharge gas supply opening is connected to a housing unit for supplying discharge gas, and a coolant chamber is connected to a cooling water line.    USE - Apparatus for reforming and removing a tar or by-product.    ADVANTAGE - The apparatus prevents loss of carbon monoxide and hydrogen, which are the main component of the synthetic gas while maintaining quality of the synthetic gas by applying the plasma generated in the plasma reactor to one of the synthetic gas generated in the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a tar or by-product reforming and removing apparatus. '(Drawing includes non-English language text)'    Gasifier (2)    Concatenated path (4)    Arc plasma reactor (6)    Non-thermal plasma reactor (8)    Tar or by-product reforming and removing apparatus (100)
NOVELTY - The apparatus (1) has a conditioning tank (2) connected to a reactor for purifying contaminated water. A gas outlet (10) is connected with a reactor (5) for discharging biogas. A separating unit (7) comprises a capturing unit for capturing the biogas, and is connected with another gas outlet. The latter gas outlet is provided with a water seal to determine height of water level in the capture unit. A discharge unit is provided with a floating layer that is located on a water surface. The separating unit is attached with a horizontal surface of a reactor cover.    USE - Apparatus for purifying contaminated water during production of biogas i.e. methane.    ADVANTAGE - The reactor is arranged for purifying contaminated water with high quality during production biogas in simple and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for purifying contaminated water during production of biogas i.e. methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for purifying contaminated water during production of biogas.    Purifying apparatus (1)    Conditioning tank (2)    Reactor (5)    Separating unit (7)    Gas outlet (10)
NOVELTY - The method involves providing a fermentation residue with high proportion of decomposed and partially decomposed organic matter that is obtained from original processed substrates. The fermentation residue is mixed together with an active methanogenic biocenosis. The mixture is utilized for fermentation process.    USE - Method for increasing production of biogas during suspension anaerobic fermentation.
NOVELTY - A polyalkenamer rubber composition is produced by mixing (in parts weight) polyalkenamer (100), auxiliary cross-linking agent (0.05-5), auxiliary agent (1-100), peptizer (0.01-10), accelerating agent (0.1-10) and inorganic additive (1-200).    USE - Polyalkenamer rubber composition used for manufacturing fuel cell gasket (claimed).    ADVANTAGE - The polyalkenamer rubber composition enables to manufacture fuel cell gasket economically and within a short period of time. The gasket has excellent airtight property, abrasion resistance, solvent resistance, moisture resistance, extension performance, high temperature stress resistance, low gas permeability and excellent surface tension characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the fuel cell gasket.
NOVELTY - The biogas carbon producing device has pneumatic delivering device, carbonization chamber (5), heat exchanger (10), purifier (14), carbon filter (22) and water-seal flame arrestor (25) which are connected in turns by gas delivery pipe (9). The gas delivery pipe is connected to gas outlet of carbonization furnace, upper and lower ends of inner cylinder of heat exchanger, third cyclone separator (16) of purifier, upper end of inner cylinder of purifier, air inlet of upper cylinder of carbon filter, upper end of inner circle of upper cylinder of carbon filter and water-seal flame arrestor.    USE - Biogas carbon producing device used in returning and recovering gas residual heat. Can be used for producing biomass carbon fertilizer.    ADVANTAGE - Performs three-level cooling and purification process to make a high-temperature combustible gas a clean combustible gas by cooling, purification and filtering. Ensures that hot water, whose heat is changed, can be used for special aquiculture of e.g. greenhouse soft-shelled turtle. Ensures that the tail-gas discharge meets the environment protection demand.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of the biogas carbon producing device.    Carbonization chamber (5)    Gas delivering pipe (9)    Heat exchanger (10)    Purifier (14)    Third cyclone separator (16)    Carbon filter (22)    Water-seal flame arrestor (25)
NOVELTY - Processing organic liquid fertilizer, involves adding wastewater produced from bean curd production and residue into fermentation tank, disinfecting and sterilizing the wastewater and residue to obtain culture medium, mixing yeast bacterium of beer production to obtain compound bacterium, spraying obtained mixed compound bacterium to the culture medium and culturing the bacterium.    USE - The method is useful for processing organic liquid fertilizer.    ADVANTAGE - The method is simple and environmentally-friendly as it utilizes wastewater as raw material for processing.    DETAILED DESCRIPTION - Processing organic liquid fertilizer, involves (a) adding wastewater produced from bean curd production and residue in ratio of 1:0.3-0.6 into fermentation tank, disinfecting and sterilizing the wastewater and residue at 103-105 degrees C for 60-80 minutes, reducing the temperature to 30-40 degrees C and obtaining the culture medium, (b) mixing yeast bacterium, preferably Bacillus subtilis and Lactobacillus involved in beer production in a ratio of 1:1:1.2 to obtain compound bacterium, (c) spraying the obtained mixed compound bacterium (1-1.8%) uniformly to the culture medium, and (d) culturing the bacterium at 35-40 degrees C, until no bubble is generated in the fermentation tank.
NOVELTY - Preparing biodiesel by catalyzing renewable oil involves using short-chain alcohol as aryl receptor and lipase as catalyst to catalyze oily material to perform ester exchange reaction with the short-chain alcohol. Short-chain alcohol (4-8 mol) and lipase are kept in single-stage or multistage enzyme for performing dehydration by using membrane at 20-50 degrees C.    USE - Method for preparing biodiesel by catalyzing renewable oil (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a simple, cost-effective and eco-friendly manner.
NOVELTY - Extracting oil from Microcystis involves culturing microalgae in presence of light. Frustule of microalgae is collected and then oil is extracted from the collected product.    USE - Method for extracting oil from Microcystis (claimed) used in preparing biofuel.    ADVANTAGE - The method enables to extract oil from Microcystis quickly.
NOVELTY - A mosquito-repellent incense comprises (wt.%): combustible base wood powder (50-60), adhesives (10-20), pesticide (0.2-0.6), and perfume (25-35). The adhesives are dry powders of skin of oil-skin tree root. The pesticide is esbiothrin mosquitocide compound. The perfume is dry powders cypress red heart wood portion.    USE - Mosquito-repellent incense.    ADVANTAGE - The raw materials are all wood materials, except for effective insecticidal components, which meets requirement of saving energy and protecting environment. The faint scent after igniting incense makes people comfortable, changing condition that common mosquito-repellent incense smells bad after igniting so as to make people feel headache.
NOVELTY - Use of biological enzyme is claimed in catalysis of waste sludge treatment. The biological enzyme is pectinase, protease, lipase, cellulose, catalase or amylase.    USE - The biological enzyme is useful for processing waste sludge for producing organic fertilizer, and as agrochemical soil. The waste sludge is obtained from urban sewage processing factory, river, and industrial organic sludge (all claimed).    ADVANTAGE - The fermentation period of the sludge is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing waste sludge, which involves mixing or contacting the prepared biological enzyme with the sludge, adequately stirring the mixture, regulating the moisture of the mixture to 50-70%, dispersing the mixture by slightly touching through fingers, where the fingers are free of water, fermenting the mixture, turning the fermenting product after the temperature reaches 50 degrees C, stirring the mixture twice a day, and fermenting the mixture for 7-10 days to obtain the final product.
NOVELTY - A halloysite nanotube supported copper ion antibacterial agent comprises (g) silane coupling agent modified halloysite nanotube (1) as a carrier and copper ions (0.1-0.2) supported by the carrier.    USE - A halloysite nanotube supported copper ion antibacterial agent.    ADVANTAGE - The agent is cheap, environment-friendly, and easy to prepare; and has easy to obtain raw material, strong antibacterial performance and preparation method having mild reaction conditions and low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the agent comprising preparing silane coupling agent modified halloysite nanotube as carrier, adding carrier (75-100 wt.%) into soluble copper salt aqueous solution, subjecting to ultrasonic vibration at 40-60 degrees C for 24-30 hours, filtering and drying the filter cake.
NOVELTY - Metal implant material has bioactively modified surface in which chitosan and its derivatives are alternately assembled based on opposite charges in a manner of layer self assembly, where the thickness of the deposition film is 100 nm or less, or two types of chitosan derivatives with opposite charges are alternately assembled on the surface in a manner of layer self assembly. The chitosan derivatives are chosen from carboxymethyl chitosan, quaternary ammonium salt of chitosan and sulfated chitosan.    USE - As metal implant material.    ADVANTAGE - The method (M1) is simple and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing the metal implant material; and    (2) method (M2) for modifying surface of the material bioactively.
NOVELTY - Treating municipal solid waste, comprises: (a) placing municipal solid waste into a magnetic separation device, then performing magnetic separation to remove ironware; (2) conveying resulted waste into a high-temperature drying sterilization device at 80-200 degrees C to dried and sterilized at high temperature; (c) adding dry powder chemical auxiliaries into resulted dried and sterilized waste; (4) crushing the resulted product by a crushing machine; (e) agitating crushed waste in an agitation machine; and (f) pressing the obtained product in the step (e) into waste charcoal by a hot press device.    USE - The method is useful for treating municipal solid wastes.    ADVANTAGE - The method: exhibits no sewage pollution, no stink pollution, no animal pollution of e.g. fly and no germ contamination; recycles the waste as a new energy source; and realizes the purpose of waste processing safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for processing the above method, comprising a hydraulic mechanism, a drying box and an industrial boiler or an air-heater. The hydraulic mechanism is multiple hydraulic cylinders and a protection cover installed out of the hydraulic cylinder. The low portion of the drying box is divided into more than two drying chambers. A heat conduction device is installed on the outer wall of the drying chamber and connected with the industrial boiler or the air-heater. A thermal insulating layer is mounted on the outer wall of the drying box. The top portion of the drying box is a waste inlet and the bottom portion thereof is a waste outlet. A convey belt is installed under the waste outlet. A push plate of the hydraulic cylinder is matched with an inner cavity of the drying chamber.
NOVELTY - A special biological organic fertilizer comprises (wt.%) organic fertilizer (65-80), peat moss (8-10), urea (nitrogen content=46%, 3-4), potassium chloride (potassium oxide content=60%, 1-5), calcium magnesium phosphate fertilizer (phosphorus pentoxide content=12%, 6-16), borax (0.1-0.5), zinc sulfate (0.1-0.3), and rare earth micronutrients (0.1-0.2). The rare earth micronutrients are Changle (RTM: rare earth micronutrients).    USE - Special biological organic fertilizer used for oiltea Camellia.    ADVANTAGE - The fertilizer not only meets the nutrition demand of oiltea Camellia, but also improves the soil and also meets the demand for environment-friendly production of edible oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of fertilizer by adding large Bacillus (0.1-0.5%) to fresh livestock and poultry manure, uniformly mixing, stacking and fermenting, measuring temperature periodically, spreading once every 5-7 days based on temperature change, and fermenting for 30-35 days to obtain fermented organic fertilizer; crushing organic fertilizer, adding peat moss, urea, calcium magnesium phosphate fertilizer, potassium chloride and other trace element fertilizer, and uniformly mixing; and granulating, sieving, drying, metering, and packaging.
NOVELTY - Method of breeding chicken, involves collecting chicken from field to obtain an indigenous strain, collecting stem tips with dews of plant which grows fast, adding brown sugar and obtaining nutrient solution, adding indigenous strain into rice bran and diluted nutrient solution, adding inoculation material into raw material of plant straw such as haulm, wheat straw and maize straw to obtain fermentation base material, and breeding chickens by spraying nutrient solution onto base material to maintain fermenting bed.    USE - The method is used for ecological breeding of chicken.    ADVANTAGE - The method is cost-effective and environmentally-friendly. The chickens peck the hypha on the fermenting bed and thus reduces feed amount by 10%. The method enables large-scale and healthy cultivation of chicken manure.    DETAILED DESCRIPTION - Ecological cycle chicken breeding method, involves (a) collecting chicken from field to obtain an indigenous strain, (b) collecting stem tips with dews of plant which grows fast, adding brown sugar to pickle and obtaining nutrient solution, (c) adding the indigenous strain into the rice bran and diluted nutrient solution, mixing uniformly and obtaining inoculation material, (d) adding inoculation material into raw material of plant straw such as haulm, wheat straw and maize straw to obtain fermentation base material, (e) performing large-scale breeding of chickens using fermentation beds, and (f) terminally spraying nutrient solution onto the fermentation base material to maintain the bed.
NOVELTY - Bio-alcohol fuel comprises a bio-alcohol fuel starting material, comprising (in wt.%): methanol or ethanol (60 plus minus 10), dimethyl ether, diethyl ether or methylal (30 plus minus 10), propanol or isopropanol (5% plus minus 2), n-butanol (4.27 plus minus 3), castor oil (0.1 plus minus 0.01), colza oil (0.2 plus minus 0.1), pentafluorobutane (0.01 plus minus 0.005), ferrocene (0.02 plus minus 0.001) and Tween (RTM: Polysorbate) (200.4 plus minus 0.2). The fuel is prepared by evenly mixing all the raw materials in a normal pressure vessel.    USE - Used as a bio-alcohol fuel.    ADVANTAGE - The bio-alcohol fuel is a low-carbon oxygenated fuel, releases clean tail gas, has less content of carbon black and can replace petrol, diesel oil, boiler fuel oil and bunker oil.
NOVELTY - Method of preparing bioethanol, involves separating supernatant from fermented beer waste liquid, fermenting the supernatant at 30-70 degrees C to obtain bioethanol, and isolating yeast from fermented liquid containing bioethanol.    USE - The method is useful for preparing bioethanol, which is used as biofuel and transportation fuel.    ADVANTAGE - The method is cost-effective, rapid as saccharification and fermentation processes are performed simultaneously, and environmentally-friendly, and enables production of bioethanol without using diastatic enzymes.
NOVELTY - An Issatchenkia orientalis PE strain, is new. The strain is capable of producing 4x 1011 colony forming unit/ml of cells at 15 degrees C.    USE - The I.orientalis PE strain is useful for removing odor of ammonia, hydrogen sulfide and methyl (claimed) from animal excrements and for preparing feed admixture for domestic animals.    ADVANTAGE - The strain is environmentally-friendly and can even grow at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microbial formulation, which comprises the above-mentioned strain.
NOVELTY - A food waste and wastewater processing system includes a flow control tank (110), a solid-liquid separation tank (120), an anaerobic methane fermenter (130), a stripper tube (140), an anoxic/aerobic advanced processing tank (150), and a drain pipe tub (160). The flow control tank controls flow amount of food waste and wastewater. The solid-liquid separation tank separates waste and wastewater flowing in from flow control tank. The anaerobic methane fermenter decomposes waste using fermentation preprocessing tank (132) and generates methane gas.    USE - Food waste and wastewater processing system is used for domestic applications.    ADVANTAGE - The food waste and wastewater processing system reduces the concentration of pollutants in food waste with water, and enables effective collection of methane gas energy. The treated water has excellent quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food waste and wastewater processing system.    Flow control tank (110)    Solid-liquid separation tank (120)    Anaerobic methane fermenter (130)    Fermentation preprocessing tank (132)    Stripper tube (140)    Anoxic/aerobic advanced processing tank (150)    Drain pipe tub (160)
NOVELTY - Production and selection of pellets, comprises: providing a pellet production plant; producing pellets from a biomass; and analyzing all the pellets that pass through the plant.    USE - The process is useful for producing and selecting pellets.    ADVANTAGE - The process utilizes the control chamber that: rejects all the harmful pellets and assigns only the suitable pellet to the market; and automatically stores control system data without the possibility of tampering, and are available on-line, with alarm for the centralized control station via telephone line or satellite connection, or internet.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the process for the production and selection of the pellets.    Silo containing pellets not yet analyzed (1)    Conveyor belt for the pellets (3)    Laboratory analysis of the pellets (5)    Radiation control of the pellets (6)    Three-way pellet discharge system (7)
NOVELTY - The water separator has an integrated oil water separator water inlet (1), a slag removing basket (2), a partition board (3), a biochemical disk type combination (4), an external container (7) of the biochemical disk type combination, and a water inlet hole (5) of the external container of the biochemical disk type combination. The separator also includes water outlets (8,9) of the external container of the biochemical disk type combination, an integrated oil water separator (13), an integrated oil water separator water outlet (12), a feeding groove (10) and a stainless steel cover board.    USE - Biochemical disk type integrated oil water separator used in the e.g. catering industry.    ADVANTAGE - The biochemical disk type integrated oil water separator combines slag removal, oil slick removal, free oil decomposition and feeding depth processing in the proper time and space so that contaminants such as the suspension, floating state grease, free state grease, biological oxygen quantity and chemical oxygen quantity in the oil sewage are removed. The oil dirt treatment problem of the oil sewage in the catering industry is effectively solved since it is suitable for the discharge of the oil sewage as well as for the discharge of the oil dirt of the oil sewage in the non-catering industry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biochemical disk type integrated oil water separator.    Integrated oil water separator water inlet (1)    Slag removing basket (2)    Partition board (3)    Biochemical disk type combination (4)    Water inlet hole (5)    External container (7)    Water outlets (8,9)    Feeding groove (10)    Integrated oil water separator water outlet (12)
NOVELTY - Invention relates to apparatus for neutralising and recycling highly concentrated organic wastes (deposits, sludge) arising from biological treatment of household waste water or waste water with similar composition. The apparatus for anaerobic processing of organic substrates into biogas and fertiliser has series-arranged collector of the initial substrate 1, hydrolysis apparatus 2, methane tank 6, effluent separator 13, thermal power unit for generating energy from biogas 22 and a boiler for burning solid hydrolysis wastes 17. The hydrolysis apparatus is fitted with an air bubbling device 3, between the methane tank and the effluent separator there is a floatation installation 9, the air bubbling device 10 of which, together with the air bubbling device of the hydrolysis apparatus, is connected to a compressor 19 with a gas-motor drive 20 operating on biogas, wherein the effluent separator 13 and the initial substrate collector are sealed, and their gas space, together the gas space of the hydrolysis apparatus and the floatation installation, is connected through a gas pipe to the gas boiler-recycler 16, which is in turn connected through a circulation line to the boiler for burning solid hydrolysis wastes, the gas-motor drive of the compressor and the thermal power unit for generating energy from biogas.    USE - Chemistry.    ADVANTAGE - Apparatus increases energy and environmental efficiency of the process of processing organic wastes into biogas and fertiliser. 1 dwg
NOVELTY - The tool (1) has a fuel cell generating electric power by oxidation reaction between a fuel i.e. hydrogen, and an oxidizing agent i.e. oxygen. A power drive source i.e. electric motor (3), receives the power to drive a tool portion i.e. chucking (3A). A water-holding unit i.e. water-holding tank (13), holds reaction water produced in the cell. A holder portion detachably holds the water-holding unit. A reaction water remover includes a reaction water outlet formed in the water-holding unit to discharge the reaction water held in the water-holding unit.    USE - Electric power tool for an electric motor.    ADVANTAGE - The reaction water produced in the fuel cell is held in the water-holding unit, so that the reaction water is inhibited from directly discharged from the electric power tool, thus inhibiting the user and work object from getting wet. The reaction water remover includes a reaction water outlet formed in the water-holding unit to discharge the reaction water held in the water-holding unit, thus avoiding accumulation of the reaction water in the water-holding unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an electric power tool.    Electric power tool (1)    Electric motor (3)    Chucking (3A)    Main body portion (5)    Handle portion (7)    Water-holding tank (13)
NOVELTY - A biomass processing apparatus (A1) consists of processes wood type biomass containing cellulose, hemicellulose, and lignin as main component. Water and carbon dioxide are mixed with biomass and held under conditions (I) in a pressurized hot-water processing tank (hemicellulose separation tank) (1) in which hemicellulose is solubilized by water and separated.    USE - Apparatus is used for processing wood type biomass containing cellulose, hemicellulose, and lignin as main component, to produce bioethanol.    ADVANTAGE - The apparatus enables economical processing of wood type biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass processing apparatus. (Drawing includes non-English language text)    Hemicellulose separation tank (1)    Cellulose saccharification tank (2)    Alcohol fermenters (3,6)    Hemicellulose saccharification tank (5)    Biomass processing apparatus (A1)
NOVELTY - A biomass material containing lignin is processed using pressurized hot water at 100 degrees C or more by a screw extruder (E) having a pressurized hot-water process portion (7). An upper seal portion (6) and a downstream seal portion (9) are provided in portion (7). The temperature of biomass material in portion (9) is less than the boiling point of liquid component of the system. The liquid component of biomass material in portion (9) is made to exist in liquid state, and the dwell pressure capability of portion (9) is increased.    USE - Continuous pressurized hot-water processing of biomass material containing lignin, cellulose and hemicellulose, to produce ethanol useful as fuel.    ADVANTAGE - The method improves the saccharification process efficiency of biomass material and enables continuous processing of biomass material.    DETAILED DESCRIPTION - A biomass material containing lignin is processed using pressurized hot water at 100 degrees C or more by a screw extruder having a pressurized hot-water process portion. An upper seal portion is provided in the upstream of hot-water process portion, and a downstream seal portion is provided in the downstream. The temperature of biomass material in the downstream seal portion is reduced to less than the boiling point of liquid component contained in the system. The liquid component contained in the biomass material in the downstream seal portion is made to exist in liquid state, and the dwell pressure capability of the downstream seal portion is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the screw extruder. (Drawing includes non-English language text)    Upper seal portion (6)    Pressurized hot-water process portion (7)    Cooler (8)    Downstream seal portion (9)    Screw extruder (E)
NOVELTY - An electrode for optical water-splitting reactions comprises photocatalyst particle (10) which consists of oxynitride, nitride, oxysulfide and/or sulfide, support body (20), and semiconductor or good conductor (30) which is provided between photocatalyst particles and between photocatalyst particle and support body.    USE - An electrode for optical water-splitting reactions used for production of hydrogen.    ADVANTAGE - The electrode has reduced internal resistance and improved photoelectric conversion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows an expanded sectional view of electrode for optical water-splitting reactions.    Photocatalyst particle (10)    Support body (20)    Semiconductor or good conductor (30)
NOVELTY - A biodiesel fuel container material contains ethylene-vinyl compound copolymer (II) (0.1-10 parts weight) with respect to polyethylene (I) (100 parts weight). The polyethylene (I) has density of 0.920-0.970 g/cm3, and melt flow rate of 0.1-100 g/10 minutes, measured at 190 degrees C and load of 21.6 kg. The ethylene-vinyl compound copolymer (II) is copolymer with ethylene (A) and vinyl compound (B) (i). The ratio of vinyl compound (B) with respect to total content of ethylene (A) and vinyl compound (B) is 0.001-2 mol%. The copolymer has melt flow rate of 0.1-200 g/10 minutes.    USE - Material is used for manufacturing biodiesel fuel container component (claimed). Uses include but are not limited to inside solution supply port, pipe, handle, fuel feed pump, reinforcement component, inlet, opening portion liner, lid, valve and removal opening.    ADVANTAGE - The biodiesel fuel container material has excellent mechanical strength, dissolubility-proof property, handleability, moldability and durability.    DETAILED DESCRIPTION - A biodiesel fuel container material contains ethylene-vinyl compound copolymer (II) (0.1-10 parts weight) with respect to polyethylene (I) (100 parts weight). The polyethylene (I) has density of 0.920-0.970 g/cm3, and melt flow rate of 0.1-100 g/10 minutes, measured at 190 degrees C and load of 21.6 kg. The ethylene-vinyl compound copolymer (II) is copolymer with ethylene (A) and vinyl compound (B) of formula (i). The ratio of vinyl compound (B) with respect to sum of ethylene (A) and vinyl compound (B) is 0.001-2 mol%. The copolymer has melt flow rate of 0.1-200 g/10 minutes, measured at 190 degrees C and load of 2.16 kg.    R1,R2=H or methyl;and    R3=H or 1-4C alkyl.
NOVELTY - The process involves pressing metal sheet and forming protrusion on both sides. The protrusions are pressed to excess dimension, where excess protrusion height is above metal sheet surface on either side of metal sheet. The metal sheet with excess dimensioned protrusion with layers having electrodes (102) and electrolyte are assembled to form fuel cell (100). The metal sheet provided with excess dimensioned protrusions layers electrodes and electrolyte, are calibrated to press. The protrusions are compressed to final dimension smaller than excess dimension.    USE - Process for manufacturing interconnect for fuel cell e.g. solid oxide fuel cell (both claimed). Can also be used in polymer electrolyte fuel cells (PEM) or direct methanol fuel cell (DMFC).    ADVANTAGE - The interconnect provides electrical and mechanical contact of good quality all over active area such that increased production tolerance on dimension and shape for components in fuel cell is ensured. The lift time is increased with lowered risk of malfunction of fuel cell and fuel cell stack. The electrical efficiency is ensured, and the internal electrical resistance is minimized in electrolyte, electrode and interconnect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of a fuel cell stack.    Fuel cell (100)    Interconnect (101)    Electrodes (102)    Spacer (107)    Gaskets (108)
NOVELTY - A modifier (50) generates hydrogen containing gas using source gas. A desulfurizer (13) removes sulfur compound in source gas to be supplied to modifier via path (16). A desulfurizer (21) hydrodesulfurizes sulfur compound in source gas to be supplied to modifier via route (17). Controller (101) controls switching unit (51) so that source gas flows through path (16) in pressure compensation operation for replenishing source gas to compensate for reduction in internal pressure after stopping operation for generating hydrogen-containing gas and source gas purging operation.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The source gas is replenished to compensate for reduction in internal pressure of modifier. The backward flow of undesulfurized source gas to recycle line can be prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Desulfurizer (13,21)    Route (16,17)    Modifier (50)    Switching unit (51)    Controller (101)
NOVELTY - A hydrodesulphurization unit (7) removes a sulfur compound in a source gas to be supplied to hydrogen generation unit. A recycling channel (10) supplies hydrogen-containing gas to source gas in a gas channel (5) in upstream of the hydrodesulphurization unit. A source gas supply unit (6) is arranged between hydrodesulphurization unit and merging portion of gas channel and recycling channel. An opening and closing valve (8) is arranged between source gas supply unit and hydrodesulphurization unit and is closed when hydrogen generator (100) is stopped.    USE - Hydrogen generator used in fuel cell system (claimed).    ADVANTAGE - The corrosion of the source gas supply unit provided between merging portion of recycle flow path, source gas supply path and hydrodesulfurization device can be suppressed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)    Gas channel (5)    Source gas supply unit (6)    Hydrodesulphurization unit (7)    Opening and closing valve (8)    Recycling channel (10)    Hydrogen generator (100)
NOVELTY - A hydrogen fuel-type fuel cell has a positive electrode catalyst layer, a gas diffusion layer and an oxygen gas flow path provided on one surface of a solid polymer electrolyte membrane in order, and a negative electrode catalyst layer, a gas diffusion layer and a hydrogen gas flow path provided on other surface of electrolyte membrane in order. The electrolyte membrane contains polymer having a sulfonic acid group, and a tin component chosen from a tin ion and a tin compound.    USE - Hydrogen fuel-type fuel cell.    ADVANTAGE - The hydrogen fuel-type fuel cell has stable electric power generation ability and favorable durability. The solid polymer electrolyte membrane has excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid polymer electrolyte membrane.
NOVELTY - A feed charge of carbonaceous gas is continuously divided into a feed gas flow (I,II). The flow (I) is charged into a primary solid oxide fuel cell to produce electricity, heat and carbon dioxide. The flow (II) is charged into a hydrogen gas forming reactor system to produce hydrogen and carbon dioxide. A portion of hydrogen gas is optionally charged into a secondary solid oxide fuel cell to produce electricity and heat, and hydrogen gas is reduced. Carbon dioxide in the primary fuel cell is optionally captured and carbon dioxide in reactor system is captured using absorbent.    USE - Production of energy in forms of electricity, hydrogen gas and heat.    ADVANTAGE - The energy in forms of electricity, hydrogen gas and heat is economically produced.    DETAILED DESCRIPTION - A feed charge of carbonaceous gas is continuously divided into a feed gas flow (I,II). The flow (I) is charged into a primary solid oxide fuel cell to produce electricity, heat and carbon dioxide. The other flow (II) is charged into a hydrogen gas forming reactor system to produce hydrogen and carbon dioxide. A portion of formed hydrogen gas is optionally charged into a secondary solid oxide fuel cell to produce electricity and heat, and net hydrogen gas is reduced. Heat developed in fuel cell is partially supplied to the hydrogen gas forming reactor system. Carbon dioxide formed in the primary fuel cell is optionally captured by burning afterburner gases in pure oxygen and drying the exhaust gas. Carbon dioxide in reactor system is captured by use of an absorbent. An INDEPENDENT CLAIM is included for device for production of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view illustrating production of energy.
NOVELTY - Method of converting gaseous hydrocarbon material into liquid fuel involves heating natural gas to obtain a mixture of synthetic gas from carbon dioxide, hydrogen and carbon monoxide, cooling the synthetic gas in a bioreactor in which synthetic gas undergoes fermentation in aqueous medium with anaerobic bacteria to obtain ethanol, which is then separated.    USE - Chemistry.    ADVANTAGE - Easier transportation of energy carriers from their extraction regions to consumers, including in cases when construction and use of gas pipelines is either unprofitable or is impossible, low power consumption. 6 cl
NOVELTY - Petroleum is added to ethanol using additive (I) consisting of zeolite and dolomite, and fragrance of Jatropha curcas as additive (II). Ethanol includes 5 vol.% of water and generated by dehydrating in the presence of a dehydrating additive consisting of kaolin and diatomite.    USE - Production of engine fuel for motor vehicles.    ADVANTAGE - The method enables production of engine fuels which can be used in various types of motor vehicles without changing the engine design, while ensuring the technical specifications of a fuel product and achieving high standards. The engine fuel is environmentally-friendly.
NOVELTY - The system has boil-off gas (BOG) reliquefaction plant comprising a cryogenic heat exchanger. A BOG compressor (2) comprises a BOG preheater (3) and a nitrogen loop with a compander (4). Gas feeding engines are in a form of liquefied nature gas (LNG) from a cargo tank (5) and/or condensate from the reliquefaction plant. A LNG optimizer (9) is arranged in front of a LNG evaporator (6) enabling heat exchange unit for warm and cold duty process in the BOG reliquefaction plant and LNG or condensate to be fed as gas into the engines.    USE - System for supplying gas such as LNG and liquid petroleum gas, to dual-fuel or gas engines and BOG reliquefaction.    ADVANTAGE - The system utilizes the cold duty process when LNG is warmed up before feeding the engines so as to cool and liquefy the boil-off gas and heat LNG before feeding the engine by using warm duty process as cooling water from the compressors in a reliquefaction system, thus reducing overall energy consumption in the system.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a system for supplying gas.    BOG compressor (2)    BOG preheater (3)    Compander (4)    Cargo tank (5)    LNG evaporator (6)    LNG optimizer (9)
NOVELTY - A manufacturing method of bioethanol involves immersing plant body containing cellulose in caustic potash of pH greater than or equal to 12 or aqueous solution of caustic soda, immersing plant body in citric acid aqueous solution of pH 1-5 and heating at 90-140 degrees C with citric acid aqueous solution, adjusting pH of citric acid aqueous solution of state which immersed plant body to not less than 5-7 by adding caustic potash or caustic soda to citric acid aqueous solution, adding Japanese radish to adjusted aqueous solution and fermenting liquid, and extracting ethanol from fermented aqueous solution.    USE - A manufacturing method of bioethanol used as alternative of petroleum-based fuel.    ADVANTAGE - The method obtains bioethanol from plant body efficiently and simply.
NOVELTY - A stirring apparatus (8) is rotated through stirring motor (10) using generated electric power, so that to-be-dried object (3) accommodated in dry process container is stirred. A fuel cell (200) is installed in airtight container (12), so that the heat generated by electric power generation is transmitted to dry process container (1) and the to-be-dried object in container is heated. The heat exchange fluid such as water (14) that is supplied to airtight container is heated with the heat generated by fuel cell.    USE - Drying system for drying to-be-dried object (claimed) such as foodstuff sludge, sewage sludge and animal excrement sludge.    ADVANTAGE - Since the heat generated by electric power generation is transmitted to dry process container, the structure of drying system is simplified. The to-be-dried object can be heated and dried independently. The need for providing steam generator is eliminated; the construction cost of drying system is reduced. The emission of exhaust gas is reduced, so that reliable driving process is achieved.    DETAILED DESCRIPTION - The heated fluid is supplied to container with fluid supply pipe. A jacket (29) is formed in outer periphery of dry process container. The heat exchange fluid is supplied to jacket and the to-be-dried object is heated from exterior.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the drying system. (Drawing includes non-English language text)    Dry process container (1)    To-be-dried object (3)    Stirring apparatus (8)    Stirring motor (10)    Airtight container (12)    Water (14)    Jacket (29)    Fuel cell (200)
NOVELTY - Method of producing alcohol by fermentation, involves selecting pulverized material of agricultural product chosen from citron seed, loquat seed, grape seed, sesame seed, ginger and Japanese ginger as active ingredient of fermentation, adding Gloriosa bulb or its extract and garlic tuber or its extract to the active ingredient and fermenting the obtained material by reinforcing alcohol fermentation ability of a microorganism at 33-40 degrees C.    USE - The method is useful for producing alcohol e.g. ethanol used for fuels.    ADVANTAGE - The method consumes less energy, produces alcohol without using apparatus for controlling temperature, cooling resource e.g. water and electric power for cooling process even at high temperature, maintains fermentation ability of microorganism for long period of time and improves fermentation rate, and is inexpensive. The method prevents production of carbon dioxide, hence controls global warming.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for alcohol, which is produced by above-mentioned method.
NOVELTY - An alcohol fermenting method involves reinforcing fermentation ability of alcohol fermentation microorganism by adding and fermenting ground material of citron seed, loquat seed, grape seed, sesame seed or garlic tuber, or its extract in alcohol fermentation ingredient.    USE - A fermentation method of alcohol used for fuels or foodstuff material.    ADVANTAGE - The method saves resources, improves fermentation rate, saves energy, and is efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of relationship of carbon dioxide gas generation amount and fermentation time. (Drawing includes non-English language text).
NOVELTY - A fat splitting microorganism belonging to genus Acinetobacter sp.SS-192 (NITE P-846) identified by national institute of technology and evaluation patent microorganisms depositary, is new. The microorganism has coccus cell form, diameter of 0.8-0.9 mu m, no spores, negative gram staining property, maneuverability, oxidase property, acid and gas production ability from glucose, and fermentation ability, positive catalase activity and oxidation ability and grows at 41 degrees C as mycological characteristics.    USE - The microorganism belonging to genus Acinetobacter sp.SS-192 (NITE P-846) is useful for preparing fat splitting agent (claimed) useful in waste water treatment for processing organic waste containing fats e.g. milk fat, lard and butter, and oils e.g. salad oil and soybean oil.    ADVANTAGE - The Acinetobacter improves optimal pH and temperature suitable for lipolysis in waste water treatment tank and hence increases optimal growth conditions of biological oxygen demand (BOD) decomposing microorganism in tank.
NOVELTY - An organic fertilizer comprises (wt.%) water hyacinth (60-66), grass peat (14-16), livestock manure (8-10), mushroom residue (8-10) and quicklime (4). The water hyacinth has water content of 30-35%.    USE - An organic fertilizer for crop, fruit tree and flower.    ADVANTAGE - The fertilizer has water content of 15-20%, reduces pollution, is rich in nutrition, does not have side effects, and has long lasting effect and long service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the organic fertilizer comprising drying and wetting the water hyacinth until the water content is 30-35%; crushing grass peat, livestock manure and mushroom residue; adding quicklime to the crushed material; adding processed water hyacinth; adding water; fermenting at 50-65 degrees C for 7-10 days; granulating the fermented product; and drying.
NOVELTY - The process involves dividing liquefied gas and liquid into water phase. Water phase is connected with a high-pressure pump and a discharging part from a bottom part of a three-phase separator. An oil phase is discharged from an outlet of biological oil in middle of the three-phase separator to form a product. A gas phase is discharged from a tail gas outlet on a top part of the three-phase separator as a fuel. A solid phase tar paste is discharged as an active carbon or fuel. The water phase is discharged and condensed to form a foliage application, a biological gasoline or a snow melt agent.    USE - High-pressure continuous tower type micro-algae liquefying process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high-pressure continuous tower type micro-algae liquefying process.
NOVELTY - The cell has an electronic medium added to green algae culture liquid for combining an electron generated during photosynthesis with the electronic medium through an electron transmission chain while reaching hydrogenase. Hydrogen generating green algae is suspended in the green algae culture liquid. The electronic medium releases the electron on an anode, and the electron is transmitted to a cathode by a battery external circuit, where the electronic medium is combined with proton of a proton exchange membrane and oxygen or oxidant in an anode pool on the cathode to generate water.    USE - Green algae biological fuel cell for generating power based on photosynthesis.    ADVANTAGE - The cell directly converts the optical energy into electric energy by performing microalgae photosynthesis and utilizing the battery system.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of a green algae biological fuel cell.
NOVELTY - Hydroprocessing a biocomponent feedstock to form a diesel boiling range product, comprises: treating a purge gas and/or an off-gas stream from an existing refinery reactor to remove hydrogen sulfide and carbon dioxide; and hydroprocessing a feedstock comprising a biocomponent portion in a reactor in the presence of the treated refinery stream, a catalyst with hydrogenation activity, and optionally steam under effective hydroprocessing conditions to produce a vapor effluent, an aqueous effluent, and the diesel boiling range product.    USE - The method is useful for hydroprocessing a biocomponent feedstock to form a diesel boiling range product (claimed) and an aqueous product.    ADVANTAGE - The feedstock and the treated refinery stream are substantially free of sulfur. The method is cost effective. The diesel boiling range product shows improved cold-flow properties.    DETAILED DESCRIPTION - Hydroprocessing a biocomponent feedstock to form a diesel boiling range product, comprises: treating a purge gas and/or an off-gas stream from an existing refinery reactor to remove hydrogen sulfide and carbon dioxide, where the treated refinery stream has a hydrogen content of 20-60, (preferably 25-50) mol.%; and hydroprocessing a feedstock comprising a biocomponent portion in a reactor in the presence of the treated refinery stream, a catalyst with hydrogenation activity, and optionally steam under effective hydroprocessing conditions to produce a vapor effluent, an aqueous effluent, and the diesel boiling range product.    DESCRIPTION OF DRAWING(S) - The figure shows a reaction system for a hydroprocessing a biocomponent feedstock.    Reactor (105)    Feed conduit (112)    Steam conduit (114)    Separator (135)    Hydrogen input. (147)
NOVELTY - Drying and gasifying a carbon-containing feedstock, involves: (a) combusting a fuel comprising methane to generate heat and a flue gas; (b) drying the carbon-containing feedstock, at least in part, using at least a portion of the flue gas, by generating a dried feedstock; (c) gasifying the dried feedstock to generate a gas stream comprising syngas, where the gasifying includes introducing at least some of the heat from step (a).    USE - For drying and gasifying a carbon-containing feedstock (claimed).    ADVANTAGE - The method economically optimizes both drying and gasification, and combines it into a single step.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for drying a carbon-containing solid feedstock, comprising: a vessel; a primary channel for flowing the solid feedstock and a gas for drying the solid feedstock; a secondary channel for flowing the gas; and several internal screens or sieve plates in communication with the primary channel and the secondary channel, where the internal screens or sieve plates are suitable for passage of the gas but not for substantial passage of the solid feedstock.    DESCRIPTION OF DRAWING(S) - The figure shows a sketch of an apparatus.
NOVELTY - The apparatus has a housing which includes a side wall, reactant-storage chamber and reaction chamber. A piston is arranged within the housing between the reactant-storage chamber and reaction chamber. A reactant-discharge port extends into the reactant-storage chamber. A device urges the piston toward the reactant-storage chamber. The reactant-entry port extends into the reaction chamber through side wall of housing. The sodium tetrahydroborate is arranged in the reactant-storage chamber. Ruthenium, cobalt, nickel and platinum are arranged in reaction chamber.    USE - Apparatus for power supply for hydrogen production system (all claimed).    ADVANTAGE - The control unit allows a selective activation of the cartridge in relation to the need for power. Since cartridges with extremely reduced sizes or considerable sizes may be realized, the versatility of use is achieved. The amount of gaseous hydrogen produced in relation to the parameterization of the spring of the piston element is regulated. The characteristics of rigidity and length of the spring are chosen so that transfer of the reactant into the reaction chamber through the fluidic conduit with a constant capacity in time is realized, when the volume of the reactant is extremely reduced. Since the cartridge generates gaseous hydrogen transforming mechanical energy, the ability to recharge electronic devices or generate energy with the help of hydrogen motors without the use of the main electric network, is improved. The control unit allows blocking and re-activating the production of gaseous hydrogen on demand.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) power supply;    (2) system for hydrogen production; and    (3) method for production of gaseous hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the cartridge application.    Cartridge (10)    Fluidic conduit (40)    Supplier (500)    Conduit (505)    Fuel cell block (510)
NOVELTY - Separating carbon dioxide from a mixture of carbon dioxide and methane involves contacting the mixture and a porous organic polymer material having a three dimensional structure containing three dimensional building blocks where the material selectively adsorbs carbon dioxide.    USE - For separating carbon dioxide from a mixture of carbon dioxide and methane (claimed).    ADVANTAGE - The polymer material selectively adsorbs carbon dioxide from a room temperature mixture of carbon dioxide and methane; is effective at relatively low bulk gas pressures and high mole fractions of methane in the mixture; and selectively removes carbon dioxide from natural gas, landfill gas, and gas mixtures of carbon dioxide and methane.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a porous organic polymer that absorbs carbon dioxide comprising tetrahedral building blocks; or three dimensional building blocks linked by imide linkers; and    (2) making a porous organic polymer where the polymer is made by condensation of a three dimensional monomer with an imide linkage-forming monomer to form a three dimensional polymer structure that selectively absorbs carbon dioxide.
NOVELTY - A carburetion agent contains 6-80 mol% of propane and 40-20 mol% of butane.    USE - Agent for carburetion of gaseous fuel (claimed) e.g. town gas and industrial gas.    ADVANTAGE - Liquefaction of carburetion agent component in town gas is prevented. The carburetion agent component is not separated by supply pipe interior.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) carburetion method; and    (2) gaseous fuel carburetion apparatus.
NOVELTY - A biomass gasification electric power generating apparatus comprises energy gas making and electric power generating apparatus which produces energy gas and converts it into electric power, consists of storage part, reaction part, energy gas storage part, and electric power generation unit.    USE - Biomass gasification electric power generating apparatus for moving body (claimed) such as hybrid vehicle.    ADVANTAGE - Steam modification is unnecessary, tar build-up is prevented, and fuel consumption of moving body is improved.    DETAILED DESCRIPTION - A biomass gasification electric power generating apparatus comprises energy gas making and electric power generating apparatus which produces energy gas and converts it into electric power, consists of storage part which temporarily stores biomass fuel which contains carbon, hydrogen and oxygen-containing compound, and an alkali metal and/or alkaline earth metal (compound), reaction part which heats the biomass fuel stored in the storage part to generate energy gas, energy gas storage part which stores energy gas generated in the reaction part, and electric power generation unit which supplies energy gas stored in the energy gas storage part to a fuel cell, and converts the energy gas into electric power. An INDEPENDENT CLAIM is included for moving body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the energy gas making and electric power generating apparatus. (Drawing includes non-English language text).    Moving body (10)    Biomass gasification electric power generating apparatus (30)    Energy gas making and electric power generating apparatus (40)    Storage part (50)    Reaction part (60)    Energy gas storage part (80)    Electric power generation unit (90)
NOVELTY - Production of proton comprises: obtaining a proton from a hydrogen molecule by making hydrogen gas contacting a ferroelectric substance and dissociating, the ferroelectric substance is a microcrystal powder which has a cleavage plane.    USE - The method is useful for producing proton (claimed).    ADVANTAGE - The method is cost effective and highly efficient in producing proton.
NOVELTY - The apparatus (10) has water supply and discharge communicating holes (46,48) that are extended in lamination direction of separators (34,36) of unit cell (12) for supplying/discharging water to/from water flow path (54) respectively. The supply and discharge communicating holes are provided symmetrically and hydrogen communicating hole (50) is positioned in a virtual line orthogonal to imaginary line connecting the supply and discharge communicating holes.    USE - Electrochemical apparatus e.g. water electrolysis apparatus for manufacturing hydrogen gas.    ADVANTAGE - The sealing pressure of the supply and discharge communicating holes can be maintained equally and fall of sealing performance of the electrochemical apparatus can be avoided with simple structure. Variation in pressure of the unit cell can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the water electrolysis apparatus.    Water electrolysis apparatus (10)    Unit cell (12)    Separators (34,36)    Water supply communicating hole (46)    Water discharge communicating hole (48)    Hydrogen communicating hole (50)    Water flow path (54)
NOVELTY - A biomass pyrolysis furnace comprises a furnace shell, an internal furnace, a steam discharge pipe, a smoke pipe, a recovery tower, a steam discharge pipe, an air inlet pipe, and a smoke pipe apparatus; where the internal furnace is set in the furnace shell; multiple meshes are mounted at the top, bottom, and four surfaces of the internal furnace; a steam exhaustion layer is mounted between the internal furnace and the inner wall of the furnace shell; and one end of the smoke pipe is connected with the furnace shell while the other end is connected with the recovery tower.    USE - The biomass pyrolysis furnace is useful for industrial and commercial applications.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass pyrolysis furnace.
NOVELTY - A pyrolysis system super-thermally spraying biomass, comprises a sample feeding device, a reacting device, and a condensing device; where the sample feeding device is used for conveying air-carried biomass powder into the reacting device; the reacting device is used for processing instant pyrolysis of the biomass powder; and the condensing device (9) is set with a vacuum cavity used for receiving airflow produced by the pyrolysis of the biomass powder and quickly decreasing the temperature by the airflow in the vacuum cavity.    USE - The pyrolysis system super-thermally spraying biomass is useful for industrial and commercial applications.    ADVANTAGE - The pyrolysis system super-thermally spraying biomass has fast heating speed and good cooling effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the pyrolysis system super-thermally spraying biomass.    Air intake pipe (1)    Pulse valve (2)    Pulse valve outlet (3)    Silicon carbon tube (5)    Condensing device (9)
NOVELTY - Forming fuel blend involves: providing a source of bio-based feedstock; treating the bio-based feedstock so as to form a carbohydrate; reacting the carbohydrate in a hydrogenolysis reaction to produce reaction products comprising an alcohol, a polyol, and a higher polyol; recycling the higher polyol through the hydrogenation reaction to produce reaction products comprising an alcohol and a polyol; and processing at least a portion of the reaction products to form a fuel blend.    USE - For forming fuel blend comprising at least one composition selected from: a fuel additive, gasoline fuel, diesel fuel, and jet fuel (claimed); for the production of higher hydrocarbons, which are used in transportation fuels and industrial chemicals.    ADVANTAGE - The method minimizes the formation of undesirable by-products such as coke, carbon dioxide and carbon monoxide, thus improving the overall yield of converting carbohydrates to higher hydrocarbons. The methods have advantage of converting bio-based feed stocks, optionally without any additional costly purification steps to form higher energy density product of lower oxygen/carbon ratio including higher alkanes, olefins and aromatics; reduces capital costs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) forming fuel blend involving: providing a carbohydrate; reacting the carbohydrate directly with hydrogen in the presence of a hydrogenolysis catalyst to produce a reaction product comprising a polyol; and processing at least a portion of the reaction product to form a fuel blend; and    (2) a system comprising: a first vessel for receiving a carbohydrate and producing a hydrogenated product; a second vessel for receiving the hydrogenated product and producing an alcohol and a polyol; and a processing reactor for reacting the alcohol and polyol in the presence of a catalyst to produce a fuel blend.
NOVELTY - A fermenting pot of microorganism bacteria culture medium, comprises a pot body (1), a feeding opening (2) that is arranged on the upper part of the pot body (1), and an electric heater (3) that is also arranged in the pot body (1); where a material liquid outlet (5) and a sewage draining port (6) are arranged on the lower part of the pot body (1); the pot body (1) is set with a gas feeding pipe (7) connected with the inner part; and a material hanging bag (8) is fixed on the upper part of the pot body (1).    USE - The fermenting pot is useful for microorganism bacteria culture medium (claimed).    ADVANTAGE - In the fermenting pot, the material hanging bag is fixed on the upper part of the pot body; thus, the powder and the liquid are completely mixed; the powder is not deposited; the raw material is saved; and the fermenting effect is improved. Moreover, the whole structure of the device is good; the structure is simple; and the use effect is good.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fermenting pot of microorganism bacteria culture medium.    Pot body (1)    Feeding opening (2)    Electric heater (3)    Material liquid outlet (5)    Sewage draining port (6)
NOVELTY - The engine has a fuel engine body provided with an engine air intake that is connected to a biomass energy generator to generate combustible gas through pipelines. The biomass energy generator is provided with an anaerobic combustion chamber. An air outlet of the anaerobic combustion chamber is connected with a gas impurity elimination device that is connected to a gas outlet for the processed gas of the engine air intake. The gas impurity elimination device is provided with a cooling drift eliminator and a filtering dust catcher that are orderly connected in series.    USE - Biomass and oil mixed fuel engine.    ADVANTAGE - The engine ensures in purifying the combustible gas generated from the biomass energy generator, so as to pass through the air intake system. The engine has low fuel consumption and low greenhouse gas emission by using renewable biomass energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biomass and oil mixed fuel engine. ' (Drawing includes non-English language text) '.
NOVELTY - The gasifier has an air feed pipe (6) connected with an oxygen distribution pipe (5) that is connected with a furnace chamber (4). The furnace chamber is arranged in a center part of a cover (3). A lower part of the furnace chamber is suspended at an inner side of a furnace (7). The lower part of the furnace chamber is provided with a cracking converter (22). An outer end of the cracking converter is provided with a filter cap (15) in which a nickel base catalyst sheet (14) and an activated aluminum oxide molecular sieve (13) are arranged in sequence manner.    USE - Biomass gasifier.    ADVANTAGE - The furnace chamber is arranged at the inner side of the furnace, and high-temperature gas can be supplied to the furnace chamber directly without a pipeline convey so as to raise the burning efficiency and reduces loss and avoids production of oil tar. The gasifier is compact in structure, occupies less area, simple to operate, and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasifier.    Cover (3)    Furnace chamber (4)    Oxygen distribution pipe (5)    Air feed pipe (6)    Furnace (7)    Activated aluminum oxide molecular sieve (13)    Nickel base catalyst sheet (14)    Filter cap (15)    Cracking converter (22)
NOVELTY - The furnace has a water ring belt arranged outside a smoke-fire passage. A heat absorbing chamber is divided into a heat absorbing chamber part on a lower part of the water ring belt and another heat absorbing chamber part located on an upper part of the water ring belt. The heat absorbing chamber parts are connected together by the smoke-fire passage. The smoke-fire passage is formed vertical to a cavity of a secondary air ring belt that is arranged on a connection part of a combustion chamber and the heat absorbing chamber.    USE - Direct-combusted semi-gasification furnace.    ADVANTAGE - The furnace can utilize the secondary air ring belt for supplying oxygen for combusting a straw in time. The combustion chamber can be effectively separated from the heat absorbing chamber so as to control directions of smoke and flame. The furnace utilizes a tube with increased flue length, so that the water in the tube can completely absorb the heat in the hot smoke.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a direct-combusted semi-gasification furnace.
NOVELTY - The device has a biomass gasifying furnace (1) whose gas is transmitted to multiple burners (4) via a gas pipe (2). The burner is installed in a pipe of a radiating tube (3). A tail part of the radiating tube is provided with a smoke discharging cylinder (5) that is provided with a smoke discharge turning plate (6).    USE - Direct heating type biomass gasifying furnace warming device.    ADVANTAGE - The device is simple to manufacture, install and detach and inexpensive, and has flexible utilization and effective warming process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a direct heating type biomass gasifying furnace warming device.    Biomass gasifying furnace (1)    Gas pipe (2)    Radiating tube (3)    Burners (4)    Smoke discharging cylinder (5)    Smoke discharge turning plate (6)
NOVELTY - The manufacturing method involves forming a fuel electrode by compacting, and controlling the recessed portion incidence rate in the surface of the fuel electrode to 2 % or less. An electrolyte layer (13) is formed on the fuel electrode. The fuel electrode with the electrolyte layer is then baked.    USE - Manufacturing method for fuel cell.    ADVANTAGE - Enables controlling the shape of the surface of the fuel electrode before baking, thus suppressing the peeling of the electrolyte layer from the fuel electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of a fuel cell.    Fuel cell (1)    Electrolyte layer (13)    Air electrode (14)    Current collection layer (16)    First opening (121)
NOVELTY - The apparatus (1) has a carbonic acid trapping part (2) acquiring carbonic acid containing in fermented liquor. The fermented liquor is sampled from a fermenter to solid-phase as a slightly soluble salt by adding a basic carbonic acid trapping agent i.e. magnesium compound. A volatile-organic-acid diffusion part (4) adds sulfuric acid to liquid phase after solid-liquid separation, and diffuses volatile organic acid in gaseous phase. A fixed-quantity part (5) quantifies volatile-organic-acid density in the gaseous phase.    USE - Apparatus for monitoring a volatile-organic-acid density in a fermented liquor i.e. digestive liquid, inside of a fermenter i.e. methane-fermentation tank, to process an organic waste e.g. excrement, organic refuse and food-processing residue.    ADVANTAGE - The apparatus can monitor the volatile-organic-acid density in the fermented liquor correctly, thus stabilizing the fermentation process, and increasing in the yield of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for monitoring volatile-organic-acid density in fermented liquor.'(Drawing includes non-English language text)'    Monitoring apparatus (1)    Carbonic acid trapping part (2)    Solid-liquid separation part (3)    Volatile-organic-acid diffusion part (4)    Fixed-quantity part (5)
NOVELTY - Waste-water treating agent comprises nitrate and nitrite, or nitrate, nitrite and an extract comprising activated sludge in an aqueous solution, which is aerated or sufficiently provided with nitrate.    USE - The waste-water treating agent is useful for rapid elimination of putrefaction bacteria.    ADVANTAGE - The waste-water treating agent: accelerates the elimination of sulfate-reducing bacteria; and prevents formation of toxic and foul-smelling hydrogen sulfide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for rapid elimination of putrefaction bacteria, comprising adding waste-water treating agent.
NOVELTY - Method for producing solid organic waste, involves using organic waste as fermentation base material and anaerobic digested sludge containing fungi as inoculation agent, and adding a composite material to the mixture in anaerobic conditions.    USE - The method is useful for producing solid organic waste for producing methane.    ADVANTAGE - The method adopts absorptive and melting properties, and biological activity of composite material to remove restraint, and hence growth environment of microorganism and yield of methane are improved. The composite material is inexpensive, abundant resources, and convenient to process.
NOVELTY - A digester (1) for production of biogas in a dung pit (2) containing biological material, comprises a dung pit having a bottom (5), a roof covering the dung pit, and at least one insulating element (4, 4'), which is placed on the bottom of the dung pit and at least partly insulates the bottom of the dung pit.    USE - As a digester for production of biogas in a dung pit containing biological material (claimed) such as manure.    ADVANTAGE - The digester is simple and inexpensive equipment for production of biogas; enables economically profitable production of biogas at a farm; enables efficient degradation of biological material; enables a high content of methane in produced biogas; enables production of biogas in an existing dung pit without having to empty the dung pit before starting biogas production in the dung pit; enables production of biogas without a digestion tank; and enables reduction of emission of methane and ammonia from a dung pit into the ambient air.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of biogas in a dung pit containing biological material involving collecting produced biogas at the roof covering the dung pit; and    (2) converting a dung pit containing biological material to a digester for production of biogas involving immersing at least one insulating element into the dung pit; placing at least one insulating element on the bottom of the dung pit; and covering the dung pit with a roof.    DESCRIPTION OF DRAWING(S) - The figure shows a top view of a digester.    Digester (1)    Dung pit (2)    Insulating material (4, 4')    Bottom (5)    Guiding units (8, 8')    Recirculation units (11, 11')    Wall (14)
NOVELTY - A slotless solid stick mechanical bar is obtained by forming solid bar on a surface without slot. The slotless solid stick mechanical bar comprises wood powder and bamboo powder.    USE - Slotless solid stick mechanical bar.
NOVELTY - The electrolysis control system (1) comprises an electronic controller (4) that includes a shaped current waveform generator and a current control device coupled to the vessel output port (34). An electrode assembly (12) is arranged in the housing to store an electrolyte solution. The shaped current waveform generator is arranged to cause the current control device to periodically couple the cathode to the ground to pass current through the electrolyte solution and generate gases.    USE - Electrolysis control system for generating gases e.g. hydrogen gas used for internal combustion engine of vehicles (both claimed) like motor vehicle, or stationary engine applications, etc.    ADVANTAGE - The system provides highly efficient energy transfer between electrical power source and electrolysis units through the use of the shaped current waveform generator and a non-inductive ohmic load. The fuel consumption and exhaust emissions of the engine can be reduced, by supplying hydrogen gas generated by the electrolysis control system. The ohmic load reduces electrode degradation and helps control runaway current by providing a stable ultra-low or low impedance load to the current control circuit during electrolysis. When the ohmic load is used with the waveform generator, the load curbs overshoot and ringing, even at high current drive providing more efficient power delivery to the electrolysis process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of enhancing combustion of internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrolysis control system.    Electrolysis control system (1)    Electronic controller (4)    Electrode assembly (12)    Transfer hose (18)    Vessel output port (34)
NOVELTY - A purified propane purge stream is recovered by fractionating in first distillation column (1) a feed stream comprising 2-10 wt.% methanol, 5-20 wt.% propylene, and 70-90 wt.% propane, to separate the feed stream into first light product stream and first heavy product stream; and fractionating the first heavy product stream in second distillation column (2) at 220-258 psia to separate the first heavy product stream into second light product stream and second heavy product stream.    USE - Method for recovering purified propane purge stream (claimed).    ADVANTAGE - The method uses 2 distillation steps, one of which is below methanol-propane azeotrope, which makes it possible to separate propane from methanol and propylene in an economical way.    DETAILED DESCRIPTION - Recovering purified propane purge stream comprises fractionating in first distillation column (1) a feed stream comprising 2-10 wt.% methanol, 5-20 wt.% propylene, and 70-90 wt.% propane, to separate the feed stream into first light product stream and first heavy product stream, the first heavy product stream comprising less than 1.5 wt.% propylene, and an amount of methanol that is greater than or equal to 70 wt.% of the methanol present in the first distillation column feed stream; and fractionating the first heavy product stream in second distillation column (2) at 220-258 psia to separate the first heavy product stream into second light product stream and second heavy product stream, the second light product stream comprising greater than or equal to 96 wt.% propane and less than 1 wt.% methanol. Propane in the second light product stream is 20-45 wt.% of the propane present in the first distillation column feed stream.    DESCRIPTION OF DRAWING(S) - The drawing is a process flow diagram of distillation columns and associated equipment.    First distillation column (1)    Second distillation column (2)    Reboiler (3)    Condenser (4)    Accumulator drum (5)
NOVELTY - The apparatus (10) has pair of current collectors which are located on opposite sides of electrolyte element. Pair of separators is stacked on current collectors. Water flow field for supplying water is defined between collectors and separators. Hydrogen flow field produced hydrogen through electrolysis. Water supply passage (46) and discharge passage (48) are extended along stacked direction. Inlet joint channels interconnected supply passage and flow field. Passage included outer and inner wall surfaces jointly formed opening of oblong cross-sectional shape.    USE - Water electrolysis apparatus e.g. high-pressure hydrogen manufacturing apparatus used to generate hydrogen gas for use as fuel gas for solid polymer electrolyte fuel cell.    ADVANTAGE - The pressure loss in the water flow field can be reduced suitably and the water can flow efficiently and economically. The entire water flow field can be uniformly and reliably supplied with water for an efficient water electrolysis process. The apparatus is simple in structure and water can be prevented from flowing preferentially into the central area of the water flow field. Since unreacted water and generated oxygen exit in the outlet joint channels and the volume increases accordingly, the pressure loss in the outlet joint channels can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the water electrolysis apparatus.    Water electrolysis apparatus (10)    Unit cells (12)    Stack assembly (14)    Water supply passage (46)    Discharge passage (48)
NOVELTY - Converting a free fatty acid containing feedstock to hydrocarbon, comprises: (a) providing a feedstock comprising at least one free fatty acid; (b) reacting the feedstock with ammonia/amine to produce a first product mixture comprising solid fatty amide; (c) subjecting the product mixture to a separation device, where the solid fatty amide is separated from the first product mixture; and (d) reacting the solid fatty amide with a hydroprocessing catalyst in a reaction zone under a condition sufficient to produce a second product mixture comprising hydrocarbon and ammonia.    USE - The process is useful for converting a free fatty acid containing feedstock to hydrocarbon including gasoline, naphtha, jet fuel, kerosene, diesel fuel, light cycle oil, vacuum gas oil, atmospheric gas oil and/or atmospheric tower bottom (all claimed).    ADVANTAGE - The process: provides feedstock suitable for traditional hydroprocessing in the refinery by overcoming high total acid number present in low-cost renewable feedstocks; provides value to waste by-product of the food industry avoiding the food versus fuel debate for biofuels; provides solid amide which is physically separable from reaction mixture while retaining its solubility in hydrocarbon enabling further conversion into fuel range hydrocarbons; allows recycling of ammonia/amine utilized; and eliminates need of additional ammonia or other chemicals required for the pretreatment process once it is initiated.
NOVELTY - Converting carbohydrates to polyols and gasoline boiling range hydrocarbons comprises: (a) contacting a zinc-platinum or cobalt-molybdenum impregnated zeolite catalyst (ZnPt-zeolite or Co-Mo-zeolite) with a carbohydrate or polyol; (b) reacting the carbohydrate or polyol on the catalyst to produce polyols and hydrocarbons; and (c) separating the polyols and hydrocarbons, where the hydrocarbons are in the gasoline boiling range of -20 to 220 degrees C.    USE - The method is useful for converting carbohydrates to polyols and gasoline.    ADVANTAGE - The method provides decreased coke formation, increased catalyst life, and reduced byproducts such as carbon monoxide, and carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for converting polyols to gasoline boiling range hydrocarbons comprising: (a1) contacting a zinc-platinum or cobalt-molybdenum impregnated zeolite catalyst with a polyol, or contacting a leached zeolite catalyst impregnated with zinc, cobalt, molybdenum, and/or platinum; (b1) reacting the polyol on the catalyst to produce hydrocarbons; and (c1) purifying the hydrocarbons from the reaction (b), where the reaction temperature is 400-550 degrees C, and the reaction pressure is 1-250 psig, and the feedstock flow rate is 0.1-5 ml/hour/g catalyst.
NOVELTY - Preparing cephradine, comprises: (a) converting D-dihydrophenylglycine (DHPG) into an activated form (DHPGa); and (b) reacting 7-aminodesacetoxy-cephalosporanic acid (7-ADCA) with DHPGa in the presence of an enzyme in an aqueous reaction mixture to form cephradine, where the steps (a) and (b) are carried out under anaerobic conditions.    USE - The process is useful for preparing cephradine.    ADVANTAGE - The cephradine: has less than 5% of cephalexin, an absorbance at 450 nm of below 0.2; provides a high color stability in the stress stability test, i.e. the coloration of the cephradine hydrate is below 0.20 at an absorbance of 450 nm after 8 weeks of storage at 40 degrees C at a relative humidity of 75%, and/or no or substantially no organic solvents, preferably the cephradine hydrate contains less than 100 ppm of N,N-dimethylformamide and/or less than 200 ppm dichloromethane. The process is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cephradine obtainable by the process.
NOVELTY - A gas oil composition (C1) comprises at least one gas oil (5-79.9 vol.%), at least one diethyl carbonate (0.1-20 vol.%), and at least one hydrotreated vegetable oil (20-75 vol.%), where the diethyl carbonate is obtained from bio-ethanol.    USE - As gas oil composition useful as fuel for diesel engines (claimed).    ADVANTAGE - The diethyl carbonate increases the percentage of components of a biological origin in the compositions comprising gas oil and hydrotreated vegetable oil (HVO) in high amounts; and improves some of the characteristics such as, density and the cetane number. The addition of diethyl carbonate does not negatively influence the other characteristics of compositions comprising gas oil and hydrotreated vegetable oil (HVO) in high amounts, such as, cold properties such as the cloud point (CP) and the cold filter plugging point (CFPP). The diethyl carbonate allows the absence of oxygen in compositions comprising gas oil and hydrotreated vegetable oil (HVO) in high amounts, to be compensated, and reduces the particulate matter emissions (PM). The gas oil has a density, at 15 degrees C, determined according to the standard EN ISO 3675:1998 of 800-870 (preferably 820-850) kg/m3; a flash point, determined according to the standard EN ISO 2719:2002, of greater than or equal to 55 degrees C (preferably greater than or equal to 65 degrees C); and a cetane number, determined according to the standard EN ISO 5165:1998 of greater than or equal to 49 (preferably greater than or equal to 51). The hydrotreated vegetable oil (HVO) has a density, at 15 degrees C, determined according to the standard EN ISO 3675:1998 of 720-820 (preferably 750-800) kg/m3; and a flash point, determined according to the standard EN ISO 2719:2002 of greater than or equal to 55 degrees C (preferably greater than or equal to 65 degrees C).
NOVELTY - The apparatus (1) has several tube shaped cathodes that are arranged concentrically with respect to central anode. Tube shaped cathodes are arranged at certain pitch within elongated tubular housing (2) and connector element is provided within tubular housing for electrically connecting tube shaped cathodes. One connector (11) is attached to connector element that reaches through a lid (4). Neutral conductive tube is placed between two consecutive tube shaped cathodes, and is placed between rod-like anode and tube shaped cathode surrounding rod-like anode.    USE - Apparatus for on demand production of hydrogen used as fossil based-fuel for internal combustion engine of vehicle.    ADVANTAGE - The on demand production of hydrogen having compact design can be performed easily and safely and the high production rate of hydrogen can be ensured. The neutral conductive tube is placed between two consecutive tube shaped cathodes, and is placed between rod-like anode and tube shaped cathode surrounding rod-like anode, thus the number of the tube shaped cathodes, the number of the neutral conductive tubes and the distance between the neutral conductive tubes can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for on demand production of hydrogen.    Apparatus for on demand production of hydrogen (1)    Elongated tubular housing (2)    Nozzle (3)    Lid (4)    Connector (11)
NOVELTY - The sewage treatment system has uplink flow water collection branches (43) and downlink flow water distribution branches (32) which are alternately installed in forward and backward direction. A group of water inlet holes with downward openings is installed by spacing 50 to 150 millimeters on the pipe body of each uplink flow water collection branch. An uplink flow water outlet valve (54) is sealed, fixed and connected at the water outlet of the uplink flow water outlet main pipeline (44), and located at the exterior of the pool body (10).    USE - Sewage treatment system for artificial wet land of vertical flow and under flow type.    ADVANTAGE - Effectively prevents and delays blocking of artificial wet land through alternately changing flow direction of sewage in substrate. Maintains better hydraulic power conductivity and stable removing rate in long time of operation process. Stabilizes sewage treatment efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the sewage treatment system of artificial wet land of vertical flow and under flow type.    Exterior of the pool body (10)    Downlink flow water distribution branches (32)    Uplink flow water collection branches (43)    Uplink flow water outlet main pipeline (44)    Uplink flow water outlet valve (54)
NOVELTY - Culturing active sludge comprises: feeding active sludge into a sequencing batch reactor (SBR), adding a part of bean product waste water, adding clean water to a preset water level, adding glucose as a microbial carbon source, potassium dihydrogen phosphate as a phosphorus source, urea as a supplementary nitrogen source and a nutrient solution, aerating for 2 days, allowing to stand for 2 hours, feeding water once a day, culturing, acclimatizing the sludge with different concentrations of water load, where the active sludge is dry sludge obtained after dehydrating by polyacrylamide (PAM).    USE - The method is useful for culturing active sludge.    ADVANTAGE - The method: produces the active sludge with a simple acclimatization, a high sludge settling ratio (SV30) of 25-40% and high sludge volume index (SVI) of 70-90; and produces sludge which contains zoogloea, Vorticella microstoma, small worms, Branchinella and Litonotus.
NOVELTY - Efficient preparation of biomass, comprises growing biomass under carbon dioxide concentration of at least 410 vol. ppm at ambient atmosphere and adding ammonium compounds to the roots, where both the steps are carried out independently during at least half of the growing season.    USE - The method is useful for producing biomass, which is converted (by combustion) into thermal energy and/or electricity and is further processed to paper or building materials (all claimed).    ADVANTAGE - The addition of ammonium compounds to the roots increases the consumption of carbohydrates.
NOVELTY - Preparation of microbiological composition from food wastes, involves crushing collected food wastes through a crusher, maintaining at 68-100 degrees C for 20-40 minutes, sterilizing at high temperature, cooling to 30-50 degrees C, adding carrier (10-200 wt.%) and probiotics (10-50 wt.%), completely mixing the ingredients, anaerobically fermenting mixture in solid fermentation tank, and airing the fermented food wastes and carrier after fermentation to obtain high value microbiological composition having viable bacterial content of more than 500000000/g.    USE - Preparation of microbiological composition from food wastes containing rice, noodles, vegetables, oils and fats, fruits, meat and bone.    ADVANTAGE - The composition is prepared by completely using food wastes and the preparation process generates no pollutants.    DETAILED DESCRIPTION - Preparation of microbiological composition from food wastes, involves crushing collected food wastes through a crusher, maintaining at 68-100 degrees C for 20-40 minutes, sterilizing at high temperature, cooling to 30-50 degrees C, adding carrier (10-200 wt.%) and probiotics (10-50 wt.%), completely mixing the ingredients, anaerobically fermenting the mixture in solid fermentation tank, and airing the fermented food wastes and carrier after fermentation to obtain high value microbiological composition having viable bacterial content of more than 500000000/g, where the fermentation is performed at 25-40 degrees C for 1-3 days with stirring for 3 times/day.
NOVELTY - Agrochemical wastewater processing involves chemical dephosphorization, iron-carbon (Fe-C) microelectrolysis, Fenton oxidation, and catalytic oxidation of wastewater; and aerobic biochemical treatment in the presence of salt-resistant aerobic bacteria.    USE - Method for processing agrochemical (imidacloprid) wastewater (claimed).    ADVANTAGE - The method not only improves total physical processes, but also performs physical pretreatment at normal temperature and normal voltage to break difficult-to-degrade organic materials at low cost, thus, improving biochemical property of wastewater, reducing dilution factors of wastewater, and reducing water for dilution by 50-80%; is more economical than existing method; and has simple pre-processing step, mild and stable reaction conditions, simple operations (such as catalytic oxidation can be performed at normal temperature and normal pressure and the catalyst can be recycled), low running cost, and good processing effect. The subsequent biochemical dilution uses small amount of water but has low total processing cost, and the biochemical effluent can reach the national Grade 1 emission standard.
NOVELTY - The two-phase anaerobic and membrane biological processing tank has regulating water box storing organic wastewater to be processed, material feeding pump, hydrolyzing-acidifying reactor, anaerobic reactor, acidifying reactor, acid producing reactor, biochemical reactor, membrane bioreactor, material feeding pipe, regulator and three-phase separator. The anaerobic reactor and membrane bioreactor regulate and control running parameters of acid producing reactor and methane producing reactor.    USE - Two-phase anaerobic and membrane biological processing tank for high-concentration refractory organic wastewater.    ADVANTAGE - Provides economical and efficient processing technology combining wastewater treatment with energy recycling while requiring small floor occupation and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the two-phase anaerobic and membrane biological processing tank of high-concentration refractory organic wastewater. (Drawing includes non-English language text).
NOVELTY - The automatic water pollution processing device has biological contact oxidation pool which is connected with sedimentation pool via pipe. The biological contact oxidation pool is connected with oxygen feeding system. The livestock plane source sewage collecting pool is provided with a water flow detecting head. The aerating device and oxygen feeding system arranged in the biological contact oxidation pool are respectively electrically connected with the PLC control system.    USE - Automatic water pollution processing device for livestock plane source.    ADVANTAGE - Automatically tracks and displays the water quality and the water flow of the inlet sewage. Synchronously displays the operation frequency, operation current, air quantity of the oxygen supply fan.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the automatic water pollution processing device for livestock plane source. (Drawing includes non-English language text).
NOVELTY - Green agriculture circulation production based on earthworm breeding includes fermenting domestic animal feces and feed crop by mixing, where feed crop is cottonseed peel, straw, maize core, and/or wheat straw wastes; breeding earthworm by using fermenting product; pilling and mixing the earthworm feces and feed crop for cultivating edible mushroom; mixing the mushroom residue after producing edible mushroom, earthworm, earthworm feces, and grain; fermenting by microorganism; using the fermenting product to breed the domestic animals; and adding feed crop in the domestic animal feces.    USE - Green agriculture circulation production (claimed).    ADVANTAGE - The method solves the prior art technical problem that the germs, particularly virus and drug residual are in the crops, meat, egg, and milk. It saves energy and protects the environment.    DETAILED DESCRIPTION - Green agriculture circulation production based on earthworm breeding comprises:    (A) fermenting domestic animal feces and feed crop by mixing, where feed crop is cottonseed peel, straw, maize core, and/or wheat straw wastes;    (B) breeding earthworm by using fermenting product;    (C) piling and mixing the earthworm feces and feed crop at 55-65 degrees C for cultivating edible mushroom;    (D) mixing the mushroom residue after producing edible mushroom, earthworm, earthworm feces, and grain; and fermenting by microorganism;    (E) using the fermenting product to breed the domestic animals; and    (F) adding feed crop in the domestic animal feces and repeating the steps (A) to (F).
NOVELTY - The molding machine has a supporting jacket frame sleeved to spindle, whose upper and lower ends are separately connected with the decelerator and mold plate. The lower end of spindle is connected to the output end of decelerator, and upper end is fixedly connected with the transverse shaft. Two ends of the transverse shaft are provided with the rolling wheel which is located above the mold plate. A discharge hopper is located under the mold plate which penetrated the molding holes. The rolling wheel and mold plate form a combined structure.    USE - Multifunctional biomass fuel particle molding machine for treating biomass particles such as stalk, waste wood, and wood branches and leaves.    ADVANTAGE - The biomass fuel particles are molded with high compactness, high combustion value and high cost performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional biomass fuel particle molding machine.
NOVELTY - The mall sewage treatment station has a grid chamber (1), a sediment adjustment pool (2), a sewage lifting pump (3), an HBH tank (4) and a water draining pump (5), which are orderly connected by pipelines. The HBH tank is connected with a fan by an air pipe and orderly connected with a sludge drying bed (7) and the sediment adjustment pool to form a loop.    USE - Sewage treatment station for processing sewage in plants and facilities. Uses include but are not limited to a mall, large-scale factory, enterprise, public institution, school, tourist attraction and countryside.    ADVANTAGE - Treatment station has low investment, quick returns, simple maintenance and low running cost.    DESCRIPTION OF DRAWING(S) - The drawing shows then schematic block diagram of the mall sewage treatment station. (Drawing includes non-English language text).    Grid chamber (1)    Sediment adjustment pool (2)    Sewage lifting pump (3)    HBH tank (4)    Water draining pump (5)    Sludge drying bed (7)
NOVELTY - Preparation of gasification agent comprises heating water via plasma torch, taking heated water as gasification agent and feeding water into gasification furnace; taking water as cooling agent of cathode and anode of plasma torch, gasifying water into steam, absorbing cathode and anode via vaporization latent heat of water, taking steam as working gas or heated object, activating steam into active chemical substance via field ionization, resolving and activating; and spraying chemical substance into gasification furnace via the plasma torch, and reacting with carbon to generate synthesis gas.    USE - Method for preparing gasification agent (claimed) used as gasification measure of coal gasification and household garbage.    ADVANTAGE - The method can reduce carbon resource consumption, improve quality of synthesis gas and reduce discharge of greenhouse gases; and can extend service life of the cathode and the anode.    DETAILED DESCRIPTION - Preparation of gasification agent comprises heating water via plasma torch, taking heated water as gasification agent and feeding water into gasification furnace; taking water as cooling agent of cathode and anode of plasma torch, gasifying water into steam, absorbing cathode and anode via vaporization latent heat of water, to avoid or release erosion of cathode and anode, taking steam as working gas or heated object, activating steam into active chemical substance via field ionization, resolving and activating; and spraying chemical substance into gasification furnace via the plasma torch, and reacting with carbon to generate synthesis gas.
NOVELTY - Processing sludge from sewage treatment plants as fertilizer comprises performing seepage-proofing treatment on a substrate of earthworm bed; inoculating earthworm; adding feed to inoculated earthworm bed to form a seizing layer; and gradually adding nutrient elements based on contents of nitrogen, phosphorus and potassium in the collected earthworm excrement, so as to obtain the fertilizer product.    USE - Method for processing sludge from sewage treatment plants as fertilizer.    ADVANTAGE - The method has less pollution, less occupation area, strong operability, relative lower cost, high sludge treating efficiency and industrial application.    DETAILED DESCRIPTION - Processing sludge from sewage treatment plants comprises:    (A) preparing earthworm bed; and performing seepage-proofing treatment on a substrate of earthworm bed;    (B) inoculating the earthworm on earthworm bed;    (C) adding feed to the inoculated earthworm bed to form a seizing layer by adding sludge from a sewage treatment plant, adding organic substance at 1/10 of total amount of sludge when the sludge is consumed by earthwork within 1-2 months, and repeatedly adding the feed when all organic substance is consumed; and    (D) collecting the earthworm and the earthworm excrement in 40 days; and gradually adding nutrient elements based on contents of nitrogen, phosphorus and potassium in the collected earthworm excrement, so as to obtain a fertilizer product.
NOVELTY - A Tricholoma lobayense nutritious additive comprises (wt.%) straw powder (32-45), broad-leaved tree bits (25-40), dry sheep manure (12-19), broomcorn powder (3.6-6.7), wheat powder (3.5-4), plant ash (0.5-1), rapeseed cake (1.7-2), brown sugar (0.5-1), lime powder (0.1-0.3), magnesium sulfate (0.1-0.3), paclobutrazol (0.1-0.3), and superphosphate (0.5-0.8).    USE - Tricholoma lobayense nutritious additive.
NOVELTY - Fuel i.e. ethanol production involves utilizing monosodium glutamate waste material. Cellulose and potato nutrient solution are mixed with the waste material. The mixture is fermented with Saccharomyces cerevisiae to obtain ethanol.    USE - Method for producing fuel i.e. ethanol by using papermaking sludge (claimed).    ADVANTAGE - The method is simple and enables to produce fuel i.e. ethanol in short duration.
NOVELTY - An electrochemical surface modification of carbon fiber (CF) comprises adopting timed current way to carry out anode oxidization treatment or surface electric polymerization treatment for CF in additionally added electric field at additional pressure of 0.5-6 V, at 20-35 degrees C for 5-150 seconds.    USE - Method of electrochemical surface modification of carbon fiber (claimed) used as biomembrane carrier in biomembrane way sewage treatment.    ADVANTAGE - The method modifies surface of CF through anode oxidization treatment or surface electric polymerization treatment thus improving oxide content of surface of the CF and roughness and hydrophilicity of surface of CF and microbe affinity.
NOVELTY - An imidazole derivative (I) is prepared by (A) heating ketoconazole in organic solvent in presence of alkaline substance to remove acetyl and obtain deacetylated product; and (B) dissolving deacetylated product into organic solvent and slowly dipping dipyrocarbonate in presence of condensing agent to react and obtain desired derivative (I).    USE - Method is used for preparation of imidazole derivative (III) for antifungal medicine (claimed).    ADVANTAGE - The method greatly improves yield of reaction product. The reagent can be repeatedly used, thus production cost. The method has simple operation, fewer reaction steps, high purity, fewer side products and good reaction stability. The method is also suitable for industrial production. The concentrated hydrochloric acid is not needed in reaction process, thus pollution is less and product is good for environmental conservation.    DETAILED DESCRIPTION - Imidazole derivative of formula (I) is prepared by (A) heating ketoconazole in organic solvent in presence of alkaline substance to remove acetyl and obtain deacetylated product; and (B) dissolving deacetylated product into organic solvent and slowly dipping dipyrocarbonate in presence of condensing agent to react and obtain desired derivative (I).    R=alkyl.
NOVELTY - Hydrogen mixed gas generating device comprises: an atomization part provided with an atomizer for atomizing methanol mixture into a mixed liquid having micro-particles, a flow lead pipe for allowing mixed liquid having micro-particles to float, a high-oxygen gas supplying pump for pumping the high-oxygen gas into flow lead pipe from gas inlet to oxidize the atomized micro-particles, and a plasma heater for heating and split-decomposing oxidized micro-particles to separate hydrogen ions, hydroxide ions and relative radicals, where the ions react with mixed liquid having micro-particles.    USE - Used as a hydrogen mixed gas generating device.    DETAILED DESCRIPTION - Hydrogen mixed gas generating device comprises: an atomization part provided with an atomizer for atomizing methanol mixture into a mixed liquid having micro-particles with an average diameter of 2 mu m, a flow lead pipe provided with a gas inlet at one end for allowing the mixed liquid having micro-particles to float and flow, a high-oxygen gas supplying pump for pumping the high-oxygen gas having more than 21% of the oxygen content into the flow lead pipe from the gas inlet to oxidize the atomized micro-particles, and a plasma heater arranged at one end of the flow lead pipe for heating and split-decomposing the oxidized micro-particles to separate the hydrogen ions, hydroxide ions and relative radicals, where the hydrogen ions, hydroxide ions and relative radicals react with the mixed liquid having micro-particles to produce a low-temperature hydrogen mixed gas containing hydrogen, carbon monoxide, carbon dioxide and methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydrogen mixed gas generating device.
NOVELTY - Low-carbon gasoline, comprises (in wt.%) 90# gasoline (30-50), hydrogenated naphtha (10-30), methyl tertiary butyl ether (5-15) and low-carbon mixed alcohol (25-40).    USE - Used as a low-carbon gasoline.    ADVANTAGE - The low-carbon gasoline: has good appearance, improved power performance and quickened speed acceleration after using, full combustion of fuel without generating collected carbon, reduced carbon dioxide, carbon monoxide and sulfur dioxide in the tail gas, reduced carbon and air pollution, and increased anti-detonating quality; and eliminates the need of changing the car fuel system and the bad effect on the engine; conserves oil; and is economical.
NOVELTY - A low-temperature water gas conversion catalyst contains active component and carrier. The active component is gold. The carrier is zirconia. The content of gold and zirconia is 0.1-3 weight% and 97-99.9 weight%, respectively.    USE - Low-temperature water gas conversion catalyst is used for hydrogen-rich modified gas.    ADVANTAGE - The low-temperature water gas conversion catalyst has excellent catalytic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of low-temperature water gas conversion catalyst, which involves heating solution containing zirconium in hydrothermal kettle, forming precipitate, cooling the hydrothermal kettle at room temperature, removing the precipitate, dripping aqueous ammonia to the precipitate, regulating pH to more than 6, rinsing the precipitate, drying the precipitate, baking, forming zirconia carrier, dispersing zirconia carrier in water by ultrasonic auxiliary method, forming zirconia carrier emulsion, adding chloroauric acid to the zirconia carrier emulsion, stirring heating while adding precipitator, controlling the final point pH value, depositing the gold on the surface of the carrier, aging, settling, drying, and forming gold/ zirconia catalyst; and    (2) activating method of low-temperature water gas conversion catalyst, which involves activating catalyst in hydrogen gas at 300 degrees C for 2 hours.
NOVELTY - A coal bed methane raw material is compressed with oxygen to obtain compressed coal bed gas. The obtained compressed coal bed gas is adsorbed using carbon molecular sieve to obtain adsorbed coal bed methane. The adsorbed coal bed methane is concentrated using pressure swing adsorption and separated the concentrated methane in deoxidized coal bed methane. The amount of oxygen is 1 volume% or less. Thus, separation and concentration of methane is effectively enabled.    USE - Concentration and separation of methane.    ADVANTAGE - The concentration and separation of methane is effectively enabled.
NOVELTY - Agent containing dimethylamine salt comprises 12% of dioctyl diethylenetriamine glycine hydrochloride and 4% of oxybiotic material.    USE - The agent containing dimethylamine salt is useful for preventing bacterial slime in banana trot (claimed).    ADVANTAGE - The agent has preventing effect of 89% or more in potted banana plant and 71% or more in field plant. The agent is less toxic and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-mentioned agent, which involves (a) mixing the dioctyl diethylenetriamine glycine hydrochloride and filler and stirring the mixture uniformly, and (b) mixing the obtained mixture of step (a) with the oxybiotic material and additive, stirring the mixture and crushing stirred mixture, where mass percent of the dioctyl diethylenetriamine glycine hydrochloride is 12% and the oxybiotic material is 4%.
NOVELTY - Method of processing livestock excretion, involves adding (in parts weight) agent (100) containing phyllite powder and starter to livestock excretion (40-50) in an excretion disposal tank at 40-45 degrees C, and adding the livestock excretion for every 1-4 hours to the tank while mixing and stirring the mixture in the tank.    USE - The method is useful for processing livestock excretion which is used for preparing compost (claimed).    ADVANTAGE - The method is economic.
NOVELTY - Livestock excretion treatment unit comprises conveying unit (20) for dropping excrements upwardly so that excrements within a storage tank (10) is circulated, an ultrasonic generating unit (30) for fogging urine, which is installed on a drop path of the circulating excrements, a discharging unit (40) for discharging fogged urine to the outside of a storage tank and a reaction tank (50) for discharging the urine component in a liquid state.    USE - The unit is useful for treating livestock excretion.    ADVANTAGE - The treatment unit deodorizes bad odor in excrement and environmentally-friendly as it does not cause any harmful effects to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of livestock excretion treatment unit.    Storage tank (10)    Conveying unit (20)    Ultrasonic generating unit (30)    Discharging unit (40)    Reaction tank (50)
NOVELTY - The present invention provides a conveyor unit for feeding biomass into a pressure container. It is difficult to feed a heterogeneous solid, such as a biomass, into a pressurized container. Rotary valve and pressure valve used so far have considerable shortcomings. The use of standard screw conveyors has failed to form a space behind the screw line up to now, where the gas can be escaped from the pressure container. These shortcomings are overcome by arranging two independently controllable screw conveyors in a screw conveyor pipeline. The biomass is compressed by the high pressure created as a result of different rotational speeds of the motors for driving the primary screw conveyor and the secondary screw conveyor in such a way that an almost gas-tight plug is formed. The invention is particularly suitable for feeding a biomass into pressurized vaporization equipment for producing synthesis gas.
NOVELTY - Wastes are only suitable for directly producing synthesis gas under specific conditions due to its heterogeneous property. The objective of the present invention is to produce synthesis gas utilizing heat energy of the wastes while the problematic compound will not reach the synthesis gas. The objective can be achieved by compensating the heat absorption reactions in a synthesis gas and heating the material flow to be coupled through energy from the high temperature fume of a waste combustion equipment, wherein the feeding flow of the synthesis gas reactor, for example, is composed of biomass. Under a condition of using cheaper heat energy of the waste combustion equipment, the present invention is suitable for producing synthesis gas from carbon-containing energy carrier such as biomass.
NOVELTY - A reformer comprises: a heating unit comprising a heating unit chamber that extends in a first direction, and a combustor arranged to receive and oxidize anode off gas; a reforming unit including a first space formed around the heating unit chamber, a second space formed around the first space, and a flow path portion arranged to connect the first space and the second space at an end region of the first and second space; and a heat resistant shield attached to a surface of the flow path portion facing the combustor and located adjacent the combustor.    USE - The reformer is useful for industrial and commercial applications.    ADVANTAGE - The reformer has high durability, and can operate an environment friendly fuel cell while ensuring the long-time lifespan by improving reforming efficiency and reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of a reformer.    Connector (11)    Heating unit (20)    Second combustor (22)    Shield (30)
NOVELTY - The device has a low-temperature gas-liquor reactor (5) whose upper part is connected with two paths of feeding systems. One of the paths of the system is connected with a liquor storage tank (11) by a first valve (v6) and a high-pressure liquid pump (12), and the other path of the system is connected with a gas storage tank by second and third valves (v1, v4) and a mass flow meter (2). An upper part of a high-temperature gas-liquor reactor (16) is connected with a data collection device (22) by fourth and fifth valves (v9, v13), a gas-liquor separator (18) and a pressure controller (19).    USE - Device for catalytically hydrogenating biological oil in a petroleum industry.    ADVANTAGE - The device can economically and high-efficiently hydrogenate the unstable oxide compounds such as biological oil, to prepare the petroleum chemical product, so that the device effectively releases the petroleum shortage. The device has simple structure and easy operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a catalytically hydrogenating method for a biological oil catalytically hydrogenating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for catalytically hydrogenating biological oil in a petroleum industry.    Valves (v1, v4, v6, v9, v13)    Mass flow meter (2)    Low-temperature gas-liquor reactor (5)    Liquor storage tank (11)    High-pressure liquid pump (12)    High-temperature gas-liquor reactor (16)    Gas-liquor separator (18)    Pressure controller (19)    Data collection device (22)
NOVELTY - A water area purification process involves throwing in raw material which contains wreckage of useful bacterial which have water purification function in same tank for overcrowded culture with water taken in from specific water area, carrying out overcrowded culture of local habitation microbe which exists in water of water area within tank until enzyme crystal arises, and dispersing next generation microbe of local habitation microbe in overcrowded culture.    USE - Water area purification process of river, mouth of river and sea area.    ADVANTAGE - The process is efficient and costs low and can purify organic contaminant and sludge in water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic general view of the process plant. (Drawing includes non-English language text).    Sand filter device (F1)    Process liquid supply piping (L2)    First-third tank as tank for pre-processing (T1-T3)    Fourth tank as tank for overcrowded culture (T4)    Sea area as water area (W)
NOVELTY - Reducing (P1) metals in metal-containing biomass-derived pyrolysis oil involves: contacting the metal-containing biomass-derived pyrolysis oil with an acidic ion-exchange resin having sulfonic acid groups to produce low metal biomass-derived pyrolysis oil and spent ion-exchange resin; and removing the low metal biomass-derived pyrolysis oil from the spent ion-exchange resin.    USE - For reducing metals in metal-containing biomass-derived pyrolysis oil (claimed).    ADVANTAGE - The process selectively reduces metals without changing the other properties of the biomass-derived pyrolysis oil (such as viscosity, carbon content, water content and acidity of the biomass-derived pyrolysis oil remains unchanged after ion-exchange). The process improves the suitability of the biomass-derived pyrolysis oil for use as a biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing (P2) a low metal biomass-derived pyrolysis oil involving contacting metal-containing biomass-derived pyrolysis oil with an acidic ion-exchange resin having sulfonic acid groups to produce low metal biomass-derived pyrolysis oil and spent acidic ion-exchange resin; and removing the low metal biomass-derived pyrolysis oil from the spent acidic ion-exchange resin.
NOVELTY - Making hexose, pentose, alkyl glucosides, alkyl pentoside involves combining a feedstock with an alcohol and water where the feedstock having cellulosic material and/or proteins; combining a feedstock with an alcohol and water where the feedstock having cellulosic material and/or hemicelluloses material; and (c) reacting the feedstock, and the alcohol and water at a temperature of 140-350 degrees C, and at pressure of 500-3200 psig to cleave the cellulosic material to generate hexose, pentose, alkyl glucoside, alkyl pentoside and its derivatives.    USE - For making hexose, pentose, alkyl glucosides, alkyl pentoside (claimed).    ADVANTAGE - The method produces fatty acid alkyl ester as well as cellulosic simplified sugars, shortened protein polymers or amino acids. The method provides simple and efficient method for the production of biofuels and ethanol from renewable energy sources.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for following:    (1) a composition comprising water, 1-5C alcohol, lignin, amorphous cellulose, monosaccharides, disaccharides, trisaccharides, hexose and xylose, all in solution; and    (2) a system is configured such that the modules present are mechanically coupled, capable of performing continuous process.
NOVELTY - Reduction (100) of water in a water-containing biomass-derived pyrolysis oil comprises distilling (104) the water-containing biomass-derived pyrolysis oil in the presence of an azeotrope-forming liquid to form an azeotrope; and removing (106) the azeotrope.    USE - Method for the reduction of water in a water-containing biomass-derived pyrolysis oil (claimed).    ADVANTAGE - The low water biomass-derived pyrolysis oil has increased storage stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for low water biomass-derived pyrolysis oil.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of the method for the reduction of the water content of biomass-derived pyrolysis oil.    Reduction of the water content of biomass-derived pyrolysis oil (100)    Providing water-containing biomass-derived pyrolysis oil (102)    Distilling the water-containing biomass-derived pyrolysis oil and an azeotrope-forming liquid (104)    Removing the azeotrope (106)    Removing low water biomass-derived pyrolysis (108)
NOVELTY - Producing a fuel by gasification in a high-temperature gasifier such as a dust gasifier involves operating the dust gasifier by co-feeding along with peat dust another kind of biomass dust such as ground wood-based biomass, soil biomass and/or some other similar biomass.    USE - For producing a fuel such as synthetic liquid fuel and/or certified biofuel (claimed).    ADVANTAGE - The dust gasifier used in the method is a high-temperature gasifier that is reliable in operation, uncomplicated and cost-effective as an investment. The peat dust used in the method is complemented with another kind of biomass dust that possibly degrades the qualities of peat dust, and allows the use of such a dust mixture without compromising the gasification process itself.    DETAILED DESCRIPTION - Producing a fuel by gasification in a high-temperature gasifier such as a dust gasifier involves operating the dust gasifier by co-feeding along with peat dust another kind of biomass dust such as ground wood-based biomass, soil biomass and/or some other similar biomass. The fraction of peat dust raw material to be used as feedstock in a dust gasifier is replaced with dried and milled biomass dust such as fibrous harvested wood residuals, chipped forest/logging residuals, bark or the like wood-based raw material, soil biomass, biomass dried and milled from waste sludge or any corresponding mass, either as separate fractions. The gasification in a pressurized dust gasifier is carried out co-feeding specially dried and milled wood dust along with peat dust suited for gasification due to its advantageous particle shape, size distribution, moisture content and mixture ratio of wood-to-peat dust. The peat dust is used in gasification by way of complementing the feedstock with wood-based biomass, soil biomass and/or other biomass suited for feedstock in a gasifier.    DESCRIPTION OF DRAWING(S) - The figure shows a process diagram of the method of producing a fuel by gasification.
NOVELTY - Producing biodiesel from biolipids comprises: (a) mixing biolipids with low-molecular weight alcohol and catalyst to obtain a reaction mixture; (b) generating cavitational fluid features in the fluidic reaction mixture to obtain a fluidic reaction mixture containing the biolipids in a liquid state and the low-molecular weight alcohol in a gaseous state; (c) reacting the liquid state biolipids with the gaseous state low-molecular weight alcohol to produce the biodiesel and a glycerol; and (d) separating the biodiesel from the glycerol.    USE - The method is used for producing biodiesel from biolipids (claimed).    ADVANTAGE - The method carries out heterogeneous reactions that do not require a large amount of energy input. It also avoids potentially dangerous, high-pressure operation.    DETAILED DESCRIPTION - Producing biodiesel from biolipids comprises: (a) mixing the biolipids with a low-molecular weight alcohol and a catalyst to obtain a two phase, liquid-liquid fluidic reaction mixture; (b) pumping the fluidic reaction mixture through a cavitation device at an inlet pump pressure and an inlet fluid velocity; (c) reducing the fluid pressure of the fluidic reaction mixture so that it reaches the vapor pressure of the low-molecular weight alcohol; (d) generating cavitational fluid features, including low-molecular weight alcohol vapor-filled bubbles, in the fluidic reaction mixture to obtain a two-phase liquid-gas fluidic reaction mixture containing the biolipids in a liquid state and the low-molecular weight alcohol in a gaseous state; (e) collapsing the low-molecular weight alcohol vapor-filled bubbles resulting in localized elevations of temperature and pressure; (f) reacting the liquid state biolipids with the gaseous state low-molecular weight alcohol to produce the biodiesel and a glycerol; and (g) separating the biodiesel from the glycerol.
NOVELTY - Method (I) for making fatty acid alkyl esters comprises: combining a feedstock (110) with an alcohol (120) and an acid catalyst (130), where the feedstock comprises free fatty acids and/or glycerides, and cellulosic material and/or proteins; and reacting the feedstock and alcohol at a pH of 0-5 at 140-300 degrees C, and at a pressure that is sufficient to prevent boiling of the alcohol during the reaction to generate fatty acid alkyl esters, cleave the cellulosic material, if present, and to shorten the proteins and/or form amino acids, if proteins are present.    USE - The method is useful for making fatty acid alkyl esters, shortened protein, amino acids (claimed) and cellulosic simplified sugars, where the fatty acid alkyl ester is useful as biodiesel.    ADVANTAGE - The method utilizes low cost and abundantly available feedstock, and water, thus allowing the conversion of biomass into fatty acid alkyl esters (biodiesel) and sugars to produce ethanol in a fast, single-step and economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (II) for making fatty acid alkyl esters, comprising: combining the feedstock with the alcohol and acid catalyst; and reacting the feedstock and alcohol at a pH of 0-5 at 140-260 degrees C, and at a pressure that is sufficient to prevent boiling of the alcohol during the reaction to generate fatty acid alkyl esters, cleave the cellulosic material, to shorten the proteins and to form amino acids.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the method for making the fatty acid alkyl esters.    Feedstock (110)    Alcohol (120)    Acid catalyst (130)    Pressurized reactor (140)    Water (160)
NOVELTY - Continuous process for producing biodiesel fuel, with conversion of more than 99.90 wt% of the triglycerides into biodiesel comprises: (a) providing a source of triglycerides and subjecting to a transesterification reaction; (b) recovering the product and subjecting to a mechanical agitation operation, and obtaining a conversion of more than 99.90 wt% of the triglycerides into biodiesel; (c) decanting and/or centrifuging the product to eliminate glycerine; (d) purifying the biodiesel; and (e) eliminating methanol and water and recovering the biodiesel fuel.    USE - The process is used for producing biodiesel fuel (claimed).    DETAILED DESCRIPTION - Continuous process for producing biodiesel fuel, with conversion of more than 99.90 wt% of the triglycerides into biodiesel during the transesterification step comprises: (a) providing a source of triglycerides with a triglyceride concentration of more than 99.0wt%; (b) subjecting the triglycerides to a transesterification reaction with methanol and/or ethanol, in a mole reaction of triglycerides and alcohol of 1:3-3.5, in the presence of 0.7-1.0 wt% sodium or potassium hydroxide as a catalyst, under conditions of ultrasonic cavitation in an ultrasonic cavitation reactor with 2-8 cavitation cells in series, at a temperature of 45-60 degrees C, at a pressure of 1.5-2 MPa (15-20 atm) and for a time of 15-30 seconds; (c) recovering the product from (b) and subjecting to a mechanical agitation operation, at a temperature of 45-60 degrees C, for a maximum time of 10 minutes until the transesterification reaction is completely finished, and obtaining a conversion of more than 99.90 wt% of the triglycerides into biodiesel; (d) decanting and/or centrifuging the product obtained from (c) to eliminate glycerine; (e) purifying the biodiesel obtained in (d) using exchange resins; and (f) eliminating methanol and water from the product obtained in (e) by distillation and recovering the biodiesel fuel.
NOVELTY - Producing hydrocarbons from microbial lipids, comprises: contacting a feed comprising microbial lipids comprising triglyceride and a free fatty acid, with a hydrogenation catalyst and hydrogen at 250-380 degrees C and a total pressure of 20-160 bar (absolute) to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons; contacting the paraffinic hydrocarbons or the effluent by contacting hydrogen and the liquid stream with hydroisomerization catalyst; and separating at least one product fraction from the product stream.    USE - The process is useful: for producing hydrocarbons from microbial lipids; and for producing kerosene or diesel fuel fraction (all claimed).    ADVANTAGE - The process: provides paraffinic kerosene and diesel components with excellent cold flow properties; and allows direct conversion of microbial lipids to hydrocarbons without need of conversion to 14-18C alkyl esters.    DETAILED DESCRIPTION - Producing hydrocarbons from microbial lipids, comprises: contacting a feed comprising microbial lipids comprising triglyceride (40-70 wt.%) and a free fatty acid (10-30 wt.%), with a hydrogenation catalyst and hydrogen at 250-380 degrees C and a total pressure of 20-160 bar (absolute) to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerization catalyst at 280-450 degrees C and a total pressure of 20-160 bar (absolute); and separating at least one product fraction from the product stream. An INDEPENDENT CLAIM is also included for a kerosene or diesel fuel fraction obtainable from the process.
NOVELTY - Producing hydrocarbons from microbial lipids comprises: contacting a feed comprising microbial lipids with a hydrogenation catalyst and hydrogen, to obtain an effluent comprising paraffinic hydrocarbons and water; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerization catalyst; and separating at least one product fraction from the product stream, where the step (a) and/or the step (c) comprises a sulfided hydrogenation catalyst.    USE - The process is useful to obtain a kerosene or diesel fuel fraction (claimed).    ADVANTAGE - The process is cost efficient process that yields fuels of good quality.    DETAILED DESCRIPTION - Producing hydrocarbons from microbial lipids comprises: (a) contacting a feed comprising microbial lipids with a hydrogenation catalyst and hydrogen at 250-380 degrees C and a total pressure of 20-160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; (b) optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent obtained in step (a); (c) contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerization catalyst at 280-450 degrees C and a total pressure of 20-160 bar (absolute); and (d) separating at least one product fraction from the product stream obtained in step (c), where the hydrogenation catalyst of step (a) and/or the hydroisomerization catalyst of step (c) comprises a sulfided hydrogenation catalyst.
NOVELTY - Method of producing saccharides comprising glucose as main component, involves mixing biomass containing cellulose and/or hemicellulose with an aqueous enzyme solution, and subjecting the mixture to enzymatic saccharification in a reactor while maintaining the mixture of the biomass with the aqueous enzyme solution in a stationary state, where the cellulose and/or hemicellulose are saccharified using enzyme contained in the aqueous enzyme solution.    USE - The method is useful for producing saccharides.    ADVANTAGE - The method is reliable as it consumes less energy, increases production amount of glucose, and is cost-effective as it utilizes less amount of enzyme. The enzyme deterioration is prevented during stirring process. The contacting efficiency of cellulose and hemicellulose with enzyme is improved.
NOVELTY - Pretreating a crude oil prior to a crude oil distillation process comprises propagating a culture of a hydrocarbon-utilizing and biosurfactant-producing microbial strain and treating the crude oil with the propagated culture.    USE - The method is useful for pretreating crude oil prior to crude oil distillation process (claimed).    ADVANTAGE - The invention provides process for distilling crude oil which is capable of increasing volume of distillate with comparable quality as well as reducing time, cost and energy incurred.
NOVELTY - Gas oil composition comprises 65-92.5% by volume with respect to the total volume of composition of at least one gas oil; 0.5-20% by volume with respect to the total volume of the composition of at least one diethyl carbonate, the diethyl carbonate being obtained from bioethanol; and 0.5-15% by volume with respect to the total volume of the composition of at least one biodiesel; on the condition that the total amount of the diethyl carbonate and of the biodiesel is higher than or equal to 7.5% by volume with respect to the total volume of the composition.    USE - The composition is useful as fuel for diesel engines (claimed).
NOVELTY - Preparing supported catalyst involves establishing shell-removal conditions for supported catalyst intermediate that comprises capped nanoparticles of catalyst material dispersed on carbon support, the capped nanoparticles comprise platinum alloy core capped in organic shell, and shell-removal conditions comprise elevated temperature and inert gas atmosphere; and removing the organic shell from platinum alloy core in shell-removal conditions to limit thermal decomposition of carbon support and to limit agglomeration of catalyst material.    USE - For preparing supported catalyst (claimed) i.e. platinum alloy catalysts which is useful in fuel cells for generating electric current.    ADVANTAGE - The process provides stable and high electrochemical activity supported catalyst. The supported catalyst maintains an electrochemical surface area of at least 30 (preferably 30-150, especially 40-120, particularly 40-60) m2/g Pt.    DETAILED DESCRIPTION - Preparing supported catalyst involves establishing shell-removal conditions for a supported catalyst intermediate that comprises capped nanoparticles of catalyst material dispersed on carbon support, the capped nanoparticles each comprise a platinum alloy core capped in an organic shell, and the shell-removal conditions comprise an elevated temperature and an inert gas atmosphere that is free of oxygen; and removing the organic shell from the platinum alloy core in the shell-removal conditions to limit thermal decomposition of carbon support and to limit agglomeration of the catalyst material such that the supported catalyst maintains an electrochemical surface area of at least 30 m2/g Pt.
NOVELTY - The sensor (100) has a fiber Bragg grating (10) coated with a coating material (20) and on a cladding or a partially removed cladding of the fiber Bragg grating. The coating material interacts with a measurand to cause a change in an effective refractive index of the fiber Bragg grating. The coating material includes a polymer material, and the measurand includes gas or temperature variation, where the gas is selected from a group consisting of carbon monoxide, carbon dioxide and methane. The coating material includes palladium in combination with carbon nanotubes.    USE - Sensor i.e. distributed combi sensor, for multiple measurand sensing.    ADVANTAGE - The coating material interacts with the measurand to cause the change in the effective refractive index of the fiber Bragg grating, thus improving the detection capacity of the sensor by coating the fiber Bragg grating with the coating material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a system for detecting multiple measurands comprising an optical fiber    (2) a method for detecting multiple measurands.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a sensor for detecting a particular measurand.    Fiber Bragg grating (10)    Coating material (20)    Sensor (100)
NOVELTY - Producing bio-oil comprises separating a lignocellulosic resource into a substantially cellulosic portion and a substantially non-cellulosic portion; and fermenting the substantially cellulosic portion to produce microbial oil, pyrolyzing the substantially non-cellulosic portions to produce bio-oil or fermenting the substantially cellulosic portion to produce microbial oil and pyrolyzing the substantially non-cellulosic portion to produce bio-oil.    USE - The method is useful for producing bio-oil (claimed).    ADVANTAGE - The invention provides robust and sustainable biofuel technologies from multiple types of sustainable and renewable feedstocks to meet the increasing demand for biofuels. It provides novel separating and conversion process for maximizing carbon conversion efficiency, while minimizing processing energy requirements.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a liquid processing stream comprising a substantially lignocellulosic stream and a substantially non-cellulosic stream, where the lignocellulosic stream is converted to microbial oil with oleaginous fermentation, the non-cellulosic stream is converted to bio-oil with pyrolysis, or the lignocellulosic stream is converted to microbial oil with oleaginous fermentation and the non-cellulosic stream is converted to bio-oil with pyrolysis; and    (2) a system comprising a hydrocarbon production facility comprising separating equipment for separating lignocellulosic biomass into a cellulosic portion and a non-cellulosic portion; and fermentation equipment for converting the cellulosic portion to a microorganism containing medium or pyrolysis equipment for converting the non-cellulosic portion to bio-oil, or its combination.
NOVELTY - The pyrolyzer has a primary fuel gas purifying chamber whose upper part is equipped with a spilling fire grate (9) that is provided with an adjustable insertion depth. A bottom part of a boiling gasifier is provided with a gasification agent inlet (4) and a gasification agent nozzle (6). A section from a position under a central line of the nozzle to a position over the grate is provided with a catalytic pyrolysis section (15). A position under the grate is provided with a fuel gas outlet (8). An upper part of the boiling gasifier is provided with a material inlet (3) and a lighting hole (13).    USE - Pyrolyzer for pyrolyzing and gasifying agriculture and forestry solid wastes e.g. straw.    ADVANTAGE - The pyrolyzer increases yield of combustible gas and quality of the fuel gas. The pyrolyzer is convenient to operate during the purification process, and has better gasification temperature, and prevents the generation of harmful gases such as dioxin. Tar particles obtained during gasification are cracked and most parts of carbon dioxide are reduced. The biomass can be applied for the incineration of the solid domestic wastes.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a pyrolyzer.    Material inlet (3)    Gasification agent inlet (4)    Gasification agent nozzle (6)    Fuel gas outlet (8)    Spilling fire grate (9)    Lighting hole (13)    Catalytic pyrolysis section (15)
NOVELTY - The method involves stacking bipolar plates and membrane electrode units one above the other. The bipolar plates are formed from plates (3.1, 3.2) with which structures are brought up and/or are introduced on one side and in sections. The plates are arranged relative to each other in a flat manner and joined with one another. The plates are produced from metal substrate bands (1, 2). The structures are produced for joining the plates in temporally parallel work steps and separately for the metal substrate bands.    USE - Method for producing a fuel cell stack.    ADVANTAGE - The structures are produced for joining the plates in temporally parallel work steps and separately for the metal substrate bands, thus enabling full automatic production of a fuel cell stack in a simple, rapid and cost-effective manner while enabling full automatic production of the bipolar plates.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of two metal substrate bands from which plates are produced for a bipolar plate.    Metal substrate bands (1, 2)    Plates (3.1, 3.2)
NOVELTY - A low-temperature fluidity improver of fatty-acid methyl ester comprises component (X) which consists of copolymer (X1) obtained by copolymerizing olefin type monomer and maleic acid anhydride type monomer (b) or copolymer (X2) obtained by copolymerizing olefin type monomer (a), maleic acid anhydride type monomer (b) and (meth)acrylic acid type monomer (c), or component (Y) which consists of copolymer (Y1) obtained by copolymerizing styrene type monomer (d) and (meth)acrylic acid ester type monomer (e) and/or homopolymer (Y2) obtained by polymerizing (meth)acrylic acid ester type monomer (e).    USE - A low-temperature fluidity improver of fatty-acid methyl ester used for biodiesel fuel (claimed).    ADVANTAGE - The improver can efficiently improve low-temperature fluidity of fatty acid methyl ester.    DETAILED DESCRIPTION - A low-temperature fluidity improver of fatty-acid methyl ester comprises component (X) which consists of copolymer (X1) obtained by copolymerizing olefin type monomer (a) of formula R1CH=CHR2 (1) and maleic acid anhydride type monomer (b) of formula (2) or copolymer (X2) obtained by copolymerizing olefin type monomer (a), maleic acid anhydride type monomer (b) and (meth)acrylic acid type monomer (c), or component (Y) which consists of copolymer (Y1) obtained by copolymerizing styrene type monomer (d) of formula R3CH=CH2 (3) and (meth)acrylic acid ester type monomer (e) of formula CH2=CR4(LR5) (4) and/or homopolymer (Y2) obtained by polymerizing (meth)acrylic acid ester type monomer (e).    R1,R2=H, or 1-100C hydrocarbon group which may be substituted by O, -C(=O)-, -C(=O)O-, -OC(=O)-, -OC(=O) O-, or hydrogen;    R3=H or phenyl;    R4=H or Me;    L=-C(=O) O- or -OC(=O)-; and    R5=1-40C hydrocarbon.    An INDEPENDENT CLAIM is included for a biodiesel fuel composition comprising low-temperature fluidity improver for fatty-acid methyl ester, and biodiesel fuel.
NOVELTY - The cooler (1) has a gas guide pipe (4) for passing through synthesis gas. A sound device (9) is arranged with a rapper at the guide pipe for transferring rapping energy. The guide pipe comprises an inner pipe (5) that is designed in oscillatory manner. The guide pipe comprises a passage for a plunger of the sound device that is connected with the guide pipe in a gas-tight manner. The plunger lies in a normal position on the inner tube. The sound device has bellows i.e. spring element, for the rapper.    USE - Gas cooler for cooling synthesis gas produced by gasification of a renewable raw material in sewage sludge.    ADVANTAGE - The sound device is arranged with the rapper at the guide pipe for transferring rapping energy, thus simplifying cleaning of the gas cooler during operation of the gas cooler.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal sectional view of a gas cooler.    Gas cooler (1)    Head region (2)    Gas guide pipe (4)    Inner pipe (5)    Sound device (9)
NOVELTY - Hydrogen is generated using a hydrogen production material (2) containing a metal material capable of generating hydrogen by exothermic reaction with water, a heat generating material capable of reacting with water and generating heat, and material other than metal material. The metal material contains 80 %mass or more of particles having size of 100 mu m or less. The metal material is contacted with aqueous acid (4) existing in liquid state at 100 degrees C and having freezing point of less than -5 degrees C, and hydrogen is generated.    USE - Method for generating hydrogen used as fuel for fuel cell in fuel cell system (claimed).    ADVANTAGE - Hydrogen is efficiently manufactured at low temperature by a simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing apparatus (100) of hydrogen; and    (2) fuel cell system (200).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the manufacturing apparatus of hydrogen.    Container (1)    Hydrogen generating material (2)    Aqueous acid (4)    Heat insulation material (9)    Manufacturing apparatus (100)    Fuel cell system (200)
NOVELTY - Field composting of crop straws, comprises providing harvested straws without fruits and seeds, crushing and pulverizing in a pulverizer, then making the length of the straws to reach 2-10 cm or kneading in a kneading machine, air drying or adding water to make water content to reach 50-65%, adding (in wt.%) straw rotten agent (0.1), calcium superphosphate (0-5), magnesium sulfate (0-6) or urea (0-5), composting and turning when the temperature reaches to more than 65 degrees C, and preserving at more than 65 degrees C for 5 days or preserving at 55 degrees C for 10 days.    USE - The method is useful for field composting of crop straws.    ADVANTAGE - The method avoids burning and abandoning of straws. The feeding device is mounted at the front end of the pulverizer, so that the pulverizer is suitable to feed, crush and pulverize gourd vine vegetable residual bodies or thick-stem vegetable residual bodies and reduces the nitrogen element loss and fully kill the disease source creatures carried by straws in the composting process of the vegetable straws, and enhances the temperature raising process, softening process and the decomposition process of the straws.
NOVELTY - Method for fermenting cow dung, involves placing fresh cow dung at 70-75 degrees C, and stacking for 20-25 days.    USE - The method is useful for fermenting cow dung.    ADVANTAGE - The method is cost-effective, rapid and less labor intense, and prevents humidification of cow dung during fermentation process.
NOVELTY - The biogas collecting system has an underground gas collecting pipe that employs an antiseptic treated integral moso bamboo. Longitudinal fine grooves and small holes are uniformly formed on the integral moso bamboo. The gas is accumulated to a gas compressing pump by a ground plastic pipe network. The biogas is pumped into water-sealing gas storage kettle by the gas compressing pump.    USE - Biogas collecting system in refuse landfill.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biogas collecting system.
NOVELTY - A botanical agricultural germicide is prepared into miscible oil by grinding dry hawthorn kernel; filtering through a 40-mesh sieve; soaking into mixed solvent for 24 hours; extracting twice under reflux condition for 3 hours at 75-80 degrees C and combining extracted liquids; condensing the extracted liquid by vacuum condensation, and fixing volume till the extracted liquid is 1/3 of weight of crude drug to obtain extract; adding (pts.wt.) the hawthorn kernel extract (2-7), solvent (1-5) and other auxiliary agents (1-2); and completely mixing at 50 degrees C to obtain germicide in form of miscible oil.    USE - Botanical agricultural germicide in form of miscible oil or microemulsion used for preventing and controlling plant diseases caused by Botrytis cinerea, Rhizoctonia solani, Fusarium sp., Alternaria sp., Phytophthora sp., Ustilago sp., Colletotrichum sp., Phoma sp., and Verticillium sp. in field crops including wheat, maize, paddy rice, potato, sweet potato, beetroot, peanut and cotton; vegetable crop including cucumber, cabbage, tomato, pepper, pea and hyacinth bean; and gardening crop including apple, peach, pear, orange, and grape (all claimed).    ADVANTAGE - The germicide is environmentally-friendly, and has broad inhibiting spectrum, high efficiency, low toxicity, and no resistance to fungi.
NOVELTY - Micro-reacting system comprises a microreactor (1) formed by assembling a microchannel reactor (11) and a microchannel heat exchanger (12). The microchannel reactor is connected with a storage container of the acid and the ammonia by a pipe. The flow regulating elements are mounted on the pipe between the acid/ammonia storage container and the microchannel reactor. The pH detecting point is arranged on the micro-bypass on the outlet end of the microchannel heat exchanger.    USE - The micro-reacting system is useful for producing ammonium salt (claimed).    ADVANTAGE - The micro-reacting system: occupies less area; is easy to control and has fast heat-transferring speed; and has stable pH control and releases less high-temperature tail gas (ammonia), and is environmental friendly, when compared to the conventional production process of the ammonium phosphate; is simple, safe and highly efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use of micro-reacting system comprising using acid solution and the ammonia water as raw materials to prepare ammonium salt solution and the concentrations of the acid, ammonia and the prepared ammonium salt are lower than the saturation concentration of the ammonium salt in the reacting temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the micro-reacting system for producing ammonium salt.    Microreactor (1)    Metering pump (2)    pH detecting point (5)    Microchannel reactor (11)    Microchannel heat exchanger (12)
NOVELTY - Fertilizer comprises (in wt.%): dried human excrement (12-16), dried duck manure (14-18), dried sheep manure (8-12), bran (8-10), broomcorn flour (6-8), sweet potato flour (12-14), beanstalk powder (6-8), rhizoma polygonati powder (2-6), pine needle powder (1-3), wild anise powder (2-4), tobacco powder (1-3), Eucommia ulmoides powder (3-5), Chinese Angelica (1-3), bulbus fritillariae cirrhosae powder (2-4), snakegourd fruit powder (1-3) and peach kernel powder (1-3).    USE - The fertilizer is useful for cultivating and planting sedum kamtschaticum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-mentioned fertilizer, which involves adding the above-mentioned raw materials into stirrer, stirring the mixture for 100 minutes, obtaining the mixture, adding the mixture into crusher, crushing the mixture into powder, obtaining the powder, adding the powder into fermenting tank for piling the mixture, closely covering and compacting the mixture using plastic cloth, fermenting the mixture for 72 hours, turning pile for first time, when turning the pile, adding human excrement water into the pile based on ratio of 1:0.6, spraying the human excrement water and turning the pile at same time, when turning the pile, turning lower portion of the pile upwards, turning inner portion of the pile outwards, turning outer portion of the pile inwards, and turning upper portion of the pile downwards, spraying the human excrement water uniformly, closely covering and compacting the pile using plastic cloth, fermenting the mixture continuously for 72 hours at 80 degrees C or more, turning the pile once for every 72 hours, adding human excrement water when turning the pile each time, and turning the pile for 7 times continuously.
NOVELTY - The electrostatic device has a set of divisive elements for treatment of hydrocarbons flowing in rubbing shock treatment with porous material. The element is copper and produces the solution of large carbon chains with hydrogen to create electrostatic charge acquired by the free electrons. The device has three components of liquid fuels, such as gasoline, diesel, methanol, fuel alcohol.    USE - Electrostatic device for improving quality of combustion of hydrocarbons.    ADVANTAGE - The electrostatic device reduces emission of carbon monoxide, carbon dioxide and other air pollutants.
NOVELTY - Preparing calcium phosphate nano-carrier system, comprises dissolving soluble calcium salt and water insoluble drug into organic solvent, adding solution of the soluble phosphate to obtain calcium phosphate nano-carrier and simultaneously realizing the loading synchronization of the drugs.    USE - The calcium phosphate nano-carrier system is useful in fields of drug delivery and bone tissue repair (claimed).    ADVANTAGE - The method is simple, economical, environmental friendly and is suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing calcium phosphate nano-carrier system using above above.
NOVELTY - Bio-ethanol diesel mixed fuel comprises (in %) 95% hydrous ethanol (10-20), diesel (40-45), biodiesel (35-40) and cosolvent (5).    USE - Used as a bio-ethanol diesel mixed fuel.    ADVANTAGE - The mixed fuel: has great fuel performance; is environmental friendly and saves energy; can be stored for long time without layering; and has simple and economical production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-ethanol diesel mixed fuel, comprising providing 95% hydrous ethanol (10-20), diesel (40-45), biodiesel (35-40) and cosolvent (5), and firstly mixing diesel with biodiesel, then mixing with 95% hydrous ethanol and adding cosolvent to obtain the mixed fuel.
NOVELTY - The device has housing whose inner cavity is filled with particle catalyst and provided with several cold shock pipes to realize cold shock gas. The bottom of the housing is provided with cold shock gas inlets connected with the cold shock pipes. Each cold shock pipe is longitudinally ad circumferentially provided with 50-500 holes to realize cold shock gas whose pressure is 1-4 MPa and temperature is 200-300 degrees C.    USE - The device is used for the synthesis of methane.    ADVANTAGE - The temperature of device can be controlled during the methane reaction process and synthesis efficiency can be improved. The low cost safe and reliable of device can be achieved by large scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the reaction device. (Drawing includes non-English language text)
NOVELTY - Invention relates to anaerobic fermentation of organic mass, for example plant and household wastes, manure and waste water to obtain ecologically clean organic fertiliser and biogas, and can be used in housing maintenance and utilities, chemical industry, power engineering and agriculture. The apparatus has a reactor 1 which is in form of a bent pipe which is buried into the ground, on the ends of which there is are gas receivers 7, a vessel for the starting material with a crushing machine 3, a vessel for collecting refermented biomass 4, a receiver 5, a compressor 6, a gas holder 15 and a spiral curved heating element 9. The process of crushing the "crust", unloading, mixing and moving the organic mass along the spiral curved heating element 9 of the reactor 1 is performed with excess pressure of compressed gas which is in form of methane from gas tanks 32 and biogas obtained from anaerobic fermentation.    USE - Chemistry.    ADVANTAGE - Invention simplifies the design and use of the apparatus, increases reliability thereof, lowers capital costs on manufacturing, and also provides a highly efficient and stable process of decomposing biomass all year round. 1 dwg
NOVELTY - Regeneration of a spent acidic ion-exchange resin and its recycling involves: contacting the spent ion-exchange resin with an alcohol ion-exchange regenerant; contacting the spent ion-exchange resin with an acidic ion-exchange regenerant to recharge the acidic ion-exchange resin to produce a regenerated acidic ion-exchange resin; and contacting a metal- and water-containing biomass-derived pyrolysis oil with the regenerated acidic ion-exchange resin to produce a low metal, water-containing biomass-derived pyrolysis oil.    USE - For regeneration of a spent acidic ion-exchange resin and its recycling (claimed), particularly for producing biofuels.    ADVANTAGE - The low metal, low water biomass-derived pyrolysis oil having greater storage stability and higher energy density than the starting biomass-derived pyrolysis oil is produced by the method. The phase separation and solidification and/or charring that occurs with simple distillation at above 150 degrees C is prevented while reducing the water content of the oil. The reduced metal and water content, along with the greater storage stability and higher energy density, increases the suitability of the low metal, low water biomass-derived pyrolysis oil as a biofuel. In addition, the regeneration and recycling of the acidic ion-exchange resin and ion-exchange regenerants simplify processing, and reduce material and disposal costs.
NOVELTY - The system has a reaction zone provided in communication with an input stream at zone temperature of about 1700 degree Fahrenheit. Another reaction zone is provided in communication with the former zone, and is at zone temperature of about 1900 degree Fahrenheit in presence of steam to steam reform methane in the input stream or in an output stream of the former zone. A separation zone is provided in communication with the latter zone, and is at separation-zone temperature of less than 1600 degree Fahrenheit to remove solid or liquid species present in an output stream of the latter zone.    USE - Reformer system i.e. multi-zone reformer system, for reforming carbonaceous feedstock e.g. cellulosic biomass, to produce synthesis gas (syngas) utilized in chemical and biorefining industries. Can also be used for reforming agricultural waste, forest product, corn stover, wheat straw, coffee ground, miscanthus, animal manure, municipal rubbish, commercial waste and coconut shells, to produce syngas.    ADVANTAGE - The reaction zone reduces the presence of the refractory tars, and another reaction zone steam-reforms methane and other components from the former reaction zone, thus generating high quality synthesis gas suitable for converting into liquid fuels such as ethanol.    DETAILED DESCRIPTION - The former reaction zone reduces molecular weight of refractory tars present in the input stream to average molecular weight of 100 g/mol or less. The former reaction zone reduces a portion of benzene, toluene, ethylbenzene and xylenes (BTEX) species present in the input stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a reformer system.
NOVELTY - Catalyst (1) comprises a surface with catalytically active sites, where the surface (2) is at least partly coated with a coating (3) comprising at least one metal oxide.    USE - The catalyst is useful for selective catalytic reduction of nitrogen oxide (NOx) in alkali metal containing flue gas using ammonia as reductant, where flue gas originates from the firing of biomass (all claimed).    ADVANTAGE - The catalyst: exhibits improved resistance to alkali poisoning; has increased lifetime; is cost-effective, environmentally friendly and manufactured easily; and is suitable for selective catalytic reduction in the high-dust position on biofired power units.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing the catalyst, comprising: providing a support; impregnating the support with a first aqueous solution comprising a vanadium component; drying and calcining the impregnated support; coating the impregnated support with a second aqueous suspension comprising at least one metal oxide; and drying and calcining the coated support for a second time; and    (2) treating an uncoated catalyst for conferring an improved resistance to alkali poisoning during selective catalytic reduction of nitrogen oxide (NOx) using ammonia as the reductant, comprising coating the surface at least partly with the coating.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of scanning electron microscope image of a cross-section of a coated catalyst having a magnification of 150 times.    Catalyst (1)    Surface (2)    Coating (3)
NOVELTY - A polypeptide having xylanase activity which maintains at least 80% of its xylanase activity after 72 hours incubation in 50 mM phosphate buffer at 70 degrees C, is new.    USE - The polypeptide and composition are useful for the enzymatic degradation of lignocellulosic biomass (claimed), preferably for the selective hydrolysis of pentose sugar components of hemicellulose-containing plant biomass.    ADVANTAGE - The xylanase has enhanced thermostability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a nucleic acid encoding a polypeptide having an amino acid sequence with at least 70%, more preferably at least 75-95% sequence identity to the defined sequence of 307 amino acids (SEQ ID No: 1), given in the specification;    (2) a vector comprising the nucleic acid;    (3) a host cell transformed with the vector; and    (4) a method of producing a xylanase protein.
NOVELTY - A cemented carbide alloy joined material consists of metallic component (2) having joint surface (5), joining layer (4) containing copper and carbon provided on surface (5), and metallic component (3) bonded to layer (4) through joint surface (6). The component (3) contains tungsten carbide based cemented carbide. The joining layer contains carbon steel, alloyed steel and stainless steel.    USE - Cemented carbide alloy joined material used for die for honeycomb structure molding (claimed) used for catalyst carrier used in internal combustion engines, boilers, chemical reaction apparatus, modifier for fuel cells and fine particle collection filters for exhaust gas, and for precision tools.    ADVANTAGE - The cemented carbide alloy joined material with high joining strength and joining position accuracy is manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the cemented carbide alloy joined material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the cemented carbide alloy joined material.    Cemented carbide alloy joined material (1)    Metallic components (2,3)    Joining layer (4)    Joint surfaces (5,6)
NOVELTY - The artificial wetland phytoremediation sewage treating pool has a water collecting pool and a clean water pool which are orderly connected. A plant treating pool is connected with the water collecting pool through a standard height water collecting pipe. A water collecting pool is connected with the clean water pool through a standard height water inlet pipe. The clean water pool is discharged by a standard height water outlet pipe.    USE - Artificial wetland phytoremediation sewage treating pool.    ADVANTAGE - Incorporates biodegradation function and adsorption function of fillers. Utilizes salt tolerant plants to treat salty wastewater while reinforcing the saturation adsorption function of the salt tolerant bacteria strains and the fillers. Absorbs salt content within the sewage, and removes the plants out of the water. Decreases the salt content of the wastewater. Exhibits simple structure, good treating effect of wastewater, low cost, and effectively protects the ecological environment.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the artificial wetland phytoremediation sewage treating pool.
NOVELTY - An organic waste is supplied to a modification container, ignited and combusted using oxygen. Gas and water are supplied to the organic waste. The temperature water is increased with combustion heat. The water and organic waste are reacted, and the organic waste is subjected to reforming reaction. When the temperature of combustion nucleus which is hot section formed in center portion of organic waste is 400 degrees C or less by continuously supplying gas and water to organic waste, the size of combustion nucleus is fixed.    USE - Modification of organic waste e.g. municipal solid waste and industrial waste used for generating hydrogen gas for fuel cell. The modified organic waste is used as fertilizer.    ADVANTAGE - The method enables modification of organic waste, without using combustion agent, and leakage odor and harmful gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (10) for modifying organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the apparatus for modifying organic waste.    Apparatus for modifying organic waste (10)    Water supply unit (20)    Exhaust gas processing unit (21)    Temperature sensor (22)    Gas introduction tube (23)
NOVELTY - Formulation process to obtain fuel granules from biomass comprises: identifying plant raw material from biomass for selecting candidate components (A); chemical and thermo-chemical analysis of (A); studying the physical characteristics of (A); establishing a summarizing table of chemical, thermochemical and physical characteristic of (A); selecting among (A) of a base product; regulating and optimizing the melting temperature of ash and corrosivity and toxicity of smoke; optimizing granulation process of base/mineral core product mixture; and control testing by large scale combustion.    USE - The formulation process is useful to obtain fuel granules from biomass.    ADVANTAGE - The process is cost effective and eco-friendly for obtaining fuel granules with predefined porosity.    DETAILED DESCRIPTION - Formulation process to obtain fuel granules from biomass comprises: identifying the plant raw material that is any locally available biomass for selecting candidate components that can be used for fabrication of fuel granules; chemical and thermo-chemical analysis of candidate components thus selected; studying the physical characteristics of candidate compounds; establishing a summarizing table of chemical, thermochemical and physical characteristic of candidate components; selecting from summarizing table and among the candidate components of a base product containing one or generally at least two base components to be mixed for obtaining, after granulation, fuel granules; regulating and optimizing by analyzing the established summary table, the melting temperature of ash and corrosivity and toxicity of smoke derived from combustion of the base product by adding a mixture of mineral additive core; optimizing the process of granulation of base/mineral core product mixture; and control testing by large scale combustion.
NOVELTY - The high-efficiency infiltrating underflow type complete plant has two pipes in which one of the pipes includes a smaller diameter and the other has larger diameter in the double-pipe infiltrating water distributor and are drilled holes at equal space. The two pipes are sleeved with each other. The pipe with smaller diameter is placed in the pipe with larger diameter. One end of the inner pipe is connected with a seal head.    USE - High-efficiency infiltrating underflow type complete plant for artificially ecological wetland.    ADVANTAGE - Exhibits simple and convenient installation of underflow type sewage processing system of artificially ecological wetland, long stability and high-efficiency operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the high-efficiency infiltrating underflow type complete plant for artificially ecological wetland.
NOVELTY - An organic-refuse compost manufacturing apparatus has a fermentation tank (1) having vertical component, closed end, upper portion, an opening wall surface and a multi-opening, a corrugated-cardboard wound around the surface of outer wall, a panel heater wound around one portion of wall surface, and a stirring rod and an auger (11) attached to the rotating shaft (5) of center portion of tank.    USE - Apparatus is used for manufacturing organic-refuse compost for domestic use.    ADVANTAGE - The apparatus quickly and instantly enables processing of organic refuse. High quality compost is produced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of organic refuse compost manufacturing apparatus.    Fermentation tank (1)    Drive motor (2)    Shaft (5)    Organic refuse (8)    Auger (11)    Compost (15)
NOVELTY - Biodiesel composition includes vegetable oils, short-chain alcohols, acid additives and high cetane ethers containing fatty acids. The short-chain alcohols are used in chemical industry, agriculture, automobile and energy sectors. The vegetable oils are fixed oils or fatty acids from refining of vegetable oils, edible oils, frying oils, industrial wastes, sewage and animal fats.    USE - Biodiesel composition.    ADVANTAGE - The biodiesel composition reduces eco-friendly contaminations and can be prepared in a simple and eco-friendly manner.
NOVELTY - Method for stimulating natural fermentation of organic sludge, involves baking diatomaceous earth and wooden fragment, carbonizing the baked material, crushing the carbonized material into granular particles of uniform size or different sizes, and adding the granular particles to the organic sludge.    USE - The method is useful for stimulating natural fermentation of organic sludge.    ADVANTAGE - The method does not require special technology and is inexpensive. Stable supply of carbonized material to organic sludge contributes to an advanced environmental clean up and industrial utilization.
NOVELTY - Metal removing agent (3) (I) made of resin having anionic functional group of a functional group density of 2-25 mmol/ml, is claimed.    USE - (I) is useful: for removing metal clusters from fuel, which is one of light oil and biodiesel fuel, and in a metal removing filter (all claimed).    ADVANTAGE - The metal removing filter has high chemical reactive property, which prevents metal components contained in the fuel from being deposited to the inside of each of the injectors of an internal combustion engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a metal removing filter (1) comprising a container (2) and (I) placed in the container.    DESCRIPTION OF DRAWING(S) - The figure shows a diagrammatic view of a metal removing filter.    Metal removing filter (1)    Container (2)    Metal removing agent (3)    Mesh (41)    Fuel inlet part. (61)
NOVELTY - Device comprises: chemical hydride fuel pellet or hydrogen generating fuel pellet having many holes extending from first end to second end; many tubes (210) formed of water vapor permeable and hydrogen impermeable material, extending from first to second end through the holes to provide water vapor containing airflow through fuel pellet; container (220) having an inlet (225) for water vapor containing gas coupled to first end of tubes, and an outlet (230) coupled to second end of the tubes, where container surrounds fuel pellet and tubes; and hydrogen outlet coupled to fuel pellet.    USE - The device is useful for producing hydrogen (claimed), which is useful in man-portable power and micro air vehicle applications.    ADVANTAGE - The device provides 4-5 times of the hydrogen of commercially available hydrogen sources of the same size and weight.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing hydrogen comprising: flowing humid air through many tubes formed of water vapor permeable and hydrogen impermeable material extending from a first end to a second end of the tubes; permeating the water vapor through walls of the tubes into a chemical hydride fuel pellet through which the tubes extend; and producing hydrogen via a reaction of fuel with the water vapor and exhausting the hydrogen through a hydrogen outlet.    DESCRIPTION OF DRAWING(S) - The figure shows a block cross section diagram of a hydrogen generator.    Tubes (210)    Chemical hydride fuel (215)    Gas-impermeable container (220)    Inlet of container (225)    Outlet of container (230)
NOVELTY - Method for pretreating biomass, involves contacting water-reactive anhydride with water-containing biomass in closed reactor to induce internal heating for increasing internal reactor temperature from ambient temperature, where the internal reactor temperature is regulated by (a) input amount or input flow rate of the water-containing biomass, (b) ratio of dry weight of the biomass to the weight of water, (c) the pressure of the water-reactive anhydride, and (d) the input amount or the input flow rate of the water-reactive anhydride.    USE - The method is useful for pretreating biomass, preferably lignocellulosic biomass or algal biomass for producing biofuel or biochemical (all claimed). The biofuel includes diesel and alcohol. The biochemical includes antigen, antibody, hormone, amino acid, haptens, protein and enzymes.    ADVANTAGE - The method can be performed even at low temperature with low energy consumption and reduced amount of chemicals, and is cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of producing biofuel or biochemical, involves converting a polysaccharide obtained from the pretreated biomass into monosaccharides, and fermenting the monosaccharides; and    (2) apparatus for pretreating biomass, comprising (a) reaction unit for pretreating biomass, where the reaction unit comprises an inlet portion at one end for inputting water-reactive anhydride, and an outlet portion at an opposite end for outputting water-reactive anhydride, a supply unit for supplying a biomass to the reaction unit, and a separation unit for separating components extracted from the biomass.
NOVELTY - Processing biomass to hydrocarbons and oxygenates, comprises: either (a) providing (102) a biomass feedstock, (b) de-oxygenating (104) the biomass feedstock to form a solid intermediate, (c) liquefying the solid-intermediate to produce a biocrude, and (d) processing (110) the biocrude by one or more refining means to produce one or more hydrocarbons; or steps (a) and (b) as above per se, heating (106) the solid-intermediate from step (b) to produce one or more volatile gases, quenching (108) to condense the one or more volatile gases, hence generating a biocrude, and step (d) as above per se.    USE - The process is useful for processing biomass to hydrocarbons and oxygenates (claimed), where the hydrocarbon is useful: as fuel e.g. biodiesel and ethanol; and in blends with conventional fuels such as gasoline and diesel.    ADVANTAGE - The hydrocarbon avoids corrosion problem, and improves storage stability of fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart of a process of processing biomass to hydrocarbons and oxygenates.    Providing biomass feedstock (102)    De-oxygenating biomass feedstock (104)    Heating solid-intermediate (106)    Quenching step (108)    Processing biocrude. (110)
NOVELTY - Production of bio-oil from phototrophic and heterotrophic algae, involves culturing phototrophic algae and heterotrophic algae to obtain first aqueous suspension and second aqueous suspension respectively, concentrating first aqueous suspensions, combining with second aqueous suspension to obtain third aqueous suspension, concentrating third aqueous suspension to obtain concentrated aqueous suspension of algal biomass, and subjecting to thermal treatment to obtain an oily phase comprising bio-oil and aqueous phase comprising organic compounds.    USE - Production of bio-oil and organic compounds e.g. sugars, carboxylic acids, glucoside fractions and proteins. The bio-oil is useful in production of biofuels for motor vehicles.    ADVANTAGE - The method provides high yield of bio-oil and organic compounds by simple and cost effective process.    DETAILED DESCRIPTION - Production of bio-oil from phototrophic and heterotrophic algae, involves (a) culturing at least one phototrophic algae under photoautotrophic conditions to obtain a first aqueous suspension of algal biomass, (b) culturing at least one heterotrophic algae under heterotrophic conditions to obtain a second aqueous suspension of algal biomass, (c) subjecting the first aqueous suspension of algal biomass to concentration to obtain a first concentrated aqueous suspension of algal biomass, (d) combining the first concentrated aqueous suspension of algal biomass with the second aqueous suspension of algal biomass and obtaining a third aqueous suspension of algal biomass, (e) subjecting the third aqueous suspension of algal biomass to concentration to obtain a second concentrated aqueous suspension of algal biomass, and (f) subjecting the second concentrated aqueous suspension of algal biomass to thermal treatment to obtain an oily phase comprising bio-oil and an aqueous phase comprising organic compounds such as sugars, carboxylic acids, glucoside fractions and proteins.
NOVELTY - Treating coal comprises contacting coal with at least one member comprising aromatic alcohols or cycloaliphatic alcohols to solubilize at least a portion of the coal.    USE - The method is useful for treating coal, where the coal is lignite, brown coal, sub-bituminous coal, bituminous coal, and anthracite (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the treated blend formed by the method;    (2) a composition comprising the solubilized aromatic or cyclic alcohol derivatives of coal; and    (3) a bioconversion method comprising contacting the treated coal with a bioconversion agent to bioconvert the coal.
NOVELTY - A composition (C1) for production of a fermentation end-product comprises: (a) a carbonaceous biomass; (b) a microorganism (G1) that processes the biomass to produce the fermentation end-product; and (c) at least one exogenous antioxidant agent.    USE - For the production of a fermentation end product, preferably an alcohol (more preferably butanol, ethanol, or propanol, particularly ethanol) (all claimed), useful as biofuels, or for producing other chemicals.    ADVANTAGE - The use of a modified microorganism to enhance the activity of antioxidant, such as catalase, in the process during the fermentation of biomass improves the production of alcohols or biofuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing (M1) a fermentation end-product involving: contacting a carbonaceous biomass with at least one microorganism that processes the carbonaceous biomass to produce the fermentation end-product and at least one agent capable of antioxidant activity; and    (2) a kit for production of biofuel from biomass comprising: (a) a microorganism that processes the carbonaceous biomass to produce the fermentation end-product; and (b) an antioxidant.
NOVELTY - The biomass gasifier has an upper spiral stirring transmission shaft (1), a lower spiral stirring transmission shaft (2), an upper inner boiler barrel (3), an upper outer boiler barrel (4), a lower inner boiler barrel (5), a lower outer boiler barrel (6), a feeding port (7), a discharge port (8), a connecting port (9), an air outlet (10), a combustion chamber (11), an upper transmission wheel (12), a lower transmission wheel (13), a driven wheel (14) and a bearing seat (15). The upper spiral stirring transmission shaft and lower spiral stirring transmission shaft are of spiral shapes.    USE - Biomass gasifier.    ADVANTAGE - Gasifier uses spiral transmission to stir and transmit the gasification raw material, heats the inner boiler barrel at high temperature by increasing an outer combustion chamber so as to thermally decompose the gasification raw material in the boiler cylinder, thus, sufficiently decomposing and volatilizing the gasification raw material in the boiler barrel, and returning the tar generated along with the fuel gas into the combustion chamber as a heating fuel via separation. Gasifier has stable gas production and high heat value without oxidation dissociation loss, which is ideal selection for users.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the biomass gasifier.    Upper spiral stirring transmission shaft (1)    Lower spiral stirring transmission shaft (2)    Upper inner boiler barrel (3)    Upper outer boiler barrel (4)    Lower inner boiler barrel (5)    Lower outer boiler barrel (6)    Feeding port (7)    Discharge port (8)    Connecting port (9)    Air outlet (10)    Combustion chamber (11)    Upper transmission wheel (12)    Lower transmission wheel (13)    Driven wheel (14)    Bearing seat (15)
NOVELTY - The furnace has a furnace cover and a feed port which are arranged on the upper part of the furnace body; a spark ignition engine, a fire grate and a discharge port which are arranged on the lower part of the furnace body; a water jacket with opened top connected with the water inlet pipe and arranged in the furnace body; a water seal between the furnace cover and the furnace body; and a discharge port in water seal by a water tank. The furnace body is connected with a washing tower with spray pipe, a fan and an air storage kettle, respectively.    USE - Carbonization gasification furnace for straw, garbage and fire coal.    ADVANTAGE - Raw materials are carbonized and gasified in the furnace body at the same time, and are used sufficiently. Entire process is operated hermetically without environmental pollution. Economical effect is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the carbonization gasification furnace of straw, garbage and fire coal.
NOVELTY - The system has furnace front storage device that includes buffer bin and working bin. The charging hole of working bin is jointed discharging hole of buffer bin. A working bin first material level meter is arranged on upper portion of working bin, for sensing material level. A valve control unit controls buffer bin and working bin valve to open and close according to transmitted signal. A flame detector senses flame of diffusion device. An ignition control unit controls on and off condition of ignition device based on signal transmitted from flame detector.    USE - Automatic control system for controlling feeding and diffusion of biomass gas, used in biomass gasifying reaction system (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass gasifying reaction system. The front face feeding device feeds material from working bin discharging hole to charging hole.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of automatic control system. (Drawing includes non-English language text)
NOVELTY - Double acting device is functionalized to convert garbage to compost with helping breeding of earthworms to produce humus and compost meal.    USE - Double acting device for composting organic waste for domestic purpose.    ADVANTAGE - The double acting device is energy saving device.
NOVELTY - The hydrothermal decomposition apparatus has a main structure (42) into which pressurized hot water (15) and a solid biomass feedstock (11) are supplied to decompose solid biomass feedstock using pressurized hot water. The temperature measurement units (T1-T8) measure inside temperature of main structure. A control unit (100) controls temperature inside main structure based on measured temperature. An inside temperature maintenance unit maintains supply temperature of pressurized hot water in range of 180-240 degrees C, for fixed time.    USE - Hydrothermal decomposition apparatus for decomposing biomass feedstock for manufacturing organic raw material e.g. alcohol, petroleum substitute products or amino acid (all claimed).    ADVANTAGE - The biomass feedstock can be decomposed easily and efficiently so that organic raw material can be produced, while reducing the decline in yield of sugar liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing system of organic raw material, which has a preprocessor that pre-processes biomass feedstock containing cellulose and hemicellulose. An enzymatic-decomposition apparatus performs enzymatic decomposition of cellulose in biomass solid content discharged from the biomass hydrothermal decomposition apparatus so as to produce sugar liquid containing hexose. A sulfuric acid decomposition apparatus decomposes hemicellulose component in hot-water discharge liquid discharged from hydrothermal decomposition apparatus so as to produce sugar liquid containing pentose. Alcohol, petroleum substitute products, or amino acids are produced by fermentation of sugar liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrothermal decomposition apparatus. (Drawing includes non-English language text)    Solid biomass feedstock (11)    Pressurized hot water (15)    Main structure (42)    Control unit (100)    Temperature measurement units (T1-T8)
NOVELTY - The high-expansion crystalline glass composition has the following components by molecular percentage: 50-70 percent (%) of magnesia, 1-15% of barium oxide, 8-25% of boric acid, 8-23% of silica, 3-15% (however 3 % is not included) of phosphate. The magnesia and phosphate crystal will be precipitated when heat-processed.    USE - High-expansion crystalline glass composition used as adhesive material for hermetic sealing of e.g. a support body board, an electrolyte and an electrode, which are used when producing fuel cells. Uses include but are not limited to solid oxide type fuel cell (SOFC), phosphoric acid type fuel cell (PAFC), molten carbonate type fuel cell (MCFC) and solid polymer type fuel cell (PEFC).    ADVANTAGE - Fluidity suitable for sealing in the heating process is ensured since there is much content of phosphate and the thermal expansion coefficient of composition is about (100-130)x (10(-7)) per degree centigrade after heating process. Stable heat resistance is securable over a long period of time since precipitation of phosphate crystal is accelerated and heat resistance is maintained even when exposed to high temperature over a long period of time or temperature rises abnormally.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory drawing which shows the basic structure of solid oxide type fuel cell.    Electrolyte (1)    Anode (2)    Cathode (3)    Support body board (4)    Fuel channel (4a)    Air channel (5a)
NOVELTY - Method for manufacturing solid fuel, involves adjusting moisture content of the wood biomass to 15-50 %mass and mixing the wood biomass with water oil.    USE - The method is useful for manufacturing solid fuel.    ADVANTAGE - The method is convenient to perform. The solid fuel improves adhesivity over conveyance path and capable of emitting large amount of heat.
NOVELTY - A fuel cell electric power generation system (10) comprises hydrogen generation unit which generates liquid which is rich in hydrogen and benzene from cyclohexane supplied from fuel container (11) and has hydrogen producing part (12) having electrode and pulse-power power supply (13) which supplies pulse voltage between electrodes, hydrogen separation unit which separates liquid which is rich in hydrogen and benzene from hydrogen generation unit, and fuel cell (15) with anode pole and cathode pole.    USE - Fuel cell electric power generation system used in hydrogen production apparatus (claimed).    ADVANTAGE - The fuel cell electric power generation system generates highly purified hydrogen and benzene by simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell electric power generation system. (Drawing includes non-English language text).    Fuel cell electric power generation system (10)    Fuel container (11)    Hydrogen producing part (12)    Pulse-power power supply (13)    Fuel cell (15)
NOVELTY - Processing high-concentration sewage of oil refinery, comprises introducing sewage after deoiling treatment into a biomembrane reactor to perform biological treatment and using microorganism to degrade the pollutant, adding oxidant during biological treatment, which comprises gaseous oxidant and liquid oxidant, introducing the gaseous oxidant into the reactor through a special inlet by air pump and dispersing in the sewage after passing through a gas disperser, and mixing the liquid oxidant with water through pipeline mixer and allowing to enter the reactor.    USE - The method is useful for oxidizing and decomposing non-degradable macromolecular organic matter into micromolecular organic matter.    ADVANTAGE - The method: improves biodegradability of sewage; inhibits the overgrowth of biomembrane and generation of residual activated sludge without affecting the biological activity; and is simple and economical.
NOVELTY - The device has a reactor (1) with a cylindrical cavity (50), a feeding device (48) for fresh biomass e.g. pellet (52), and a particle filter (40) for used and gasified biomass. An agitating arm (68), an agitator shaft (70), a gear mechanism (72) and two freely movable balls (66) are arranged in the cavity, where the balls are made of metal and heatable from outside the cavity by applying electromagnetic energy. The cavity is arranged in an inclined manner with respect to a base plate (60) during an operation, such that the biomass to be gasified is moved toward a pull-off lock (56).    USE - Device for producing gas from biomass for operating a combustion engine that is utilized for driving an electrical generator (all claimed). Uses include but are not limited to wood, pellet, saw dust and sewage sludge.    ADVANTAGE - The agitating arm, the agitator shaft, the gear drive and the two freely movable balls are provided in the cavity, where the balls are made of metal and heatable from outside the cavity by applying the electromagnetic energy, thus enabling the device to produce the gas in a highly-efficient and reliable manner and allowing the device to use various types of biomasses for producing the gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reactor of a device for producing gas from biomass.    Reactor (1)    Particle filter (40)    Feeding device (48)    Cylindrical cavity (50)    Fresh biomass (52)    Pull-off lock (56)    Base plate (60)    Freely movable balls (66)    Agitating arm (68)    Agitator shaft (70)    Gear mechanism (72)
NOVELTY - Process for pretreatment of crude vegetable or animal oil comprises passing the oil in a reactor comprising at least one fixed bed of at least one adsorbent comprising a porous refractory oxide free of catalytic metals comprising groups of 6 and 8-12, at a temperature of 130-320 degrees C, a pressure of 0.1-7 MPa with a residence time of the oil on the fixed bed of 0.1-1 hour.    USE - The process is useful for the production of the middle distillates base (claimed), diesel and/or jet fuel.    ADVANTAGE - The process is eco-friendly and inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for the production of a middle distillates base comprising (a) the pretreatment process; (b) hydrotreatment of the pre-treated effluent from the step (a) in the presence of at least one fixed bed catalyst, at a temperature of 200-450 degrees C, under a pressure of 1-10 MPa, an hourly space velocity of 0.1-10 h-1 and in the presence of a total amount of hydrogen mixed with filler such as the ratio of hydrogen/feed is 70-1000 Nm3 of hydrogen/m3 of filler; and (c) separating hydrogen, gas and at least one diesel base from the hydrotreated effluent from the step (b).
NOVELTY - Preparing lipid by microalgae, comprises: (a) growing photosynthetic microalgae; (b) culturing microalgae in stress conditions inducing an overproduction of fat by microalgae; (c) extracting lipid produced by the microalgae followed by storing or recovering lipid, where the process comprises circulating an aqueous stream comprising, by mixing, microalgae, carbon dioxide and nutrients within at least one tubular reactor located in a buried well (4, 6, 8) provided with means for irradiation of microalgae to ensure the photosynthesis, in the step (a).    USE - The lipid is useful as biofuel.    ADVANTAGE - The process is cost effective for preparing the lipid with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for installation for the implementation of the process, particularly a pre-existing industrial site, comprising: means (2) to provide an aqueous stream comprising, by mixing, micro-algae, carbon dioxide and nutrients; a region (3) of photosynthetic growth of microalgae of the aqueous stream, comprising at least one tubular reactor to convey the aqueous stream, the tubular reactor being located within a buried well (4, 6, 8) equipped with a means for irradiating microalgae to ensure photosynthesis; a reactor (9) for algal lipid overproduction, comprising means for culturing microalgae obtained from the photosynthetic growth zone, in stress conditions inducing the production of lipid by microalgae; and means (10) for extracting lipid produced by microalgae in algal lipid synthesis zone, generally associated with means of storing and/or recovering the lipid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of an installation for the implementation of the process.    Means for providing an aqueous stream (2)    Photosynthetic growth region (3)    Buried well (4, 6, 8)    Reactor for algal lipid overproduction (9)    Means for extracting lipid. (10)
NOVELTY - Saccharomyces cerevisiae strain (A) comprising a strain deposited in CNCM under 1-4264 number and a strain deposited in CNCM under 1-4265 number, is new.    USE - The yeast strain is useful for producing alcohol (all claimed) including beer, wine or distillery, fermented beverages and/or alcohol for biofuel or chemical industries.    ADVANTAGE - The yeast strain is resistant to a toxic medium.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) method for selecting a yeast strain resistant to a toxic medium comprising: fermenting at least one yeast strain in a toxic selection medium and non-toxic selection medium; adding an initial composition of the toxic selection medium and non-toxic selection medium to non-ionized organic acid in a toxic concentration; introducing a sugar as the limiting factor for fermentation in toxic- and non-toxic-selection medium; and selecting at least one yeast strain in which the amount of alcohol produced at maximum time (tmax) in the toxic selection medium is greater than or equal to 65% of the amount of alcohol produced at tmax by the strain in the non-toxic selection medium;    (2) yeast strain obtained by the method;    (3) yeast obtained by culturing a yeast strain; and    (4) process-I of producing alcohol comprising fermenting the yeast in a fermentation medium.
NOVELTY - Multivalent ammonium phosphate fertilizer based on organic raw material comprises calcium phosphate carrier of organic origin and a catalyst, where the fertilizer is multi-nutrient fertilizer, preferably nitrogen-phosphorus-sulfur or nitrogen phosphate fertilizer based on organic raw material, and is formed in a granular form.    USE - The ammonium phosphate fertilizer is useful in agricultural areas and in horticultural- and ornamental plant areas, and as a component of flame retardant (claimed). No biological data given.    ADVANTAGE - The process for producing the fertilizer: is an energy efficient process; uses less-polluted renewable raw material; and releases water that is utilized for the dissociation of the reactants and for the formation of calcium sulfate and granules.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for producing the fertilizer comprising mixing the constituents of the fertilizer in a stoichiometric ratio in a continuous mixer and formulating into a homogeneous mixture.
NOVELTY - Producing fuel from sewage sludge linked with heavy metals immobilization, involves: adding glauconite in an amount of (0.2-2% on sludge dry matter basis) to a mixture of sewage sludge and coal. The glauconite is added in the form of sand and gluconite mixture having gluconite content of (45-55%) in an amount of (0.4-4% on sludge dry matter basis).    USE - For producing fuel from sewage sludge linked with heavy metals immobilization (claimed). The ash and slag produced is useful in highway engineering.    ADVANTAGE - The method provides improved method for utilization of sewage sludge by conversion into fuels, than the prior art thermic methods such as pyrolysis, or mixing sludge with dolomite and treating the solid phase with steam; where the drawback of these solutions is that a secondary discard i.e. fly ash containing high amounts of non-converted carbon is produced. Further the discard is difficult to utilize also because it contains mobile and over the standard amounts of heavy metals. The method of mixing sewage sludge and coal with glauconite has beneficial effect of immobilization of heavy metals in ash and slag, which in consequence allows for safe storage of ash and slag in damps or its use in highway engineering.
NOVELTY - Disclosed is a vermicomposting system and method. The system comprises several parallel stacks arranged between a loading module and an unloading module, and several vermicomposting modules mounted in each stack. The stack is inclined downwardly sloping towards the unloading module. The slope of the stack is based on the desired rate of free movement of the vermicomposting modules under gravity along the stack from loading module end to unloading module end. Image 0/0
NOVELTY - Absorbent solution (A) comprises: (a) at least one amine; (b) water; and (c) at least one degradation-inhibitor compound to reduce the degradation of the amine, where the degradation-inhibitor compound has thiourea structure of formula (R2-NR1-C(=S)-NR3-R4) (I).    USE - (A) is useful for absorbing acidic compounds contained in a gaseous effluent, which is a natural gas, flue gas, synthesis gas, refinery gas, a gas obtained from Claus process, biomass fermentation gas, cement gas or fumes from incinerator, where the gaseous effluent contains at least 500 ppm by volume of oxygen (all claimed).    ADVANTAGE - The absorbent solution exhibits improved thermal and chemical stability against effluent impurities, preferably oxygen, sulfur oxides and nitrogen oxides.    DETAILED DESCRIPTION - Absorbent solution (A) comprises: (a) at least one amine; (b) water; and (c) at least one degradation-inhibitor compound to reduce the degradation of the amine, where the degradation-inhibitor compound has thiourea structure of formula (R2-NR1-C(=S)-NR3-R4) (I).    R1-R4 = H, 1-8C hydrocarbon, 5-8C aryl or heterocyclic group, 1-8C hydroxyalkyl, 1-8C alkoxy-1-8C alkyl, keto-1-8C alkyl, group of formula (-C(=NH)-NH2), group of formula (-NH-C(=S)-NH2), group of formula (-C(=S)-NX-Y1), or group of formula (-NX-Y1); and    X, Y1 = H, 1-8C hydrocarbon or 5-8C heterocyclic or aryl group.
NOVELTY - Manufacture of organic fertilizer comprises using organic wastes i.e. urban sewage sludge and livestock and poultry manure as raw materials; and adding crushed roots of stalked plants and dry materials of the upper part of stalked plants, indigenous bacteria, filamentous fungi, bacteria, actinomycetes, lactic acid bacteria, and yeast.    USE - Manufacture of organic fertilizer (claimed).    ADVANTAGE - The process provides organic fertilizer, which can reduce fertilizer inputs, protect the rural environment, and create good agricultural ecosystems, which can cultivate fertilized soil, realize high and stable yields, and increase both production and income.    DETAILED DESCRIPTION - Manufacture of organic fertilizer using organic wastes i.e. urban sewage sludge and livestock and poultry manure as raw materials comprises adding crushed additive A into the raw material for composting; adding an additive B; ventilating; stirring; conducting cooling treatment when temperature of materials reaches above 70 degrees C; adding an additive C and stirring when temperature of materials is cooled at 65 to 45 degrees C; adding an additive D and stirring when temperature of materials is cooled at 45-25 degrees C; and drying the materials and forming. The additives A are roots of stalked plants and dry materials of the upper part of stalked plants. The additive B includes indigenous bacteria, filamentous fungi, bacteria, actinomycetes, lactic acid bacteria, and yeast for breaking down cellulose. The additive C includes indigenous bacteria, filamentous fungi, bacteria, actinomycetes, lactic acid bacteria, and yeast for breaking down protein polymer compound. The additive D includes indigenous bacteria, filamentous fungi, bacteria, actinomycetes, lactic acid bacteria, and yeast for increasing the composting of labile polymer compound.
NOVELTY - A low density straw block used as raw material of biogas; where the density of the straw block is 0.3-0.6 g/cm3; is new.    USE - The low density straw block is useful as raw material of biogas (claimed).    ADVANTAGE - The low density straw block is directly packed, transported and stored, and directly dissolved in water at pre-processing stage during biogas production to enhance work efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the low density straw block used as raw material of biogas.
NOVELTY - A furnace body and a combustible gas treatment component are connected through a combustible gas pipeline. The combustible gas treatment component comprises a biomass gasification furnace, smoke dust processor, combustible gas purifier and combustible gas condenser. An outlet of the combustible gas condenser is connected with a combustible gas inlet of a lower burner through a combustible gas pipeline with a draught fan. A discharge opening of a lower roasting chamber is connected with a carbon powder watering cooler, carbon powder non-sieve crusher and carbon powder bar maker.    USE - Carbon making device using sludge.    ADVANTAGE - Capable of completely and quickly treating sludge, provides good carbon making effect and high energy recycling rate, and is more economical than burning treatment. Sludge is subjected to closed treatment without contact with outside, thus keeping working place sanitary and clean.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon making device.
NOVELTY - The production line has a feed opening of a garlic powder production device which is connected with a garlic waste slag outlet of a garlic oil production device. The slag outlets of a soybean oil production device, a corn oil production device and a garlic oil production device are respectively connected with the feed opening of the biological granulated feed production device. The garlic peel slag outlet of the garlic oil production device is connected with the feed opening of a straw coal production device.    USE - Production line of agricultural product such as soybean oil, corn oil, garlic oil, etc.    ADVANTAGE - The soybean oil, corn oil and garlic oil can be efficiently produced by using waste materials to produce biological granulated feed and also capable of producing straw coal by using straw and garlic peel slag in production process of garlic oil. The raw material can be sufficiently used such that the material consumption can be reduced at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the production line of agricultural product.
NOVELTY - Seedling growing biological substrate is obtained by processing paper-making sludge, where the paper-making sludge comprises bio-fertilizer (30-50%), pearlite (10-20%) and balanced vermiculite. Functional bacterium (1-2 kg/cube) is added to the substrate.    USE - Seedling growing biological substrate.    ADVANTAGE - The seedling growing biological substrate is economic and has sufficient nutrition amount. The substrate is helpful for growing fresh green leaves and strong stems and root system with diseases preventing function.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing seedling growing biological substrate, which involves:    (A) mixing paper-making sludge and wheat bran or crop straws with bacterium strain and piled fertilizer;    (B) piling the mixture in a fermentation groove;    (C) using 2-3 kg/cube of fermentation bacterium strain with the piled fertilizer to ensure moisture content of the mixture at 50-60% and carbon-nitrogen ratio at 25-30;    (D) fermenting the mixture in the fermentation groove and heating the mixture;    (E) turning up the fermentation material in groove by using a turner at temperature of material rises to 65-75 degrees C;    (F) cooling and heating the mixture repeatedly;    (G) carrying fermentation for 30 days;    (H) reducing moisture of the mixture up to 30-40%;    (I) drying the fermented material in air and then grinding it to obtain the paper-making sludge fertilizer;    (J) weighing paper-making sludge fertilizer accounting, pearlite and vermiculite, and then adding them with functional bacterium; and    (K) mixing the material to obtain finished product.
NOVELTY - Organic fertilizer is prepared by using (in wt.%): baking agent (0.2-0.4), oil cake (0.4-0.6), white sugar (0.1-0.2), urea (1.5-3), zeolite powder (1-2) and balanced garden waste.    USE - Organic fertilizer used as microbial organic fertilizer.    ADVANTAGE - The organic fertilizer has short fermenting period and high contents of organic matters and humus, where content of total nutrition meets national standard of the organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves mixing (in wt.%): baking agent (0.2-0.4), oil cake (0.4-0.6), white sugar (0.1-0.2), urea (1.5-3), zeolite powder (1-2) and balanced garden waste, and then fermenting the mixture to obtain organic fertilizer.
NOVELTY - A regulation and control test device for preparing bio-oil by using fast thermal cracking of biomass, comprises a fluidized bed pyrolytic reactor, a cyclone separator, a coarse filter, a fixed bed thermal cracking reactor, multi-path sampling valves, a gas chromatographs, condensers, oil storing tanks, a high-temperature oil circulation groove, low-temperature circulation grooves, a suit of tail gas circulation device and a gas storing tank. Full definition of the device is given in Full Definitions under DEFINITIONS field.    USE - The regulation and control test device is used for preparing bio-oil by using fast thermal cracking of biomass (claimed).    ADVANTAGE - The device has the test functions such as fast thermal cracking, catalytic cracking, online analysis and regulation and control and leveled controllable condensation. The device has compact structure, performs stable work, and capable of analyzing all the components of the pyrolysis gas and evaluating the catalyst. It gives reliable and quantitative results. The device can effectively regulate and control test for the preparation of bio-oil.
NOVELTY - The method involves forming rough gas in a gasifier by biomass fuels. Distilling, splitting and reduction reaction of non-separated weak tar-containing waste water is conducted in a high-temperature oxygen-deficient environment in a splitting injection device to form gas and high-temperature vapor. The rough gas is transferred into a splitting stove. The waste water is converted into another gas by a preheating room and a splitting room of the splitting stove. The latter gas is burnt with the former gas in the burning room that is provided with stereoscopic supplying oxygen.    USE - Method for purifying straw gasification fuel gas.    ADVANTAGE - The method enables installing a tar-waste water converting device and a stereoscopic oxygen-supply device on a stove, so that small amount of the non-separated tar waste water is fully converted into flammable gas and transferred into the burning room for burning in a stereoscopic oxygen-supplying environment to realize zero releasing of tar and waste water in gasifying fuel gas after the gas passing through a purification device. The method enables saving 10-15 percent of fuel and providing easy igniting effect for sufficient burning by utilizing non-releasing toxic gas with environmental-friendly property, thus increasing 72 percent gasification efficiency and providing 100-200 degrees centigrade of burning temperature to the stove.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a purification equipment for straw gasification fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a purification equipment.'(Drawing includes non-English language text)'
NOVELTY - A citronella oil bud inhibiting agent comprises 5-10 pts.wt. citronella oil, 80-85 pts.wt. beta -cyclodextrin and 5-10 pts.wt. stearic acid. The agent is derived from citronella oil of natural plant by steam distillation or supercritical carbon dioxide extraction. In the supercritical carbon dioxide extraction, temperature is 40-50 degrees C, and the pressure is 10-30 MPa. At first, 5-10 pts.wt. citronella oil and 80-85 pts.wt. beta -cyclodextrin are fully mixed and agitated in a sealing container, and then 5-10 pts.wt. stearic acid is added, and then sealed after mixing and agitating.    USE - A citronella oil bud inhibiting agent used for sprout inhibition in potato storage process (claimed).    ADVANTAGE - The agent adopts citronella oil derived from natural plant as active ingredient; can effectively inhibit sprouting during the potato storage, reduce or avoid the chemical substance; and has good bud inhibiting effect and environmental friendliness.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for citronella oil bud inhibiting agent applied to sprout inhibition in potato storage process.
NOVELTY - Preparation of composite biological pellet fuels comprises concentrating oily sludge, adding flocculant into concentrated sludge to mix and react, dewatering flocculated sludge, mixing dewatered sludge and biological materials, synchronously adding preservative, extruding and forming uniformly mixed materials by extruding-forming machine.    USE - Method for preparing of composite biological pellet fuels (claimed).    ADVANTAGE - The main raw materials of the biological pellet fuel are natural reproducible forestry residues, thus reducing environment pollution and energy consumption; and the produced biological pellet fuel has high calorific value, low burning point, and low cost and neutral, and harmless.
NOVELTY - A tea tree is planted by embedding fernwort as green fertilizer into root part of tea tree during autumn; and when the fernwort grows up, collecting each part of fernwort and burning into ash to exert on the root part of the tea tree.    USE - Method of planting a tea tree (claimed).    ADVANTAGE - The method fully utilizes each kind of nutrient content of the fernwort and increases growth of the tea tree with strong immunity and tea leaf quality which is free of pest.
NOVELTY - A frost prevention agent comprises (wt.%) quat. ammonium salt surfactant (5-20, preferably 8-15), Chinese medicinal herb extract liquid (0-50, preferably 10-20), copper salt (1-5, preferably 2-4 calculated as weight of copper element), and water (20-94, preferably 61-80).    USE - Frost prevention agent used for reducing or preventing cold injury or frost damage in crops or fruit trees including banana, loquat, dragon fruit, strawberry, pineapple, pawpaw, emblic leafflower fruit, tomato and tobacco in frigid zone, temperate zone and subtropical zone (claimed).    ADVANTAGE - The frost prevention agent has synergistic effect, provides long-acting effect with no toxic effect, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the frost prevention agent, comprising: (A) preparing quat. ammonium salt surfactant ethanol solution; (B) preparing copper salt solution with cupric ions (Cu2+); (C) preparing Chinese medicinal herb extract liquid by extracting herba portulacae, fluxweed and Scutellaria baicalensis with ethanol and water; and (D) mixing the three solutions with water, and uniformly stirring to obtain the frost prevention agent.
NOVELTY - Method for preparing compound fertilizer, involves (a) evaporating and concentrating extracted waste liquid of fermented glutamic acid at 40-150 degrees C such that the weight content of solid in the concentrated slurry reaches 40-99%, (b) cooling the concentrated slurry such that the temperature reaches 20-120 degrees C, and (c) prilling the material, and cooling and solidifying the material to obtain the compound fertilizer.    USE - The method is useful for preparing compound fertilizer.    ADVANTAGE - The method is environmentally-friendly and enables preparation of fertilizer with high adaptability and high resource utilization rate.
NOVELTY - Agent comprises strain A and material B. The strain A comprises (in parts): Bacillus subtilis (20-80), photosynthetic bacteria (5-15), actinomycte (10), yield increasing fungus (5), fermented bacteria (5), radix sophorae flavescentis (5) and bone meal. The material B comprises brown coal powder (60), white clay (10), livestock feces (20) and humic acid sodium (2-10).    USE - The agent is useful for treating dysplasia of seedling caused by low temperature, rain, bakanae disease, rice blast, bacterial leaf blight, cooper bright and false smut (claimed).    DETAILED DESCRIPTION - Agent comprises strain A and material B. The strain A comprises (in parts): Bacillus subtilis (20-80), photosynthetic bacteria (5-15), actinomycte (10), yield increasing fungus (5), fermented bacteria (5), radix sophorae flavescentis (5) and bone meal. The material B comprises brown coal powder (60), white clay (10), livestock feces (20) and humic acid sodium (2-10). The strain A and material B are mixed uniformly in the ratio of 1-9, granulating the obtained mixture, adding the granulated mixture into parching cylinder at 60 degrees C, cooling the mixture, sieving the cooled mixture, and packaging the sieved mixture in bags.
NOVELTY - Preparing dronedarone key intermediate methyl 4-(3-(dibutylamino)propoxy)benzoate comprises: (i) reacting methyl p-hydroxybenzoate with 3-bromo-propanol in presence of an inorganic alkali as a catalyst to obtain methyl 4-(3-hydroxypropoxy)benzoate; (ii) reacting the hydroxyl moiety on the methyl 4-(3-hydroxypropoxy)benzoate with mesyl chloride to obtain methyl sulfonate group; and (iii) replacing the methyl sulfonate group by di-n-butylamine.    USE - The method is useful for preparing methyl 4-(3-(dibutylamino)propoxy)benzoate.    ADVANTAGE - The method is simple, economical and environmental friendly and easily recycles the solvent.
NOVELTY - Environmental-friendly refrigerant comprises hydrocarbon series propane (R-290) (50-56 kg) and iso-butane (R-600a) (40-49 kg). The refrigerant further added with normal-butane (R-600) (2-5 kg), propylene (R-1270) (1-3 kg) and an additive (hxamethyl silicone oil) (0.5-1 kg) to obtain near-azeotropic mixed refrigerant.    USE - The composition is useful for replacing 1,1,1,2-tetrafluoroethane (HFC-134a).    ADVANTAGE - The composition has ozone layer damage index of 0 and global warming potential value of 3.
NOVELTY - The device has a housing whose top and bottom provided with raw material gas inlet and synthesized gas outlet. The inner cavity of housing is filled with particle catalyst and cooling bushings to realize cooling medium. The bottom of housing is provided with cooling medium inlets connected with inner pipes of cooling bushings and cooling medium outlets connected with outer pipes of cooling bushing. The pressure of fused salt is 02-4 MPa and temperature is 250-400 degrees C.    USE - Reaction device of methane synthesis.    ADVANTAGE - The temperature of device can be controlled during methane reaction process and synthesis efficiency can be improved. The low cost, safe and reliable of device can be achieved by large scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the reaction device. (Drawing includes non-English language text)
NOVELTY - The device has a housing whose top and bottom is provided with the raw material gas inlet and synthesized gas outlet. The inner cavity of housing is provided with particle catalyst and cooling disc pipes to contain cooling medium. The housing is provided with cooling medium inlet and outlet channels connected with the two ends of cooling disc pipes. The ceramic ball layer comprises many adjacent ceramic balls. The pressure of water is 5-20 MPa ad temperature is 263.91 to 365.7 degrees C.    USE - Reaction device of methane synthesis.    ADVANTAGE - The temperature can be controlled effectively during the methane process, sodium that synthesis efficiency of device can be improved. The low cost, safe and reliable of device can be achieved for large scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the reaction device. (Drawing includes non-English language text)
NOVELTY - Preparing butane by molecular sieve absorption method under liquid phase status, using: an integral molecular sieve absorption tower, which is connected with the upper and lower parts of a liquid circulation pump through a connection pipeline, where the middle part is connected with a rotary valve, an upper extraction liquid evaporation tower and a lower extraction liquid evaporation tower through the connection pipeline, is claimed.    USE - The method is useful for preparing butane.    ADVANTAGE - The method: is simple, yields product of high purity, and is environmental friendly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the device used for the production of butane.
NOVELTY - Green preparation method of dehydropregnenolone acetate from pseudo-steroid sapogenin acetate as a raw material, comprises (i) performing one-pot reaction on (II), a vanadium-containing catalyst, a quaternary ammonium compound catalyst and hydrogen peroxide in a molar ratio of 1:0.01-10:0.05-10:2-10 by mechanically stirring at 55-100 degrees C in a reactor for 3-24 hours to prepare a solid-liquid mixture; and (ii) performing post-treatment on the solid-liquid mixture to prepare (I).    USE - The method is useful for the preparation of dehydropregnenolone acetate.    ADVANTAGE - The method is a low cost and environmental-friendly method and produces high yield of (I) and avoids the use of organic solvent. In the method, the catalyst can be completely recycled.    DETAILED DESCRIPTION - Green preparation method of dehydropregnenolone acetate represented in formula (I) from pseudo-steroid sapogenin acetate represented in formula (II) as a raw material, where in both (I) and (II), C-C or C=C is formed between C-5 and C-6 or between C-9 and C-11, when C-C is formed between C-5 and C-6, H connected with the C-5 is alpha-H or beta-H, comprises (i) performing one-pot reaction on (II), a vanadium-containing catalyst, a quaternary ammonium compound catalyst and hydrogen peroxide in a molar ratio of 1:0.01-10:0.05-10:2-10 by mechanically stirring at 55-100 degrees C in a reactor for 3-24 hours to prepare a solid-liquid mixture; and (ii) performing post-treatment on the solid-liquid mixture to prepare (I).
NOVELTY - The deflaker has rotating members (125) for removing foreign substance in biomass fuel by rotating parallely and transmitting to a vibrating screen. A motor (130) rotates one of the rotating members. A power transmission element delivers torque of the former rotating member to the latter rotating member. A paddle part is connected to a pair of side plates of the rotating members, where the paddle part provides impact to the biomass fuel.    USE - Biomass fuel deflaker.    ADVANTAGE - The height of the deflaker can be increased before running the vibrating screen.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass fuel deflaker.    Rotating members (125)    Motor (130)
NOVELTY - The method involves obtaining mixed grains by evenly mixing dry biomass gains and a dry coal powder, and feeding the mixed grains to entrained flow gasification by a phase pneumatic transport, where pressure of the phase pneumatic transport is 0.05-6.0 MPa. The mixed grains and a gasification agent are gasified to generate clean synthesis gas. The biomass is selected from a group consisting of agriculture and forestry waste, preferably comprising straw, sawdust, fire wood, weed, chaff, shell, bagasse and corncob.    USE - Method for preparing clean synthesis gas (claimed).    ADVANTAGE - The method enhances entrained flow gasification gasifying temperature, avoids harmful ingredients such as tar oil and phenol in the obtained synthesis gas, and reduces carbon dioxide emission. The biomass has a low volatile content and high energy density, so as to avoid secondary pollution and realize large-scale, high efficient, clean and economic utilization of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing clean synthesis gas. '(Drawing includes non-English language text)'
NOVELTY - Microbial preparation comprises Zoogloea, Comamonas, Bacillus, Pseudomonas, Alkaligenes and Nocardia.    USE - Microbial preparation used in sewage treatment plant.    ADVANTAGE - The microbial preparation has synergistic effect for sewage treatment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method for preparing microbial preparation, which involves culturing Zoogloea, Comamonas, Bacillus, Pseudomonas, Alkaligenes and Nocardia in a culture medium; and    (2) a method for increasing the effect of microbial preparation, which involves mixing clean water and sewage, adding glucose, peptone, nitrogen-phosphorus-potassium compound fertilizer and microelement, stirring the mixture for 24-48 hours and putting culture solution in a sewage tank.
NOVELTY - A waste oil regeneration containing waste material fuel of wood chips is manufactured by mixing water adhesive and starch with 80 degrees C of waste oil ( plus minus 10) for inflammable waste materials such as waste thread, rice bran, fallen leaves, rubber and pulverized plastic which are set as combination and mixing at wood chips, putting in formwork manufacture, cooling and drying fuel roasted in covered pan.    USE - Manufacture of waste oil regeneration containing waste material fuel.    ADVANTAGE - The method manufactures fuel which exhibits disinfection, insect repellence, decay prevention and deodorizing effect.
NOVELTY - The present invention provides a mixing method for a sewage treatment pond and its apparatus mainly introducing the sewage to be purify treated and treated into a sewage treatment pond and accumulating the sewage to reach a level height; then disposing a water supply component on the sewage water level near the location of an operation hole of the sewage treatment pond, the water supply component having an external pressurized water source introducing section, an extension pipe and a water feeding inlet; introducing water having pressure into the sewage treatment pond by means of the external pressurized water source introducing section; then guiding the water having pressure to the water feeding inlet through the extension pipe and spraying water flow toward the sewage through the water feeding inlet to agitate the sewage to achieve the objects and advantages of adequately and uniformly mixing the sewage with microorganisms and enhancing the sewage decomposition performance. Furthermore the design of disposing the aforementioned water supply component on sewage water level and near the location of the operation hole has the advantages of repairing and conveniently replacing the water supply component.
NOVELTY - The power supply device (100) has a fuel cell (102) having a hydrogen inlet and a hydrogen outlet. A hydrogen generator (104) is connected to the hydrogen inlet and used for generating hydrogen to enter the fuel cell. A check valve (106) is arranged in the hydrogen inlet for avoiding the hydrogen within the fuel cell from exhausted from the hydrogen inlet. An exhaust valve is arranged in the hydrogen outlet for exhausting the hydrogen within the fuel cell. The exhaust valve is another check valve used for preventing exterior air from entering the fuel cell.    USE - Power supply device for electronic device such as computer, flash light or other electronic devices.    ADVANTAGE - The power supply device has two valves that are respectively arranged the hydrogen inlet and the hydrogen outlet of the fuel cell for controlling the interior pressure of the fuel cell, hence the power generation efficiency of the fuel cell is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram of the power supply device.    Power supply device (100)    Fuel cell (102)    Hydrogen generator (104)    Check valve (106)    Image generator component (108)
NOVELTY - The system has an engine e.g. hydrogen combustion engine (10) that generates power. A water-to-hydrogen generator (16) generates and supplies fuel to the engine at a rate that is equal to a rate required by the engine to run so that no excess fuel is generated, and connected to engine. A vibration electrical generator (20) captures vibration energy from the engine, converts the vibration energy into electricity, and transmits the electricity to power the water-to-hydrogen generator.    USE - Power generating system of vehicle such as car (from drawings).    ADVANTAGE - The system provides an engine having an electrolysis system that is powered in simplest form. Multiple piezoelectric generators generates a minimum amount of hydrogen necessary to fuel the engine as required by the engine to operate so that only the minimal amount of hydrogen exists at any time regardless of operating status of the engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of generating power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view with flowchart of power generating system having piezoelectric vibration.    Hydrogen combustion engine (10)    Alternator (12)    Water-to-hydrogen generator (16)    Battery (19)    Vibration electrical generator (20)
NOVELTY - The steam reformer (102) has an exterior shell (108) which includes a diffusion burner and angled fins. The angled fins extend away from an inner surface of the exterior shell and downward toward the diffusion burner. An interior reactor (106) is positioned within the exterior shell. The exterior shell includes two angled fins which are ring shaped. An angle between an upper of the two angled fins and the exterior shell is less than an angle between a lower of the two angled fins and the exterior shell.    USE - Methane steam reformer for generating hydrogen for use in fuel cell.    ADVANTAGE - The steam reformer has diffusion burner and angled fins so as to increase radiative heat transfer from the flame within the external shell to the interior reactor. By controlling the amount of heat transferred to the interior reactor, a reforming reaction which occurs within the interior reactor can be driven toward the formation of products. The increased heating of the interior reactor is facilitated to drive a reforming reaction in the interior reactor toward the formation of more products. The external shell includes angled fins that are used to increase an amount of heat transferred to an interior reactor which it surrounds without extending the length of the reformer compared to an external shell that does not have angled fins.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for steam reformer; and    (2) system for steam reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the steam reforming system coupled to fuel cell stack.    System for steam reformer (100)    Reformer (102)    Fuel cell stack (104)    Interior reactor (106)    Exterior shell (108)
NOVELTY - Hydrogen generation system comprises: a solid hydrogen fuel (11); an absorbent material (13), which absorbs liquid in the system; and a phase-change material (15), disposed adjacent to a position at which a hydrogen releasing reaction occurs, where the phase-change material absorbs and stores the reaction heat generated from the hydrogen releasing reaction, reacted by the solid hydrogen fuel and the liquid, and maintains a reaction temperature, thus controlling hydrogen releasing rate of the hydrogen releasing reaction and stabilizing hydrogen flow.    USE - Used as hydrogen generation system.    ADVANTAGE - The hydrogen generation system: is small and easy to be carried out compared to the conventional systems; and utilizes phase-change material for providing hydrogen to a fuel cell at a stabilized hydrogen-releasing rate for long time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) generating hydrogen using solid hydrogen fuel comprising (a) providing the solid hydrogen fuel, (b) providing the absorbent material mixed with the solid hydrogen fuel in a fuel pack, (c) providing a liquid pack (31) comprising a liquid of water, alcohols and its aqueous solutions, aqueous solutions of salts and/or aqueous solutions of acids, (d) providing the phase-change material disposed adjacent to the solid hydrogen fuel, and (e) conducting water or aqueous solution of the liquid pack into the fuel pack to perform hydrogen releasing reaction; and    (2) applying solid hydrogen fuel to fuel cell comprising steps (a)-(e) as above per se, and (f) providing a fuel cell applied with the hydrogen released from the solid hydrogen fuel.    DESCRIPTION OF DRAWING(S) - The figure illustrates the hydrogen production system with the solid hydrogen fuel.    Solid hydrogen fuel (11)    Absorbent material (13)    Phase-change material (15)    Liquid package (31)    Hydrogen releasing apparatus (43)
NOVELTY - The generator (212) has gas impermeable wall (222) that divides a vessel (220) into hydrogen and oxygen generating chamber. A polymer electrolyte membrane (PEM) is installed in opening such that fluid communication through opening passes by PEM. A nickel alloy material is arranged in hydrogen generating chamber. A hydrogen gas collection area having a port through which hydrogen is delivered to exterior of vessel. The anode (237) and cathode are connected to electric source. The electric circuit is formed by source, anode, cathode, and electrolyte solution (206).    USE - Hydrogen gas generator for powering vehicle.    ADVANTAGE - The hydrogen generation system is safe, economical, and independent from commercial hydrogen filling stations. The gas generation and management system provides a steady flow of compressed gas to a gas sink. The gas generation and management system also provides compressed gas during start-up operations, and renders the gas generation and management system much safer than existing compressed gas systems by minimizing the amount of compressed gas present in the gas generation and management when the system is not operational. The cost of components is minimized in a simple and effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for generating hydrogen gas in vessel.    DESCRIPTION OF DRAWING(S) - The drawing shows a side cross sectional view of the hydrogen generating PEM electrolyzer of gas generator system.    Electrolyte solution (206)    Hydrogen gas generator (212)    Vessel (220)    Interior gas impermeable wall (222)    Anode (237)
NOVELTY - The method involves continuously or intermittently feeding and moving a sheet of porous substrate toward a desired direction. A layer of a solid mixture of conductive filler, a thermoset binder and a thermoplastic matrix material is left on the substrate, when a carrier fluid is directed to flow through the pores. The substrate is moved to allow solid mixture layer to go through a compaction stage. The solid mixture layer is heated and consolidated. The flow channels are generated on a surface of the solid mixture layer to form a flow field or bipolar plate.    USE - Method for producing fuel cell flow field plate or bipolar plate.    ADVANTAGE - The fuel cell system has reduced cost because of their amenability to mass production, and the performance is increased because of the reduced contact resistance and internal resistance and increased voltage. The method for producing fuel cell flow field plate is continuous and automated, so that the cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the Schematic view of a slurry molding for producing preform to flow field plate.    Mold (37)    Molding pin (39x, 39z)
NOVELTY - Apparatus for twin-tub methane-fermentation comprises: (a) methane fermentation tank; (b) oxidation-reduction potential measurement part which measures the oxidation-reduction potential in acid production tank; (c) pH-measurement part which measures pH in an acid production tank; and (d) acid production tank evaluation part which evaluates reaction state in acid production tank based on the pH-measurement value inputted from measured value inputted from oxidation-reduction potential measurement part and pH-measurement part.    USE - The apparatus is useful for twin-tub methane-fermentation (claimed).    ADVANTAGE - The method provides easily optimized methane fermentation treatment having high speed and stable steps.    DETAILED DESCRIPTION - Apparatus for twin-tub methane-fermentation comprises: (a) methane fermentation tank to which methane fermentation of the acid produced by the acid production tank and the acid production tank which produce acid from organic substance is carried out; (b) oxidation-reduction potential measurement part which measures the oxidation-reduction potential in acid production tank; (c) pH-measurement part which measures pH in an acid production tank; and (d) acid production tank evaluation part which evaluates reaction state in acid production tank based on the pH-measurement value inputted from measured value inputted from oxidation-reduction potential measurement part and pH-measurement part. An INDEPENDENT CLAIM is a twin-tub methane-fermentation method comprising performing methane fermentation process to which the methane fermentation of the acid produced in the acid production process and the acid production process which acid is produced from organic substance is carried out in separate reaction tank, where reaction state of acid production process is evaluated based on measured value and pH-measurement value.
NOVELTY - A hydrogen production apparatus comprises modification-catalyst layer (50) which has catalyst function which modifies source gas and produces hydrogen, hydrogen separation layer (30) selectively permeates and separates hydrogen, reaction barrier layer (40) which prevents reaction of catalyst of modification-catalyst layer and hydrogen separation material of hydrogen separation layer, and surface protective layer (20) which protects surface of hydrogen separation layer.    USE - A hydrogen production apparatus.    ADVANTAGE - The apparatus has high durability and small size.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of hydrogen separation tube. (Drawing includes non-English language text).    Hydrogen separation tube (3)    Surface protective layer (20)    Hydrogen separation layer (30)    Reaction barrier layer (40)    Modification-catalyst layer (50)
NOVELTY - A self-supporting low hydrocarbon direct dissociation processing system has a reaction tube (1) for carrying out decomposition reaction of low hydrocarbon in presence of catalyst to produce hydrogen and carbon, heating unit (13) for heating the reaction tube, a supply path (11) for supplying water generated from reaction tube to heating unit, and a flow volume regulator (12) provided in supply path.    USE - Self-supporting low hydrocarbon direct dissociation processing system is used for producing hydrogen used as fuel.    ADVANTAGE - The self-supporting low hydrocarbon direct dissociation processing system enables direct dissociation of low hydrocarbon without generating carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the conceptual diagram of self-supporting low hydrocarbon direct dissociation processing system. (Drawing includes non-English language text)    Reaction tube (1)    Compressor (6)    Supply path (11)    Flow volume regulator (12)    Heating unit (13)
NOVELTY - Manufacturing catalyst of low hydrocarbon and an aromatic compound, comprises contacting methane to a metallosilicate which carry the catalyst metal, and a hydrogen storage substance, and low hydrocarbon and an aromatic compound are manufactured.    USE - The method is useful for manufacturing catalyst of low hydrocarbon and an aromatic compound (claimed).    ADVANTAGE - The method efficiently and effectively manufactures catalyst of low hydrocarbon and an aromatic compound.
NOVELTY - A glycerol refiner comprises glycerol evaporation part which melts alkali compound while vaporizing glycerol, separation part which separates the vaporized glycerol and the melted alkali compound, and solidification part which solidifies the melted alkali compound. Glycerol containing liquid consists of glycerol and alkali compound is heated so that the boiling point of glycerol may become higher than the melting point of the alkali compound.    USE - A glycerol refiner for glycerol obtained from biodiesel manufacture (claimed).    ADVANTAGE - Adding other chemicals are not unnecessary, apparatus is simple, and process is low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) glycerol modifier comprising glycerol refiner and reforming reactor which accommodates a catalyst and modifies the glycerol;    (2) glycerol purification method which involves heating glycerol containing liquid, consists of glycerol and alkali compound, so that the boiling point of glycerol may become higher than the melting point of alkali compound, vaporizing glycerol while melting alkali compound, and separating vaporized glycerol; and    (3) glycerol modification method which involves reacting refined glycerol and reactive gas which contains water vapor in the presence of a catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schemtic block diagram of the glycerol refiner. (Drawing includes non-English language text).    Glycerol refiner (1)    Glycerol evaporator (2)    Gas-liquid separator (3)    Collection tank (4)    Pressure control valve (5)
NOVELTY - The vessel has an electrode supporting element (6) which is provided with an elastic mat to wound a metal coil on a corrosion resistant frame. The electrode supporting element and a flexible electrode (5) e.g. hydrogen producing cathode are fixed to a current collection board. A pin (8) is penetrated through the flexible electrode and the current collection board. The pin is not penetrated through the elastic mat accommodated between the flexible electrode and the current collection board.    USE - Electrolytic vessel for processing ion-exchange membrane.    ADVANTAGE - The electrode supporting element is provided with elastic mat to wound metal coil on corrosion resistant frame, so that the damage of ion-exchange membrane can be avoided. Hence, the stable operation of electrolytic vessel can be obtained for long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the electrolytic vessel in cathode attachment state.    Flexible cathode (5)    Electrode supporting element (6)    Pin (8)
NOVELTY - The apparatus has an anode and cathode are provided in both surfaces of fluorine resin cation exchange membrane (9) such as perfluoro sulfonic-acid cation exchange membrane. A conductive diamond electrode is provided with an electroconductive diamond film (10) which is covered by the surface of P-type silicon substrate (11). The fluorine resin cation exchange membrane without a cut is fixed to electrolysis cell. A filled layer (19) that is closely filled with ion exchange resin grain is contacted on the anode side surface of fluorine resin cation exchange membrane.    USE - Ozone development apparatus for use in water-and-sewer-services facility.    ADVANTAGE - The exhaustion of fluorine resin cation exchange membrane can be suppressed. The ozone can be generated stably for long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis cell.    Fluorine resin cation exchange membrane (9)    Electroconductive diamond film (10)    P-type silicon substrate (11)    Sealing material (15)    Filled layer (19)
NOVELTY - An ion-permeable separation membrane has organic nonwoven fabric, in which mixture of hydrophilic inorganic material and organic binding material is made inherent.    USE - Ion-permeable separation membrane is used for alkaline water electrolysis.    ADVANTAGE - The ion-permeable separation membrane has reduced wrinkles, twists and excellent pressure resistance and smoothness, and reduces the expansion-contraction of fiber at the time of solvent extraction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of ion-permeable separation membrane.
NOVELTY - Integrated sewage processing device comprises a tank body, a water inlet distribution device, an aeration device, a gas-water separator, a solid-liquid separation device and a water outlet collection device, where all are integrally assembled in a tank. The tank is divided into five functional zones of an anaerobic biological zone, a facultative anaerobic biological zone, an aerobic biological zone, a gas-water separation zone and a solid-liquid separation zone.    USE - Used as an integrated sewage processing device.
NOVELTY - The system has hydrogen producing apparatus that produces hydrogen (22) using hydrogen producing material by exothermic reaction with water. The fuel cell (1) is provided for producing electric power by using the hydrogen as fuel. The pulse electricity supply is performed with respect to fuel cell while stopping electric power generation. The pulse heating switches (10a,10b) is provided for heating the fuel cell so that predetermined temperature of fuel cell is maintained while stopping electric power generation.    USE - Fuel cell system for personal computer and mobile phone.    ADVANTAGE - Since the pulse heating switches are provided for heating the fuel cell so that predetermined temperature of fuel cell is maintained while stopping electric power generation, the reliability of fuel cell system can be improved with stable operation even in sub-zero temperature low-temperature environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Voltage detector (6)    Pulse heating switches (10a,10b)    Oxygen (21)    Hydrogen (22)
NOVELTY - Method for preparing microorganism carrier, involves adding carrier containing microorganism to suspension liquid, in which the microbial population contains anaerobic decomposer microbe and acetic acid utilizing methane bacteria, adding lignocellulosic biomass to the suspension liquid and decomposing the lignocellulosic biomass using the microbial population.    USE - The method is useful for preparing microorganism carrier which is used for generating methane gas from lignocellulosic biomass (claimed).    ADVANTAGE - The method consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for generating methane gas from the lignocellulosic biomass, which involves performing methane fermentation of hydrophobic carrier and lignocellulosic biomass in methane fermentation liquid using the microorganism carrier obtained by the above-mentioned method and acetic acid utilizing methane bacteria.
NOVELTY - Hydrogen which can be added to an anaerobic digester to cause microbes to combine the hydrogen with dissolved carbon dioxide or carbonates, to make methane and other organic compounds and converting the carbon in it into hydrocarbon fuels, biofuels and chemical feedstock for industrial processes without the need for a feedstock of biological origin.    USE - The hydrogen is useful for producing methane and other organic compounds and converting carbon into hydrocarbon fuels, biofuels and chemical feedstock for industrial processes (claimed).    ADVANTAGE - The hydrogen efficiently and effectively produces methane and other organic compounds.
NOVELTY - A mixture of raw material containing carbon compound and catalyst is reacted in a pyrolysis furnace (5) heated to 700-900 degrees C and substituted with superheated steam in order to regenerate the carbon compound.    USE - Regeneration treatment of carbon compound from raw material containing carbon compound e.g. foodstuff residue, agricultural residue, woody biomass, activated sludge and waste plastic, to produce liquid fuel or electrical energy.    ADVANTAGE - The carbon compound is regenerated economically at low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gasifier used for producing gas containing hydrogen and carbon monoxide from raw material containing carbon compound, which consists of catalyst mixer (2), supply port for supplying raw material, discharge port for discharging the gas, pyrolysis furnace, superheated steam supply unit (10) and heater; and    (2) regeneration processing system, which consists of generator (13) connected to liquid fuel synthesizing apparatus, excessive gas supply apparatus which supplies excessive gas produced from the liquid fuel synthesizing apparatus (12), as fuel for electric power generation in the generator.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the regeneration processing method.    Catalyst mixer (2)    Pyrolysis furnace (5)    Superheated steam supply unit (10)    Liquid fuel synthesizing apparatus (12)    Generator (13)
NOVELTY - The present invention discloses an environmentally protective nano bactericidal mildew proofing agent, including a fungicide, a mildew proofing agent, an insect repellent agent, a waterproofing agent, an emulsifying agent, a color developing agent, a diluent, a plasticizer and an organic solvent, the percentages by weight of which respectively range from 1 to 5%, from 10 to 20%, from 5 to 10%, from 15 to 20%, from 1 to 3%, from 0 to 0.3%, from 25 to 35%, from 0.1 to 0.5% and from 25 to 35%.
NOVELTY - The box has cage, box case, feeding port, a discharging port, gas-guide tube and gas-storage box. The size and shape of the cage are as same as the size and shape of the box case. The box case is accommodated in the cage. The box case is provided with the feeding port, the discharging port and a gas-collecting hole used for sending methane through the gas guide tube. A triangular valve is provided between gas-guide hole and terminal of gas-guide tube. The cage is placed on ground or hung overhead.    USE - Methane box.    ADVANTAGE - The methane box is simple in structure so that cost of building the methane tank is reduced. The gas feeding and gas discharging performance of methane box can be improved. Fermenting and methane generating ratio of raw materials are promoted. A filtering net and a counterweight block are arranged in the box, so that the raw materials, gas and liquid methane are separated efficiently and the hardening of the raw materials can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane box.
NOVELTY - Isomerizing a saturated, branched and cyclic hydrocarbon, in which a tertiary carbon atom of the hydrocarbon is converted to a secondary carbon atom in the course of isomerization, comprises performing the isomerization in the presence of a superacidic ionic liquid comprising an organic cation and an inorganic anion, where the anion is a superacidic aluminum trichloride-Lewis base adduct, and a copper(II) compound.    USE - The process is useful for isomerizing a saturated, branched and cyclic hydrocarbon.    ADVANTAGE - The process is simple and economical. The process provides high yield, preferably in high space-time yields and selectivities.
NOVELTY - Two-phase anaerobic treatment method for processing organic wastewater, involves performing souring process and methane fermentation process one by one, and controlling pH value using alkali chemicals. When the alkali chemicals are added, the souring process becomes below settling value of the alkali chemicals addition ratio, which is calculated from the addition of organic substance to the souring process. When the souring process becomes below the settling value of the alkali chemicals the addition of wastewater to the souring process is reduced or stopped.    USE - The method and apparatus are useful for processing organic wastewater (claimed) generated from factories e.g. food industry and chemical plant.    ADVANTAGE - The method is rapid and simple, and has excellent stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows flow block diagram of anaerobic treatment method.    Raw water conveying pump (1)    Souring tank (2)    Alkali chemicals (6)    Alkali chemicals addition tank (7)    Methane fermentation tank (9)
NOVELTY - Method of fermenting hydrogen and methane, involves subjecting biomass feedstock to hydrogen fermentation process to produce hydrogen gas, producing methane gas by performing methane fermentation of slurry after the hydrogen fermentation, digesting slurry after the methane fermentation process, subjecting the digested slurry to denitrifying process, and separating sludge from the denitrified slurry.    USE - The method is useful for fermenting hydrogen and methane which is used in chemical and airline industries.    ADVANTAGE - The method is inexpensive and environmentally-friendly. The hydrogen and methane gas is obtained without using alkali chemicals and enables removal of nutritive salts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen and methane fermentation system, which comprises hydrogen fermenter tank for subjecting biomass feedstock to hydrogen fermentation process to produce hydrogen gas, methane fermentation tank for producing methane gas by performing methane fermentation of slurry after the hydrogen fermentation, and digested sludge storage tank for digesting slurry after the methane fermentation process.
NOVELTY - The treatment technique involves pretreating sludge containing oil; tempering sludge containing oil; carrying out three-phase centrifugal separation for the sludge containing oil; carrying out composite firing for the left sludge containing oil and biomass; and carrying out high temperature burning treatment in the rotary kiln after mixing the left sludge containing oil, separated solid impurities and scum and biomass.    USE - Reclamation and harmless comprehensive treatment technique for sludge containing oil.    ADVANTAGE - Treatment technique eliminates secondary pollution of sludge containing oil and recycles waste heat for high temperature smoke.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow diagram of the reclamation and harmless comprehensive treatment technique for sludge containing oil. (Drawing includes non-English language text).
NOVELTY - Vermicompost matter (humus) preparation involves using municipal solid waste and organic or recyclable materials without placing them to landfill, incineration or other area. The humus is prepared by opening and drying raw material bags. The material containing plastic package is sifted, sorted and cleaned. Worm compost (humus) is mixed at end of the process with other materials to produce long life cycle. The method includes degradation of the soil without depositing non-biodegradable materials.    USE - Method for preparing vermicompost matter (humus) used in recovery of crop plant.    ADVANTAGE - The vermicompost matter (humus) preparing method enables to produce product that is beneficial to soil and promotes development of plant ecology.
NOVELTY - The process involves reacting coal (10) with an oxygen-containing gas in a first-stage gasifier (1) to produce a gas product containing carbon dioxide, water, and hydrogen and carbon monoxide (8) from the gasification of coal. A cooling agent is introduced into the gas product to decrease a temperature. A first-stage gas product (2) is obtained and introduced into a second-stage gasifier (3). The first-stage gas product is reacted with coal and a catalyst to obtain a second-stage gas product (4) containing methane (6).    USE - Process for producing methane by gasification of coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for producing methane by gasification of coal.'(Drawing includes non-English language text)'    First-stage gasifier (1)    First-stage gas product (2)    Second-stage gasifier (3)    Second-stage gas product (4)    Methane (6)    Hydrogen and carbon monoxide (8)    Coal (10)
NOVELTY - The apparatus (41) has solid-liquid separation section (51) which is formed on upper portion of overall aeration section (49) and arranged with membrane separation device (55). A flow path narrow section (50) is formed between aeration section and separation section. The flow path narrow section allows flow path narrow device (59) to narrow cross-sectional area of flow path from aeration section to separation section to bind fine air bubbles (53) discharged from aeration device (52) to discharge bound bubbles to lower portion of membrane separation device.    USE - Organic waste water processing apparatus for biologically treating organic waste water such as sewage.    ADVANTAGE - The energy required for aeration is reduced and cleaning effect of membrane separator is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste water processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the organic waste water processing apparatus. (Drawing includes non-English language text)    Organic waste water processing apparatus (41)    Overall aeration section (49)    Flow path narrow section (50)    Solid-liquid separation section (51)    Aeration device (52)    Air bubble (53)    Membrane separation device (55)    Flow path narrow device (59)
NOVELTY - A hydrogen gas-manufacturing apparatus (10) has a moisture-containing carbon liquid mixture-manufacturing device (1) which mixes moisture-containing liquid and powder-form carbon, and a hydrogen gas-manufacturing device (2) which heats, vaporizes and reacts moisture-containing carbon liquid mixture.    USE - Apparatus is used for manufacturing hydrogen gas (claimed). Uses include but are not limited to fuel cell, gas engine, gas turbine, boiler, coke oven, rotary kiln, Stirling engine and heating furnace for chip fabrication factory and coal gasification factory, hydrogen station and research laboratory.    ADVANTAGE - The apparatus enables economical manufacture of hydrogen gas, with reduced energy consumption and without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the apparatus for manufacturing hydrogen gas. (Drawing includes non-English language text)    Moisture-containing carbon liquid mixture-manufacturing device (1)    Hydrogen gas-manufacturing device (2)    Hydrogen gas-manufacturing apparatus (10)
NOVELTY - The technique involves selecting an address of duck shed and building the shed. A biological padding is manufactured. The padding is used and maintained in a young duck as the duck is sensitive to mycete. The padding is piled up and fermented. The padding is repeatedly used for more than 10 times. Color of the padding is made dark about 1.5 to 2 days later. A degrading action is made difficult to be sifted out and renewed, where waste padding is not verminous and does not burn the seedling to have long fertilizer efficiency to be excellent organic fertilizer.    USE - Biological fermenting bed breeding technique for meat duck.    ADVANTAGE - The technique eliminates pollution, emission and sewage production and saves labor. The beneficial flora of the padding builds a strong fine environment. The padding adsorbs, neutralizes, degrades and inverts the organic matter in the excrement.
NOVELTY - A modifier (1) comprises first cylinder (2), second cylinder (3) which covers outer periphery of first cylinder, first honey-comb body (4) in which catalyst which is provided internally by first cylinder can modify source gas is supported, second honey comb (5) which is arranged between first and second cylinders, inlet port which can supply source gas to first honey comb body, turning structure which turns source gas emitted from first honey comb body, exit which emits reformed gas, and pair of electrode which is connected to first honey comb body.    USE - A modifier.    ADVANTAGE - The modifier is efficient.    DETAILED DESCRIPTION - A modifier (1) comprises first cylinder (2), second cylinder (3) which covers outer periphery of first cylinder, first honey-comb body (4) in which catalyst which is provided internally by first cylinder can modify source gas is supported, second honey comb (5) which is arranged between first and second cylinder and supports catalyst, inlet port which is formed in first cylinder and can supply source gas to first honey comb body, turning structure which turns source gas emitted from first honey comb body and supplies reformed gas to second honey comb body, exit which emits reformed gas, and pair of electrode which is connected to first honey comb body and can supply electric current to first honey comb body.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the modifier.    Modifier (1)    First cylinder (2)    Second cylinder (3)    First honey-comb body (4)    Second honey comb (5)
NOVELTY - A thermoelectric hydrogen supply system comprises cogeneration system (38) which uses natural gas which vaporized liquefied natural gas (LNG) as fuel, hydrogen separation type steam reforming device (45) which steam reforms natural gas in which off gas from waste gas from cogeneration system and hydrogen separation type steam reforming device is made to merge, and carbon dioxide recovery apparatus containing compressor which uses oxygen enriched air, heat-of-cooling exchanger which uses LNG and gas liquid separation tank (49).    USE - Thermoelectric hydrogen supply system used in industrial plant.    ADVANTAGE - The system is efficient, recovers carbon dioxide, and efficiently improves liquefied natural gas vaporization process and carbon dioxide compression liquefaction recovery process.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the thermoelectric hydrogen supply system. (Drawing includes non-English language text).    Liquid natural gas tank (31)    Cogeneration system (38)    Hydrogen separation type steam reforming device (45)    Combustor (46)    Gas liquid separation tank (49)
NOVELTY - A circulating fluidized bed gasification reactor comprises fluidized bed gasifier where raw material is gasified and flow medium is introduced, and fluidized bed combustion furnace with multistage cyclone where char and flow medium produced during gasification is transferred and unburnt matter is burned. The reheated flow medium ciculates inside the reactor.    USE - Circulating fluidized bed gasification reactor for processing tar, biomass, garbage, sewage sludge, coal, hybrid gasification with biomass, or hybrid gasification with a solid or liquid fuel.    ADVANTAGE - Light tar can be efficiently removed in the system using simple method, and tar processing cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the multistage cyclone in the circulating fluidized bed gasification reactor. (Drawing includes non-English language text).
NOVELTY - A device for preparing biological agent for degrading industrial mixing sewage, comprises a culture medium pre-treating unit, a separating and sieving unit, a micro-organism thallus pre-treating unit, and a thallus freeze drying unit.    USE - The device is useful for preparing biological agent for degrading industrial mixing sewage (claimed).    ADVANTAGE - The device can prepare degraded microorganism and the thallus is frozen and dried to obtain the microorganism powder preparation to prolong the storage period of the thallus and conveniently carry the thallus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for preparing biological agent for degrading industrial mixing sewage.    Culture medium liquid storing pot (101)    Agar powder storing pot (102)    Sewage treating aerobic or anaerobic device (200)    Fermenting pot (302)    Sterilized freeze drying bottle storing device (402)
NOVELTY - Producing ethanol from syngas, comprises: (a) providing syngas having an input hydrogen (H2)/carbon monoxide (CO) ratio; (b)converting a portion of the syngas to dimethyl ether; (c) carbonylating at least some of the dimethyl ether to methyl acetate; (d) hydrogenating the methyl acetate to methanol and ethanol; (e) converting the methanol from step (d) to hydrogen and carbon monoxide; (f) feeding the carbon monoxide generated in step (e) back to step (c); (g) feeding the hydrogen generated in step (e) back to step (d); and (h) recovering the ethanol.    USE - The process is useful for producing ethanol from syngas.    ADVANTAGE - The process provides high yield. The process is economical by capital-cost reduction, reduced process complexity, operating flexibility and co-product potential, and is environmentally friendly.    DETAILED DESCRIPTION - Producing ethanol from syngas, comprises: either (a) providing syngas having an input H2/CO ratio, (b)converting a portion of the syngas to dimethyl ether, (c) carbonylating at least some of the dimethyl ether to methyl acetate, (d) hydrogenating the methyl acetate to methanol and ethanol, (e) converting the methanol from step (d) to hydrogen and carbon monoxide; (f) feeding the carbon monoxide generated in step (e) back to step (c), (g) feeding the hydrogen generated in step (e) back to step (d), and (h) recovering the ethanol; or (i) the step (a) as above per se, (ii) providing a recycle stream comprising syngas components and methanol, (iii) converting a portion of the recycle stream to dimethyl ether, (iv) the step (c) as above per se, (v) introducing the fresh syngas and the methyl acetate to a unit for hydrogenating the methyl acetate to methanol and ethanol, (vi) separating the ethanol from the recycle stream, and (vii) the step (h) as above per se.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a process for selectively converting syngas into ethanol.
NOVELTY - Baicalin preparation involves taking high-quality Scutellaria baicalensis as raw material, and pulverizing and sieving through 10-40-mesh sieve. The material is added to boiling water during stirring to extract liquid, where liquid is filtered and concentrated to obtain paste, which is precipitated with alcohol. 3-5 parts of low-carbon alcohol is added into the concentrated paste at 40-70 degrees C, where the filtrate is decompressed to obtain cake. The obtained cake is washed with water to obtain baicalin.    USE - Method for preparing baicalin (claimed).    ADVANTAGE - The method enables to prepare baicalin with high yield in a simple, safe, eco-friendly and cost-effective manner.
NOVELTY - Pesticide effervescent tablets are prepared by crushing carrier including bentonite, diatomite, silica, corn starch, and/or clay, mixing carrier with pesticide drug and freezing to below - 10 degrees C to obtain nano carrier pesticide; pre-mixing nano carrier pesticide with acid source, carbon dioxide source, binder, wetting-dispersing agent, disintegrating agent and lubricant, crushing and then mixing, and filtering through more than 300 mesh standard sieve to obtain dried powder; and preparing set size of tablets from the dried powder using a tablet press at 15-25 degrees C and at humidity of below 40%.    USE - Method of preparing pesticide effervescent tablets (claimed).    ADVANTAGE - The method is simple and environmentally-friendly, and has low cost and better pesticide utilization rate than those of common emulsion in water.    DETAILED DESCRIPTION - Preparation of pesticide effervescent tablets comprises:    (A) crushing bentonite, diatomite, silica, corn starch, clay, kaolin, gum arabic and/or magnesium aluminum silicate as carrier, mixing carrier with pesticide drug and freezing to below - 10 degrees C to obtain nano carrier pesticide having size of 100-1000 nm, where weight ratio of carrier and pesticide drug is 0.03-10:1;    (B) pre-mixing nano carrier pesticide with acid source, carbon dioxide source, binder, wetting-dispersing agent, disintegrating agent and lubricant, crushing and then mixing, and filtering through more than 300 mesh standard sieve to obtain dried powder; and    (C) preparing set size of tablets from the dried powder using a tablet press at 15-25 degrees C and at humidity of below 40%.
NOVELTY - Oxyfluorfen emulsion in water comprises (wt.%) oxyfluorfen (2-50), solvent (5-50), emulsifying agent (1-20), antifreezing agent (2-10), thickening agent (0.1-2), defoaming agent (0.1-0.8), and water (balance).    USE - Oxyfluorfen emulsion in water.    ADVANTAGE - The oxyfluorfen emulsion in water is an environment-friendly water base agent of oxyfluorfen, has low toxicity, can be easily diluted, is convenient to use, and does not burn nor explode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of oxyfluorfen emulsion in water, comprising:    (A) uniformly mixing oxyfluorfen, solvent and emulsifying agent to prepare oil phase;    (B) uniformly mixing antifreezing agent, thickening agent, defoaming agent and water to prepare water phase;    (C) slowly dropping the oil phase to the water phase or slowly dropping the water phase to the oil phase with high-speed mixing;    (D) mixing for 30 minutes after finishing dropping; and    (E) cutting in high-speed cutting machine for 40-60 minutes to obtain the oxyfluorfen emulsion in water.
NOVELTY - A silver-elemental germifuga comprises halloysite nanotube modified by silane coupling agent as carrier (1 g); and elemental silver (0.1-0.2 g) loaded on carrier.    USE - Halloysite nanotube-loaded silver-elemental germifuga.    ADVANTAGE - The germifuga has easily-obtained raw material, low cost, simple operation, loose condition, and little energy consumption; is environment-friendly, has wide product application range, and strong antibiotic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the germifuga which comprises adding halloysite nanotube in reaction medium, where moisture content is removed from halloysite nanotube; adding 1-2 times silane coupling agent, dispersing agent and modifying nanotube at 115-125 degrees C; stirring mixture, refluxing mixture for 24-30 hours, washing and drying product to obtain halloysite nanotube modified by silane coupling agent; and obtaining modified carrier, loading silver ion, and restoring silver ion to obtain halloysite nanotube which loads silver. The reaction medium is benzene, methylbenzene, N,-dimethylformamide or N,N-dimethylethanamide.
NOVELTY - High-activity high-formaldehyde-resistance degrading bacteria comprises Pseudomonas putida xyz-zjut (CCTCC No: M2010125) preserved at 23'rd, May 2010.    USE - The degrading bacteria is useful for the formaldehyde degradation by the microorganism.    ADVANTAGE - The degrading bacteria has high-activity and high-formaldehyde-resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the Pseudomonas putida xyz-zjut in the formaldehyde degradation by the microorganism.
NOVELTY - The device has reproducible filters that are arranged between a copper liquid reducing valve on the bottom of copper wash tank and a buffer tank on the top of reflex column. Copper liquid inlet valve whose inlet is connected with the outlet pipeline of the reducing valve. The outlet of the copper inlet valve is connected with an outlet of the buffer tank. The inlet of the reproducible filter subline valve is connected with the outlet of the reducing valve. The outlet of the reproducible filter subline valve is connected with the inlet of the buffer tank.    USE - Refining regeneration device for synthesis ammonia production.    ADVANTAGE - The copper wash tower can be cleaned without pollution and the cleaning of the device and the pipes can be avoided, so that the production efficiency of the device can be improved and the environmental pollution can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the refining regeneration device. (Drawing includes non-English language text)
NOVELTY - Environment-friendly anti-blocking agent comprises (in wt.%): a sulfated vegetable oil (90) and a low-carbon alcohol (10).    USE - The anti-blocking agent is useful for high-tower granulation urea-base composite fertilizer.    ADVANTAGE - The anti-blocking agent: has excellent in anti-blocking effect, is pure and natural, is environment-friendly, saves resource, reduces the agricultural production cost and increases the income of the peasants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the environment-friendly anti-blocking agent, comprising: adding the sulfated vegetable oil (70-90 wt.%) into a vacuum drying pot, heating and vacuum drying until the water content is lower than 0.5%; adding the dried sulfated vegetable oil into a decoloring pot, stirring and adding into active carbon (0.5-1% of the weight of the sulfated vegetable oil), reacting for 2-3 hours at 800-900 degrees C, adding the de-colored sulfated vegetable oil into a stirring tank, stirring and adding into 6-10C low-carbon alcohol (10-30 wt.%), stirring uniformly to obtain the anti-blocking agent, and packaging.
NOVELTY - Treating mother solution of glyphosate comprises (i) adding calcium hydroxide aqueous solution to regulate acidic mother solution of glyphosate into alkaline mother solution and producing triethylamine from the triethylamine hydrochloride in the mother solution, (ii) distilling by a distillation tower, collecting the distillate from the tower top, (iii) adding dehydrating agent to obtain the triethylamine, and (iv) adding hydrochloric acid to the mother solution in the tower bottom to regulate the pH to neutral, then performing solid-liquid separation and discharging the separated waste water.    USE - The method is useful for treating mother solution of glyphosate.    ADVANTAGE - The method: has simple operation process; and is eco-friendly.    DETAILED DESCRIPTION - Treating mother solution of glyphosate comprises (i) adding calcium hydroxide aqueous solution to regulate acidic mother solution of glyphosate into alkaline mother solution and producing triethylamine from the triethylamine hydrochloride in the mother solution, (ii) distilling the treated mother solution of glyphosate by a distillation tower, collecting the distillate at 40-100 degrees C from the tower top, (iii) adding dehydrating agent into the distillate from the tower top to obtain the triethylamine, and (iv) adding hydrochloric acid to the mother solution in the tower bottom to regulate the pH to neutral, then performing solid-liquid separation and discharging the separated waste water after treating .
NOVELTY - Multifunctional soil conditioner comprises organic waste, nitrogen fertilizer (0.5-5 %), modified chitosan and polyacrylamide, where the weight ratio of organic waste to modified chitosan (0.1-1 %) to polyacrylamide is 1:(0.5-5):(0.01-0.05); the weight ratio of carbon to nitrogen is 20-50 in the organic waste; the organic waste is bagasse and waste bacterial pack; the deacetylation degree of the modified chitosan is more than 92 %.    USE - Used as a multifunctional soil conditioner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing multifunctional soil conditioner, comprising (i) fermenting organic waste, pre-drying bagasse and waste bacterial pack, controlling content of nitrogen fertilizer (0.5-5 %) and water (50-70 %), packing and fermenting the material naturally, where the ratio of the carbon to nitrogen is 20-50, (ii) mixing fermented organic waste, modified chitosan solution (0.1-1 %) and polyacrylamide according to the weight ratio of 1:(0.5-5):(0.01-0.05) to obtain the product.
NOVELTY - The system (200) has a carbon reformer (110) to perform reforming of carbon into steam and air at a temperature of 700 degree Centigrade, and to generate the hydrogen gas and carbon monoxide gas. The alkali metal carbonate is provided in the carbon reformer. The dust is removed from the carbon monoxide gas using a dust remover (140). The catalytic reaction is performed with respect to the hydrogen emitted from an anode (161) of a fuel cell (160) by a catalytic reactor (170) using a fuel catalyst, to generate electricity.    USE - Fuel cell combined electric power system.    ADVANTAGE - A high efficiency and environmental friendly fuel cell combined electric power system can be provided reliably with sufficient precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heat supply method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell combined electric power system. (Drawing includes non-English language text)    Carbon reformer (110)    Dust remover (140)    Fuel cell (160)    Anode (161)    Catalytic reactor (170)    Fuel cell combined electric power system (200)
NOVELTY - The reactor has a transparent window (120) that is arranged in the front side of main portion (110) of reactor. A transfer unit (140) is installed on the internal spaces (111) of reactor main portion corresponding to the heat collector (130) made of metal oxide. The solar energy is absorbed by the catalyst layer (131) of heat collector. The position of heat collector is varied from the focus point at which the sunlight is gathered, by collecting the information of temperature condition required for the reaction by the transfer unit.    USE - Hydrogen phosphorus solar chemical reactor.    ADVANTAGE - The position of heat collector is easily changed from the focus point of sunlight in flexible manner, by collecting the information of temperature condition of chemical reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solar chemical reactor.    Reactor main portion (110)    Internal spaces (111)    Window (120)    Heat collector (130)    Catalyst layer (131)    Transfer unit (140)
NOVELTY - Composting involves mixing compost material and bacterial agent, fermenting obtained compost at high temperature to obtain primary composting product, and continuously fermenting the primary composting product to obtain fertilizer.    USE - Method for composting used for preparing fertilizer (claimed).    ADVANTAGE - The method recycles heat produced by high-temperature fermentation simultaneously with the addition of bacterial agent in the composting process.
NOVELTY - Preparing normal-butane by absorption and rectification combined extraction method, preferably formed by integrally assembling a raw can, an absorption can, a rectification tower and a product steel bottle which are connected by the connection pipeline with a control valve.    USE - The method is useful for preparing normal-butane by absorption and rectification combined extraction method.    ADVANTAGE - The method: has simple preparation; produces the product with high purity; and is environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the process for carrying out the preparation of normal-butane by absorption and rectification combined extraction method.
NOVELTY - Device for preparing n-butane using adsorption-separation technology, comprises a raw material tank, an absorption device, a rectification tower, a product cylinder, which are integrally connected by a connection pipeline with a control valve.    USE - The device is useful for preparing n-butane using adsorption-separation technology.    ADVANTAGE - The method is simple to carry out, produces n-butane with high purity and does not cause environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device.
NOVELTY - Liquid fuel comprises (in wt.%): pure alcohol (70), an auxiliary heating agent (0.2), an explosion protection agent (0.3), an essence (0.1), an insect repellent (0.1), a pigment (0.15) and water (remaining amount).    USE - Used as a liquid fuel.    ADVANTAGE - The liquid fuel, in comparison with the conventional liquid fuel: is economical, safe, clean, environmental friendly and convenient to use; comprises low-cost raw materials, which are extensive; does not require a special equipment for production; has strong power and high heat value; saves energy; disperses fragrance in the room to expel the mosquito and fly; and can be packed in a plastic barrel or an iron barrel, which is convenient and safe and the package cost is low.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the liquid fuel, comprising: (a) dissolving the pure alcohol (70%) and auxiliary heating agent (0.2%) in a plastic barrel, agitating for 40 minutes; (b) adding water, the insect repellent (0.1%), the pigment (0.1%) and the essence (0.1%); (c) adjusting the pH to neutral with sodium hydroxide solution, storing for overnight to remove the impurity, extracting the clear liquid and packaging the liquid in the barrel.
NOVELTY - Method for recycling resources, involves collecting large quantity of naturally-growing natural resources, and mixing the resources with grass fodder, livestock excrement, water balancing material and mixed rotted material.    USE - The method is useful for recycling resources for producing biogas used as fuel energy, and liquid fertilizer (claimed).    ADVANTAGE - The method utilizes naturally-growing natural resources, preferably livestock excrement, food waste and by-product compost which spoil city environment and prevents acidification of farmland, benefit economical management of livestock industry, and hence is environmentally-friendly and economical. The method protects health of the people by removing bad smell contamination and environmental contamination.
NOVELTY - Method of treating anaerobic digested liquid of livestock and poultry breeding waste for producing methane, involves subjecting livestock and poultry breeding waste to anaerobic digestion to obtain methane and anaerobic digested liquid, separating the liquid, centrifuging the obtained liquid, transferring the supernatant into a chemically enhanced primary treatment tank, adding flocculant to the liquid, and refluxing the sludge mixed liquid with clean water in the digestion system.    USE - The method is useful for treating anaerobic digested liquid of livestock and poultry breeding waste (claimed).    ADVANTAGE - The method is rapid.    DETAILED DESCRIPTION - Method of treating anaerobic digested liquid of livestock and poultry breeding waste, involves subjecting livestock and poultry breeding waste to anaerobic digestion to obtain methane and anaerobic digested liquid, separating the liquid, settling the liquid using pre-sedimentation tank, centrifuging the obtained liquid, transferring the supernatant into a chemically enhanced primary treatment tank, adding flocculant to the liquid for removing phosphorus from the liquid, transferring the liquid to anoxic/aerobic membrane bioreactor through the primary treatment tank for removing organic matter, phosphorus and nitrogen in a membrane component efficiently and simultaneously, separating the liquid, refluxing the sludge mixed liquid with clean water in the digestion system to obtain zero emission of wastes, denitrifying the sludge mixed liquid using anoxic reactor through reflux pump under aerobic condition, and refluxing the obtained liquid with clean water in anaerobic digestion system through circulating water pump at interval.
NOVELTY - Afforestation structure of full-ecological roof, comprises afforestation plants, nutrient soil layer, root insulation film, filtering layer and waterproof layer. The structure further comprises heat insulation layer, and intelligent dripping pipe system installed in the nutrient soil layer. The thickness of the waterproof layer, root insulation film, heat insulation layer, filtering layer and nutrient soil layer are 0.2-0.4 cm, 0.02-0.05 cm, 5-12 cm, 0.02-0.05 cm and 3-6 cm respectively.    USE - The afforestation structure of full-ecological roof is useful for constructing roof into totally-ecological green park.    ADVANTAGE - The afforestation structure is environmentally-friendly, consumes less energy and has high tensile strength, excellent heat insulation property, water-tightness property, penetration property, temperature resistance, cold resistance, aging resistance, barren resistance, drought resistance, and corrosion resistance. The waterproof layer prevents leakage of water and root insulation film prevents root system from penetrating the waterproof layer, and has prolonged service life. The nutrient soil layer supplies substrate with abundant nutrition and water and gas ventilation to afforestation plants, and hence plants, preferably sedum lineare series and Taiwan grass series grows vigorously and are evergreen in all four seasons.    DETAILED DESCRIPTION - Afforestation structure of full-ecological roof, comprises afforestation plants, nutrient soil layer, root insulation film, filtering layer and waterproof layer. The structure further comprises heat insulation layer, and intelligent dripping pipe system installed in the nutrient soil layer. The thickness of the waterproof layer, root insulation film, heat insulation layer, filtering layer and nutrient soil layer are 0.2-0.4 cm, 0.02-0.05 cm, 5-12 cm, 0.02-0.05 cm and 3-6 cm respectively, where the layers are arranged from lower to upper direction.
NOVELTY - Soil enhancing material for promoting the growth and/or development of a plant when grown in a growing medium containing the soil enhancing material, where the soil enhancing material comprising at least one viticulture material or a material derived from a viticulture material and one or two components derived from vegetation, where the viticulture material and the components derived from vegetation are, or are derived from, naturally occurring materials.    USE - The soil enhancing material is used for promoting the growth and/or development of a plant when grown in a growing medium containing the soil enhancing material (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a plant grown or growing in a plant growing medium for enhancing the growth and/or development of the plant; and    (2) a method of forming a soil enhancing material to provide improved growth of a plant when grown in the soil enhancing material comprising: (a) selecting a viticulture product or a material derived from a viticulture product; (b) sizing the viticulture product to a predetermined size, or range of sizes; (c) selecting a component derived from vegetation; (d) sizing the vegetation product to a pre-arranged size or range of sizes; and (e) mixing the viticulture product and vegetation product together to form a mixture of the viticulture product and vegetation product, where the size of the viticulture product is compatible with the size of the vegetation product so that the mixture forms the soil enhancing material.
NOVELTY - A partition wall separates mixing unit (100), reaction bath (200) and liquefied fertilizer generation unit (300). An exhaust gas valve (220) is connected at lower end side of mixing unit, to eject sampled gas. Liquefied fertilizer generation unit is connected to side of reaction bath, and sight glass (310) and precipitate drop hole (320) to pass precipitate from reaction bath. Organic waste is annihilated and recycled by tightness of reaction bath, fertilizer generation unit connected to precipitate water storage tank (400) after cultivation of microorganism.    USE - Apparatus for annihilation and recycling of organic waste by multi-phase long-term stay process.    ADVANTAGE - The environmental contamination by annihilation and recycling of organic waste can be prevented by removing the treated organic waste effectively. Highly concentrated liquid manure and methane can be obtained by performing recycling process at reduced processing cost. The clean carbon credit security of organic waste annihilation and recycling, is ensured through warming gas reduction. The maintenance and repair process of organic waste annihilation and recycling process can be performed effectively. The reuse of resource can be ensured at high profitability at ensured environmental protection effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for annihilation and recycling of organic waste by multi-phase long-term stay process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for annihilation and recycling of organic waste by multi-phase long-term stay process.    Mixing unit (100)    Reaction bath (200)    Exhaust gas valve (220)    Liquefied fertilizer generation unit (300)    Sight glass (310)    Precipitate drop hole (320)    Precipitate water storage tank (400)
NOVELTY - The apparatus has organic waste supply pump (102) which supplies the organic waste to the expansion jaw (111). A partition wall (116) is arranged to separate the expansion jaw and digestion tub (112). The organic waste from the expansion jaw is supplied to the digestion tub from expansion jaw. The biogas stirring unit (122) is made to supply biogas to digestion tub, so that the biogas is mixed with organic waste in digestion tub, so as to carry out methane fermentation of organic waste in digestion tub.    USE - Anaerobic absorption apparatus for treating organic waste such as sewage sludge.    ADVANTAGE - The anaerobic digestion of organic waste can be performed efficiently, so that organic waste can be treated reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic digestion method for treating organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic absorption apparatus. (Drawing includes non-English language text)    Organic waste supply pump (102)    Expansion jaw (111)    Digestion tub (112)    Partition wall (116)    Biogas stirring unit (122)
NOVELTY - Optimizing the composition of biofuel comprised of fatty acid alkyl esters involves (a) submitting sample of fatty acid alkyl ester-containing component of the biofuel to analyzer which measures the mass percentages in the component of at least two fatty acid alkyl esters; (b) inputting values indicative of at least two fatty acid alkyl ester mass percentages into processor with preprogrammed instructions; and (c) controlling blending of the biofuel in response to the processor output signal.    USE - For optimizing composition of biofuel comprised of fatty acid alkyl esters (claimed).    ADVANTAGE - The method accurately and conveniently analyzes fatty acid alkyl ester-containing biofuels such as biodiesel, which enables fuel formulators to optimize the design of fatty acid alkyl ester-containing biofuels, and which facilitates the identification of fatty acid alkyl ester-containing biofuel's feedstock; and has speed and economy prove well-suited for refinery operation.    DETAILED DESCRIPTION - Optimizing the composition of biofuel comprised of fatty acid alkyl esters, involves: (a) submitting sample of fatty acid alkyl ester-containing component of the biofuel to analyzer which measures the mass percentages in the component of at least two fatty acid alkyl esters; (b) inputting values indicative of at least two fatty acid alkyl ester mass percentages into a processor with preprogrammed instructions (1) calculates at least one fatty acid alkyl ester mass percentage ratio and algorithmically determines the volumetric percentages of at least one fatty acid alkyl ester in the component using at least one fatty acid alkyl ester mass percentage ratio as algorithmic independent variables (2) correlates the fatty acid alkyl ester volumetric percentages to fuel performance data and generates output signal indicative of that correlation; and (c) controlling blending of the biofuel in response to the processor output signal.
NOVELTY - Bio-gasoline composition (I) comprises hydrocarbons, oxygenates and phenolic compounds (at least 5 wt.%), where (I) has a total oxygen content of less than 15 wt.%.    USE - (I) is useful for producing a renewable gasoline.    ADVANTAGE - (I) is economic and eco friendly.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of a biomass conversion system.    Biomass source (12)    Biomass feed system (14)    Biomass conversion reactor (16)    Conversion effluent (18)    Solids separator. (20)
NOVELTY - Device for obtaining biofuel, contains housing, loading and trigger connecting branches, and cartridges with thermometers, where vertically in the center of device the hollow shaft is installed, on which hollow gate mixer is installed.    USE - For obtaining biofuel (claimed).
NOVELTY - Energy-effective mobile complex of discharge timber ties utilization, comprises a chamber for drying ground tie mass, pyrolysis chamber, furnace, condenser and chamber to collect condensate of pyrolytic gases, chipping machine, air duct with gas-purifying installation, gas receiver, furnace economizer, and coal activation chamber.    USE - The energy-effective mobile complex of discharge timber ties utilization is useful for industrial and commercial applications.    DETAILED DESCRIPTION - Energy-effective mobile complex of discharge timber ties utilization, comprises a chamber for drying ground tie mass, pyrolysis chamber, furnace, connected by the air duct to the drying chamber, condenser and chamber to collect condensate of pyrolytic gases; the complex, arranged on the railroad flatcar, comprises the installation of mechanical cleaning of the surface of ties, chipping machine to crush ties, air duct with gas-purifying installation, gas receiver, furnace economizer, coal activation chamber configured to activate coal due to water vapor overheated in the furnace economizer; the complex is configured to heat the tie mass in the pyrolysis chamber due to the heat of the pyrolytic gas, heated in the furnace economizer, and to isolate non-condensed portion of pyrolytic gases, collected in the gas receiver, as fuel.
NOVELTY - The furnace has an elbow whose side opening is connected with an inlet pipe of a furnace head. One end of the inlet pipe of the furnace head is connected with a peripheral wall of the furnace head provided with a round groove-shaped pedestal. A top part of the pedestal is provided with a stage-type turned edge, which is connected with the pedestal and bent inward and downward. The turned edge and a bottom part of the groove are formed with distance. The stage-type turned edge is provided with a pore plate-shaped furnace disk.    USE - High-temperature short-flame straw gasification furnace.    ADVANTAGE - The furnace is safe to use, durable, and saves fuel and ensures continuous ignition for long time.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a high-temperature short-flame straw gasification furnace.