NOVELTY - Decomposition treating method of cellulose organic substance using methane fermentation, involves operating methane fermentation processing tank converted into biogas which carries out microbial decomposition processing of process target object containing cellulose organic substance, and comprises methane by continuous type or half batch formula when accommodating support which can support microorganisms in methane fermentation processing tank, and subjecting anaerobic cellulose decomposer microbe.    USE - The decomposition treating method is useful for cellulose organic substance using methane fermentation (claimed).    ADVANTAGE - The method provides long term stability, improves cellulose decomposition process, reduces initial stage installation cost and running cost, and eliminates problem of driving operation of whole processing system, or complexity of maintenance management.
NOVELTY - Fuel cell system comprises fuel cell that produces electric power using fuel gas and oxidizing agent gas; hydrogen generating apparatus that produces fuel gas; combustor that heats hydrogen generating apparatus; combustion exhaust path for discharging exhaust gas combustor; cathode exhaust route for discharging cathode off gas from fuel cell; stored water device; water level detector (17) for detecting water level of stored water device when below predetermined height; and drainage path (13).    USE - Fuel cell system, e.g. polymer electrolyte fuel cell or solid oxide fuel cell.    ADVANTAGE - The fuel cell system prolongs usage of stored water device, while suppressing power consumption required for water level control of stored water device. The stored water device can maintain water quantity and drive fuel cell system stably.    DETAILED DESCRIPTION - Fuel cell system comprises fuel cell that produces electric power using fuel gas and oxidizing agent gas; hydrogen generating apparatus that produces fuel gas; combustor that heats hydrogen generating apparatus; combustion exhaust path for discharging exhaust gas combustor; cathode exhaust route for discharging cathode off gas from fuel cell; stored water device that collects condensed water vapor and is positioned in middle of combustion exhaust path; water level detector (17) for detecting water level of stored water device when below predetermined height; and drainage path (13) connected to stored water device for draining water. The stored water device has water-seal structure that keeps exhaust gas from flowing into drainage path, and switch (18) for closing drainage path.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system provided with stored water device.    Drainage path (13)    Inlet (15)    Discharge port (16)    Water level detector (17)    Switch (18)    Controller (19)    Partition (20)    Bottom face part (21)    Opening (22)
NOVELTY - The invention relates to a process for preparing composite molecular membranes to be employed in gas separation. According to the invention, the process consists in sintering a resorcinol-formaldehyde xerogel through the sol-gel method, within the walls of commercially-available macroporous monotubular ceramic supports, followed by drying, under normal conditions, for 15...25 days, to result in resorcinol-formaldehyde xerogel composites on ceramic support which, after the pyrolysis under inert atmosphere, at a temperature of 600...900 degrees C, are converted into carbon xerogel composites on ceramic support with gas separation/purification properties, for gases, such as hydrogen, methane, carbon dioxide and carbon oxide.
NOVELTY - Salt of 1-(2-deoxy-2-fluoro-4-thio-( beta )-D-arabinofuranosyl)cytosine, is new.    USE - The salt of 1-(2-deoxy-2-fluoro-4-thio-( beta )-D-arabinofuranosyl)cytosine is useful in pharmaceutical composition for treating tumor (claimed).    ADVANTAGE - The salt of 1-(2-deoxy-2-fluoro-4-thio-( beta )-D-arabinofuranosyl)cytosine is being produced under environmentally friendly conditions and not deliquescent, has excellent crystallinity, fluidity, tableting property, storage stability, and high solubility with respect to water and thus highly suitable for mass production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the salt of 1-(2-deoxy-2-fluoro-4-thio-( beta )-D-arabinofuranosyl)cytosine which involves converting 1-(2-deoxy-2-fluoro-4-thio-(beta)-D-arabinofuranosyl) cytosine into the salt.
NOVELTY - Sludge destructive distillation energy conversion process, comprises: (a) drying sludge material using a rotary drying furnace; (b) passing the mixture of agriculture and forestry waste material into drying furnace, mixing the sludge and mixture of agriculture and forestry waste material and passing into a material forming device; and (c) subjecting the molding material of the mixture of the sludge and agricultural and forestry waste to destructive distillation energy conversion in the destructive distillation furnace.    USE - The method is useful for converting sludge destructive distillation energy to produce combustible methane gas, crude charcoal, and a part of liquefied products (wood vinegar, wood tar, etc.) (all claimed).    ADVANTAGE - The method can solve the sludge stabilization and harmlessness processing, while the sludge is made to achieve energy self-sufficiency in the destructive distillation energy conversion process to generate economic benefits. The method has good practical significance and widespread promotion using value.    DETAILED DESCRIPTION - Sludge destructive distillation energy conversion process, comprises: (a) drying sludge material until the water content is not less than 30% using a rotary drying furnace, passing the mixture of agriculture and forestry waste material into the drying furnace, mixing the sludge and mixture of agriculture and forestry waste material with a ratio of 3:7 until the moisture content of the mixture is reduced to 20%; (b) passing the mixture of sludge, agriculture and forestry waste into a material forming device with a proportion of 1.1-1.3; and (c) and subjecting the molding material of the mixture of the sludge and agricultural and forestry waste to destructive distillation energy conversion in the destructive distillation furnace.
NOVELTY - A composite biomass fuel block comprises central carbon block coated with a combustion supporting layer in the outer surface to form fuel block material, combustion supporting space arranged in the central carbon block, and a combustion supporting structure arranged between the central carbon block and the combustion supporting layer.    USE - Composite biomass fuel block (claimed).    ADVANTAGE - Since the composite biomass fuel block has a flat core, the fuel block can be stored and transported easily. The composite biomass fuel block has high density, small size and high flash point, is safe and convenient for storage, is clean, has favorable combustion characteristics and high burn-off rate.
NOVELTY - A composite biomass fuel rod comprises carbon rod core, combustion supporting layer provided on carbon rod core, a combustion supporting space arranged in carbon rod core, and combustion supporting structure arranged between carbon rod core and combustion supporting layer.    USE - Composite biomass fuel rod (claimed).    ADVANTAGE - The composite biomass fuel rod has high density, high flash point, high burn-off rate, excellent storage stability and combustion characteristics, and small size.
NOVELTY - Penicillium oxalicum HB1 (CGMCC NO: 4842) fermenting solution used in agriculture is claimed. The fermenting solution is prepared by taking dry corn straw powder, beef extract peptone, and HB1 bacterial suspension in a ratio of 8-25 g: 1-2 g: 1 ml, and adding 100 ml water.    USE - Penicillium oxalicum HB1 fermenting solution is used in agriculture (claimed).    ADVANTAGE - The method can realize non-pollution treatment of the straw, and also can increase soil fertility, uses the fermentation solution to accelerate the corn straw to decay, is suitable in straw returning field area for promoting corn straw decay.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use method of fermentation solution either: in the production of agricultural plants, comprising adding 4-5 corn straw powder in 1 kg soil, mixing uniformly, surface spraying 1-3 ml fermenting solution, and watering the soil, where the soil water content is 20-25%; or in the corn straw field, comprising crushing normal corn straw, maintaining soil relative humidity by watering or other ways at 65-80%, spraying 50-75 kg/667m2 fermentation solution on the crushed corn straw surface, ploughing immediately or rotary tillage.
NOVELTY - The recycling system comprises a rotary die and a cartridge die to clean a guide jig, a rotor driven with a spindle axis to drive the system, a planetary ring gear for modifying an operating mode of the rotor, and a shield attached at a top portion of a roller and a front cover attached with a housing and a main body.    USE - The recycling system is useful for processing solid waste i.e. domestic waste to produce solid fuel or refuse-derived fuel (RDF) (claimed).    ADVANTAGE - The recycling system reduces environmental contamination and the generation of bad smell, increases the depletion of the fossil fuel and produces the RDF fuel in efficient and inexpensive manner.
NOVELTY - Preparing trans-2-(3,4-difluorophenyl)cyclopropanamine (IX), comprises: providing trans-2-(3,4-difluorophenyl)cyclopropanecarbohydrazide (V); converting (V) to trans-2-(3,4-difluorophenyl) cyclopropanecarbonyl azide (VI); and converting (VI) to provide (IX).    USE - The process is useful for preparing (IX), where (V) and (IX) are useful in the preparation of ticagrelor (claimed), which is useful for treating or preventing thrombotic events e.g. stroke, heart attack, acute coronary syndrome or myocardial infection with ST elevation, other coronary artery diseases and arterial thrombosis and other disorders related to platelet aggregation. No biological data given.    ADVANTAGE - The process utilizes environmentally friendly and non-explosive reagents and is industrially applicable and economical process.    DETAILED DESCRIPTION - Preparing trans-2-(3,4-difluorophenyl)cyclopropanamine of formula (IX) or its salt, comprises: providing trans-2-(3,4-difluorophenyl)cyclopropanecarbohydrazide of formula (V); converting (V) to trans-2-(3,4-difluorophenyl) cyclopropanecarbonyl azide of formula (VI); and converting (VI) to provide (IX) or its salt, where chiral center asterisk is in its (R) or (S) configuration. INDEPENDENT CLAIMS are also included for:    (1) the trans-2-(3,4-difluorophenyl)cyclopropanecarbohydrazide (V) and their stereochemical isomeric forms; and    (2) a crystalline hydrochloride salt of (IX), which is (1R,2S)-2-(3,4-difluorophenyl)cyclopropylamine) hydrochloride.
NOVELTY - Method for preparing an aromatic compound, involves condensing two or more aromatic rings through a carbon-carbon bond or an ether bond, and allowing a protein which belongs to family 153 (CYP153) of the cytochrome P450 or a fusion type protein containing this is functioned as a monooxygenase, to react with two or more aromatic compounds having phenolic hydroxyl group.    USE - The method is useful for preparing aromatic compound which is used as pharmaceutical, agrochemical, and dye e.g. synthetic intermediate.    ADVANTAGE - The method is suitable for mass production, environmentally-friendly and cost-effective, easily converts product, utilizes biocatalyst derived from bacteria, and does not adopts complicated steps.
NOVELTY - Preparation of methane special-purpose carbon adsorbent in pressure swing adsorption involves crushing coal powder, adding 40-45 pts. wt. coal tar, 3-8 pts. wt. sodium hydroxide, 4-6 pts. wt. potassium nitrate, 3-8 pts. wt. calcium carbonate, 4-6 pts. wt. magnesium chloride and 10-20 pts. wt. water in 100 pts. wt. pulverized coal material, providing the precursor in rotating furnace or multifunctional converter, activating in presence of water vapor, soaking resultant product in hydrochloric acid solution, washing with water, and drying.    USE - Preparation of methane special-purpose carbon adsorbent in pressure swing adsorption (claimed).    ADVANTAGE - The method provides methane special-purpose carbon adsorbent in pressure swing adsorption having high strength, centralized micropores, large pore volume, quick adsorption characteristics and desorption speed, methane adsorption volume of 25 ml/g, carbon monoxide adsorption of less than 2 ml, and increased methane adsorption quantity.    DETAILED DESCRIPTION - Preparation of methane special-purpose carbon adsorbent in pressure swing adsorption involves crushing coal powder with particle diameter of more than 200 meshes to obtain pulverized coal material, adding 40-45 pts. wt. coal tar, 3-8 pts. wt. sodium hydroxide, 4-6 pts. wt. potassium nitrate, 3-8 pts. wt. calcium carbonate, 4-6 pts. wt. magnesium chloride and 10-20 pts. wt. water in 100 pts. wt. pulverized coal material, stirring the resultant product, extruding strips, stewing, carbonizing to obtain precursor, providing the precursor in rotating furnace or multifunctional converter, activating in presence of water vapor at 850-950 degrees C, soaking resultant product in hydrochloric acid solution for 8-24 hours, washing with water, and drying at 120 degrees C for 1 hour.
NOVELTY - Removing oxytetracycline from livestock and poultry breeding wastewater using straw biomass carbon, involves: adding biomass carbon into aqueous solution containing the oxytetracycline and copper (Cu2+) according to the solid-liquid ratio (g/mL) of (1:50)-(1:100), adjusting the pH to 3.5-7.5, and stirring for 24-48 hours.    USE - The method is useful for removing oxytetracycline from livestock and poultry breeding wastewater using straw biomass carbon (claimed).    ADVANTAGE - The method uses agricultural straws as a raw material to prepare the biomass carbon so as to realize reasonable and effective utilization of the agricultural waste, so the method is not only low in cost, but also environment-friendly. The rate of adsorbing and removing the oxytetracycline from the aqueous solution by the biomass carbon at 600 degrees C is highest; when the initial concentration is lower than 92 mg/L, both the adsorption rate and the removal rate can be above 92%.
NOVELTY - Synthesis of allicin derivatives comprises reacting disulfide derivative and hydrogen peroxide with proline and oxidant in solvent.    USE - Method for synthesizing allicin derivatives of formulae R1-S-S(O)(O)-R2 and R1-S-S(O)-R2 (claimed).    ADVANTAGE - The method is simple and environment-friendly and has high yield and mild condition.    DETAILED DESCRIPTION - Synthesis of allicin derivatives of formulae R1-S-S(O)(O)-R2 and R1-S-S(O)-R2 comprises reacting disulfide derivative of formula R1-S-S-R2 and hydrogen peroxide with proline in solvent.    R1,R2=1-4C alkane or 2-4C olefin, preferably Me, Et, Pr, Bu, iPr, or cyclopropyl.
NOVELTY - Preparation of oxiracetam comprises reacting 4-methoxy-3-pyrroline-2-one-1-yl-acetic acid under acidic condition to obtain 2,4-dioxopyrrolidin-1-yl-acetic acid; reducing obtained product under alkaline condition to obtain 4-hydroxy-2-oxopyrrolidin-1-yl-acetic acid; reacting obtained product with methyl ester to obtain 4-hydroxy-2-oxopyrrolidin-1-yl-acetic acid methyl ester; and carrying out ammonolysis with obtained product.    USE - Method for preparing oxiracetam (claimed).    ADVANTAGE - The method is simple and environment-friendly and has low cost and short production time.
NOVELTY - Preparing ezetimibe intermediate compounds (I), comprises reacting 3-(1-(4-fluorophenyl)-2-(4-hydroxyphenyl)-4-oxoazetidin-3-yl)propanal compounds (II) with ternary complex system composed of chiral catalyst, titanate ester and p-fluorophenylmagnesium halide (III) in an ether solvent.    USE - The method is useful for preparing ezetimibe intermediate compounds.    ADVANTAGE - The method: has simple operation, low cost and simple post-process; produces high de-value (more than 99%) product; is suitable for industrial production; and is environment-friendly.    DETAILED DESCRIPTION - Preparing ezetimibe intermediate compounds of formula (I), comprises reacting 3-(1-(4-fluorophenyl)-2-(4-hydroxyphenyl)-4-oxoazetidin-3-yl)propanal compounds of formula (II) with ternary complex system composed of chiral catalyst, titanate ester and p-fluorophenylmagnesium halide of formula (III) in an ether solvent.    R = H, benzyl, substituted arylmethyl, substituted silyl or tetrahydro-2H-pyran group; and    X = halo.
NOVELTY - The utility model claims a plant breeding poultry excrement processing device, specifically a method for producing poultry excrement ecological feedstuff and fertilizer. The device comprises a raw material supply device, a stirring device, a heating device, a fermentation discharge device, an air inducing device, stirring and fermenting device is set at the lower part, the inlet of the discharge hole is connected with the spiral stirring and fermenting device of the raw material supply device, stirring and fermenting device is connected with the discharge device, a heating device connected with the interlayer and a stirring and fermenting device, a stirring fermentation device air outlet is connected with an air inducing device. This new device capable of making poultry excrement after stirring and oxygen, a material heating, slow temperature, detoxification and sterilizing discharging, short action time in the stirring and fermenting device, so excrement can keep the original nutrient substance. Providing a powerful device support for breeding livestock excrement treatment problem.
NOVELTY - An innocuous garbage comprises basic structure containing tribasic system completely separate set of each type to both completely isolated from the atmosphere, and is obtained by supplying energy heating system isolated materialized biomass conversion device system assembly, carrying out dry distillation system for continuous dry distillation of waste material using molded charcoal produced by dry distillation or pyrolysis gas generated by condensing and separating the primary noncondensable gas, and carrying out continuous catalytic reforming catalytic reforming system.    USE - Innocuous garbage (claimed).    DETAILED DESCRIPTION - An innocuous garbage comprises basic structure containing tribasic system completely separate set of each type to both completely isolated from the atmosphere, and is obtained by supplying energy heating system completely isolated materialized biomass conversion device system assembly at (120-240) plus minus 10 degrees C under vacuum conditions, carrying out waste materials for continuous drying system at (350-750) plus minus 10 degrees C under vacuum condition, carrying out dry distillation system for continuous dry distillation of waste material at (800-900) plus minus 10 degrees C for constant temperature under thermal cracking gas using molded charcoal produced by dry distillation or pyrolysis gas generated by condensing and separating the primary noncondensable gas, and carrying out continuous catalytic reforming catalytic reforming system. An INDEPENDENT CLAIM is included for resource treatment method of innocuous garbage.
NOVELTY - Biological organic fertilizer comprises 30-50 wt.% dairy manure, 5-25 wt.% microbial strain agent, 9-25 wt.% straw stalk, 0.1-6 wt.% zinc oxide or zinc salt and 6-25 wt.% magnesium oxide or magnesium salt.    USE - The fertilizer is useful for Gannan red and yellow soil region (claimed).    ADVANTAGE - The fertilizer enables to supplement nutrition in crops in timely manner, promote crop growth, eliminate common magnesium and zinc deficiency in the citrus orchard of the Gannan red and yellow soil region, and improve yield of the citrus trees.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) uniformly mixing the zinc oxide or zinc salt and magnesium oxide or magnesium, (b) mixing dairy manure and microbial strain agent, and (c) fermenting the mixture obtained in the steps (a) and (b).
NOVELTY - A water-based aerosol comprises 15-30 pts. wt. propellant, 2-8 pts. wt. foaming agent, 0.2-0.3 pt. wt. sodium benzoate, 0.2-0.3 pt. wt. sodium nitrite, 67-77 pts. wt. deionized water and 0-0.5 pt. wt. sodium hydroxide.    USE - Water-based aerosol.    ADVANTAGE - The aerosol is non-flammable, has low cost, has no environmental pollution and can create snow scene.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of water-based aerosol comprising adding deionized water into stirring kettle, starting stirrer, adding sodium hydroxide, sodium benzoate and sodium nitrite, stirring for 5-10 minutes to completely dissolve, adding foaming agent, continuously stirring for 5-15 minutes to completely dissolve, filling into aerosol tank having filter screen of 300-400 meshes, valve sealing, filling propane and butane and installing spraying cover.
NOVELTY - A low temperature microwave plasma reformer in car used for production of hydrogen comprises system controller (1001), power supply regulator (1019), microwave generating magnetron (1020), wave guide (1021), coaxial transmission device (1022), resonant cavity (1018), heat exchanger (1007), and evaporator (1008). The system controller controls flow rate and microwave power of fuel and water. The power supply regulator is used for adjusting microwave magnetron. The electric energy is converted to microwave at 2.45 GHz by microwave generating magnetron.    USE - Low temperature microwave plasma reformer in car used for production of hydrogen.    DETAILED DESCRIPTION - A low temperature microwave plasma reformer in car used for production of hydrogen comprises system controller (1001), power supply regulator (1019), microwave generating magnetron (1020), wave guide (1021), coaxial transmission device (1022), resonant cavity (1018), heat exchanger (1007), and evaporator (1008). The system controller controls flow rate and microwave power of fuel and water. The power supply regulator is used for adjusting microwave magnetron. The electric energy is converted to microwave at 2.45 GHz by microwave generating magnetron. The relationship between ethanol vapor flow rate and chemical excitation of plasma state of microwave power is Pmic(W)=254.82(J)/46(g) Reth(g/s)=5.54Reth. The mass flow rate ratio of ethanol and water is 46:18 equal to 2.56.    Reth(g/s)=mass flow rate of ethanol and steam in g/s.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of microwave plasma reformer in car.    System controller (1001)    Heat exchanger (1007)    Evaporator (1008)    Resonant cavity (1018)    Power supply regulator (1019)    Microwave generating magnetron (1020)    Wave guide (1021)    Coaxial transmission device (1022)
NOVELTY - Preparation of aromatic aldehyde, being a toluene compound comprises mixing bromine initiator, catalyst, toluene compound and polar organic solution in a reaction container, introducing oxygen into the reaction container, and reacting at 30-120 degrees C for 5-15 hours while stirring.    USE - Method for preparation of aromatic aldehyde (claimed).    ADVANTAGE - The method is environment-friendly and has mild reaction condition and high product selectivity and yield. Catalyst preparation and separation are simple.
NOVELTY - Phosphinate salt metal organic frame compound (I) is new.    USE - Phosphinate salt metal organic frame compound used for separating nitrogen and oxygen, and separating carbon dioxide and methane (claimed).    ADVANTAGE - The organic frame compound has good oxygen/nitrogen gas and carbon dioxide/methane selectively adsorbing performance.    DETAILED DESCRIPTION - Phosphinate salt metal organic frame compound of formula (Ni1.5 (4,4'-bipy)1.5(H3L)(H2O)3)(H2O)0.5 (I), is new.    L=2,4,6-trimethylbenzene, or -1,3,5-trimethylene phosphonic acid.    An INDEPENDENT CLAIM is included for a preparation of (I).
NOVELTY - Cobalt complex (I) is new.    USE - Complex (I) used as catalyst for electrochemical decomposition of water to generate hydrogen (claimed).    ADVANTAGE - The complex (I) shows extremely low overpotential on catalytic water (including seawater) reduction to generate hydrogen, and has high catalytic activity and stability.    DETAILED DESCRIPTION - Cobalt complex of formula (I) is new.    X=charge-balancing anion SO4, Cl, Br, OAc, BF4, or PO4; and    n=1 or 2.    INDEPENDENT CLAIMS are included for:    (1) preparation of complex (I); and    (2) electrochemical decomposition of water to generate hydrogen by catalytic reaction at 4-10 pH using complex (I) as catalyst.
NOVELTY - Micronomicin sulfate purification is carried out by passing micronomicin sulfate analytical solution through ultrafiltration membrane system to decolorize, then sending decolorized solution to nanofiltration membrane system, and concentrating filtrate. The ultrafiltration membrane system comprises a first-level ultrafiltration unit (1), a second-level ultrafiltration unit (2), and a third-level ultrafiltration unit (3) which are sequentially arranged. The nanofiltration membrane system comprises a nanofiltration membrane (7), a filter unit (8), and a third-level nanofiltration unit (9).    USE - Method for micronomicin sulfate purification (claimed).    ADVANTAGE - The method has simple technique and easy operation, less loss of active component, stable product quality, and reduced energy consumption and material consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a membrane system.    First-level ultrafiltration unit (1)    Second-level ultrafiltration unit (2)    Third-level ultrafiltration unit (3)    Nanofiltration membrane (7)    Filter unit (8)    Third-level nanofiltration unit (9)
NOVELTY - Process for producing extracted lipid, involves: i) extracting lipid from a collection of vegetative plant parts having a total non-polar lipid content of at least 10 wt./wt.% (dry weight); and ii) recovering the extracted lipid, where the volume of the extracted lipid is at least 1 liter.    USE - For producing extracted lipid from vegetative plant parts such as leaves, stems, roots and tubers, for producing industrial products such as alkyl esters, in particular methyl esters for blending with petroleum based fuel (all claimed).    ADVANTAGE - The method enables extraction of lipids from vegetative plant parts having a total non-polar lipid content of at least 10 wt./wt.% (dry weight). The extracted lipids produced are suitable for producing renewable biodiesel fuel.
NOVELTY - System for providing asset of closed cycle production, comprises bioreactor complex for generating biogas, gas-separating complex, unit of preparation of waste, pipeline and locking reinforcement, where the system is a catalyst device for converting a energy of methane from output of branch device in the vapors of water, saturated by carbonate gas with the releasing of heat for its subjecting the airspace of greenhouse complex for keep in it of optimum microclimate.    USE - The system is useful for providing asset of closed cycle production (claimed).    DETAILED DESCRIPTION - System for providing asset of closed cycle production, comprises bioreactor complex for generating biogas, gas-separating complex, unit of preparation of waste, pipeline and locking reinforcement, where the system is a catalyst device for converting a energy of methane from output of branch device in the vapors of water, saturated by carbonate gas with the releasing of heat for its subjecting the airspace of greenhouse complex for keep in it of optimum microclimate, where construction of catalyst device is contained pipeline reinforcement, by which it is conducted with the withdrawal of heat energy for keep of required temperature conditions in a greenhouse, bioreactor, preparation complexes, where the heat-transfer agent is water, and the recycling in the bioreactor wastes come to separating complex, where separation occurs into water to the preparation complex, fertilizer for a greenhouse, feed for animal, where the heat pump is supplied into the preparation complex for preliminary heating of the substrate.
NOVELTY - The tube (300) has a catalyzed electrode material (330) that is arranged inside of tube portion (310). A membrane (320) surrounds the hole for blocking the water molecule, while exchanging the hydrogen of cation in tube portion. The conductive medium is contained inside the tube portion. The hole is formed in side of tube portion. The electrode material is selected from platinum, palladium, ruthenium, iridium, cobalt molybdenum alloy.    USE - Phosphorus hydrogen depositing tube.    ADVANTAGE - The separation of hydrogen and oxygen generated in hydrolysis can be facilitated, such that hydrolysis efficiency can be improved reliably. The gap between hydrogen electrode and photo-electrode can be removed, such that the membrane area can be reduced effectively. The photoelectric conversion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the phosphorus hydrogen depositing tube.    Phosphorus hydrogen depositing tube (300)    Tube portion (310)    Membrane (320)    Electrode material (330)
NOVELTY - Silt and/or sediment of cleaning construction as feedstock is subjected to preconditioning treatment, lipid fraction is extracted and recovered using chloroform-methanol by Folch method. The extract is washed with potassium chloride, upper phase is removed using mixture of potassium chloride and methanol. The obtained extract of lipid is dried, passed through sodium sulfate, triglycerides are removed using methanol in presence of acid catalyst. The biodiesel is recovered from the reaction mixture, and obtained extract of biodiesel is dried, to obtain biodiesel fuel.    USE - Production of biodiesel fuel (claimed).    DETAILED DESCRIPTION - Silt and/or sediment of cleaning construction as feedstock is subjected to preconditioning treatment, lipid fraction is extracted and recovered using chloroform-methanol in volume ratio of 2:1 by Folch method. The extract is washed with 0.88% potassium chloride, and stratified. The upper phase is removed using 0.88 vol.% mixture of potassium chloride and methanol in ratio of 1:1. The obtained extract of lipid is dried, passed through sodium sulfate, triglycerides are removed using methanol in molar ratio of 1:9 in presence of acid catalyst. The biodiesel is recovered from the reaction mixture using hexane, and obtained extract of biodiesel is dried, to obtain biodiesel fuel. The volume ratio of methanol to acid catalyst is 50:1.
NOVELTY - This utility model claims a kind of marsh gas in anaerobic reactor, for solving the problem that the marsh gas in anaerobic reactor because of the problem of defect on the structure, the reactor in the reaction is not enough, the output is low, a kind of marsh gas in anaerobic reactor, comprising a reactor cylinder body, and the top is provided with a gas collecting device, the cylinder bottom is set with a water distribution device, the device is set on the wall surface of the reactor upper part of the cylinder body and connected with the reactor cylinder, stirring device is set in the reactor body wall surface of the lower part of the stirring shaft of the stirring device passes through the reaction chamber wall is connected with the reactor cylinder, the connecting part and the same horizontal plane of the reactor cylinder as a centre of a circle of the stirring shaft connected with an obtuse angle is a predetermined angle. The marsh gas industry anaerobic reactor, reacting adequately, marsh gas production is high.
NOVELTY - A pig raising waste water processing system, it comprises: the first is used for recycling MAP nitrogen phosphorus chemical sedimentation tank in the sewage component (1), a biochemical reactor for processing the clear liquid from the MAP chemical sedimentation tank (8). Clear liquid outlet of the MAP chemical deposition pool is connected with the anaerobic ferment period in the reactor biochemical filter tank (anaerobic water outlet of the clear liquid inlet, an anaerobic filter tank 2) is connected with the aerobic aeration tank (7) water inlet of the anaerobic, the aerobic water outlet of the aerobic aeration pool is connected with sedimentation tank (5) of the aerobic water inlet, the anaerobic filter tank (2) is connected with the biogas outlet collecting marsh gas tank (3). This utility model can reduce energy consumption, reduces sewage treatment cost, at the same time, capable of producing an organic compound fertilizer from the sewage.
NOVELTY - This utility model claims a kind of kitchen garbage recycling processing device, comprising organic fertilizer and organic fertilizer granulator comprises a motor, wherein the organic fertilizer granulator of the inlet end is provided with a semi-wet disintegrator of packaged solid material, fermenting and stacking a horizontal mixer, the outlet end of the organic fertilizer granulator and the inlet end of the roller sieving machine connected with the outlet end of the roller sieving machine connected with the rotary drying machine and organic fertilizer comprises a power, the organic fertilizer comprises a robot is provided with a automatic packaging scale and a belt conveyor. Kitchen garbage recycling processing device of the utility model is providing a, crushing, fermenting and stirring device is the inlet end of the organic fertilizer granulator, and provided with drum screening machine, a rotary drying machine and the organic fertilizer and organic fertilizer granulator comprises a machine, not only can the kitchen waste into organic fertilizer, reduce environmental pollution, but also realizes the automatic package from feeding, convenient to install, easy to popularize and apply.
NOVELTY - The utility model claims a fermentation system, claims a dynamic high temperature composting fermentation system, comprising a feeding system, a material-distributing machine, fermenting tower and discharging sub-system, the feeding sub-system through a material pipe and a distributor is used for walking is set on the track and can move along the walking track for a distributor feeding, the ferment tower is provided with a fermentation chamber, the fermentation chamber is set above the walking track, the mixing, the fermentation chamber is provided with an aeration device, the discharging sub-system arranged in the fermentation chamber; This utility model uses a distributor for fully mixing before the fermenting, provided with walking track of fermentation tower, wherein in the process of mixing can be the ferment, the system has compact structure, small area, low energy consumption, high degree of automation is high, and it can realize high-efficient organic fertilizer production and energy-saving.
NOVELTY - The method involves arising out reaction of sulfur oxides with calcium hydroxide in a pulverized coal boiler. An obtained product is mixed with fly ash in the pulverized coal boiler. Flue gas is introduced into the pulverized coal boiler.    USE - Method for treating a post-reaction product for performing a flue gas desulfurization process of a pulverized coal and biomass boiler.
NOVELTY - The additive composition comprises an organic peroxide and a solvent.    USE - Additive composition for ethanol-based fuels for reducing consumption and emissions (claimed).    ADVANTAGE - The additive composition saves fuel consumption and reduces emissions of gases that promote global warming without sacrificing qualities of fuel required by regulatory agencies.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing additive composition, which involves mixing 0.001-50.0 wt.% of organic peroxide with a final quantity of solvent until completing amount 100% by mass.
NOVELTY - This utility model claims one kind of butyl octanol tail gas recovery device for liquefied gas supply system, wherein it comprises a liquefied gas storage tank, the storage tank is connected with the liquefied gas liquefied gas feeding pump, feeding the liquefied gas pump is connected with the liquefied gas conveying pipeline and liquefied gas supply pipeline, a liquefied gas pipeline is connected with the raw material gas, and is provided with an adjusting valve is set on the supplementing pipeline, a raw material gas pipe connected to the absorption tower, the top of the absorption tower is provided with not condensed gas exhaust pipeline, the lower end of the absorption tower is connected with the absorption tower and reboiler, an absorption tower is connected with the agent feeding pipeline. The structure solves the problem that the tower kettle circulation of non-ideal condition, so as to reduce the product of the liquefied gas loss, at the same time, reduces the fluctuation in device operation process, which ensures the stable operation of the device.
NOVELTY - Mixture of carbon monoxide and hydrogen is contacted with synthesis gas and the mixed gas is supplied to reactor isothermal phase. The higher methane content gas is supplied to adiabatic reactor to obtain methane.    USE - Manufacture of methane (claimed).
NOVELTY - A methane-synthesis reactor consists of a reaction-gas inlet provided in a reaction-gas flow path including a catalyst, and a cooler provided in the reactor main component for circulating a refrigerant. The generated gas is ejected outside the reactor main component in the catalyst vicinity.    USE - Reactor is used for methane synthesis.    ADVANTAGE - The reactor enables efficient removal of heat-of-reaction during methane synthesis and improves production rate of methane. Since the reaction temperature is low, sintering of catalyst is prevented. Preheating cost of reaction gas is reduced as the reaction-gas inlet is heated by the heat-of-reaction.
NOVELTY - The device has two fermentation chambers (10, 12) provided with supporting bands. One of the fermentation chambers is provided with a stirrer, a heater, a power feeder plant mass and containers. A container external side is in a form of a truncated pyramid. A ventricular reservoir (4) is pumped into a tubular conduit and the other fermentation chamber. An overflow trap (18) is connected with insulating pipelines (24) and a sprinkler (5) and installed on the former fermentation chamber. Excess liquids from the insulating pipelines are fed into a reservoir (7).    USE - Biogas producing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas producing device.    Ventricular reservoir (4)    Sprinkler (5)    Reservoir (7)    Fermentation chambers (10, 12)    Overflow trap (18)    Insulating pipelines (24)
NOVELTY - The method involves sintering (S10) a porous layer ceramic support, and manufacturing (S20) a fuel anode transcription paper. The fuel anode functional layer transcription paper is formed (S30). The electrolyte transcription paper is manufactured and transferred (S40). The air electrode diffusion stopper transcription paper is formed (S50) on the transmitted layer. The air electrode transcription paper is formed (S60) on the air electrode diffusion stopper. The fuel anode functional layer is formed.    USE - Method for manufacturing solid oxide fuel cell (Claimed).    ADVANTAGE - The method involves sintering a porous layer ceramic support, and manufacturing a fuel anode transcription paper, and thus enables simplifying manufacturing process of solid oxide fuel cell, and enables improving performance of the solid oxide fuel cell battery, and enables improving mechanical strength of solid oxide fuel cell by improving thermal stress durability.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a solid oxide fuel cell manufacturing method. (Drawing includes non-English language text).    Sintering a porous layer ceramic support (S10)    Manufacturing a fuel anode transcription paper (S20)    Forming fuel anode functional layer transcription paper (S30)    Manufacturing and transferring electrolyte transcription paper (S40)    Forming air electrode diffusion stopper transcription paper (S50)    Forming air electrode transcription paper on the air electrode diffusion stopper (S60)
NOVELTY - Manufacturing solid fuel substitute, comprises mixing pine nut shell and rice hull in a weight ratio of 1:0.02-0.3 to obtain a fuel composition, and subjecting the 100 wt.% fuel composition having a moisture content of 0.07-28 wt.% through compression molding under the molding pressure of 360-1130 kgf/cm3 at 19-75 degrees C to obtain solid fuel.    USE - The method is useful for manufacturing solid fuel substitute (claimed).    ADVANTAGE - The substitute has excellent thermal efficiency and adequate combustion time, does not require chemical additives, prevents the generation of harmful gases during combustion, and is environmentally friendly.
NOVELTY - The apparatus (10) has water supply units (42,52) that supplies water to the buoyancy tanks (40,50,60). The hydrogen and oxygen gases generated from generation units (20,30) are stored in the buoyancy tanks through the gas connection pipes (41,51). The generation units are arranged in the gas generation tanks. The water stored within the gas generation tank is electrolyzed to generate the buoyancy.    USE - Buoyancy origination apparatus used in power generator.    ADVANTAGE - The production and annihilation of buoyancy can be facilitated effectively. The discharging time of water from buoyancy tank can be reduced. The generation time of buoyancy can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the buoyancy origination apparatus used in power generator.    Buoyancy origination apparatus (10)    Generation unit (20,30)    Buoyancy tank (40,50,60)    Gas connection pipe (41,51)    Water supply unit (42,52)
NOVELTY - The fuel cell power generation system has devulcanizer (20) that removes the sulfur provided in the fuel gas supplied from gas supply fan (10). An opening/closing valve (70) is provided to open/close the fluid path of the devulcanizer. The sulfur removed fuel gas is transferred to fuel conversion apparatus (30) from the desulfurization turning point, to react with water to produce hydrogen for power generation. A heating source (40) is provided to supply heat for chemical reaction of fuel gas at fuel conversion apparatus.    USE - Fuel cell power generation system.    ADVANTAGE - Since sulfur removed fuel gas is transferred to fuel conversion apparatus to react with water to produce hydrogen for power generation, rate of air and fuel gas supplied to fuel conversion apparatus is maintained effectively. The power generation efficiency of the fuel cell power generation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell power generation system. (Drawing includes non-English language text)    Gas supply fan (10)    Devulcanizer (20)    Fuel conversion apparatus (30)    Heating source (40)    Opening/closing valve (70)
NOVELTY - The system (100) has a gas purification unit (140) that refines the aeration gas generated from the anaerobic tank (120). An electrolyte sub-title refusal (130) removes nitrogen component and processing liquid ejected from anaerobic tank. The anaerobic tank removes ammonia from fire-extinguishing supernatant ejected from digeater (110). The digeater fermenting the organic wastewater electrolyzed to the organic waste water treatment system with high nitrogen content. The ammonia nitrogen and the nitrogen content uses the hypochlorous acid in order to remove the nitrate form nitrogen.    USE - Organic waste water treatment system.    ADVANTAGE - The concentration of the ammonia nitrogen obtained in the methane fermentation processing is reduced using the anaerobic activated sludge process after the nitrogen amount of the methane fermentation is submerged. The removal of the nitrogen component such as the ammonia nitrogen and nitrate form nitrogen can be processed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of organic waste water treatment system. (Drawing includes non-English language text)    Organic waste water treatment system (100)    Digeater (110)    Anaerobic tank (120)    Electrolyte sub-title refusal (130)    Gas purification unit (140)
NOVELTY - Preparing porous metal organic framework comprises dissolving 1-16 group of metal ion and 14-17 group of anion combined with metal salt and organic ligand precursor with organic solvent in mixed solvent of water to form metal-organic framework sieve, immersing the metal-organic framework sieve in a first solvent, processing the metal-organic framework sieve using supercritical carbon dioxide and second solvent, and vacuum drying the metal-organic framework sieve at high temperature.    USE - The method is useful for preparing porous metal organic framework, which is useful in micromolecule absrobent, where the micromolecule is carbon dioxide, methane or hydrogen (all claimed).    ADVANTAGE - The porous metal organic framework has high surface area and synthetic yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for porous metal organic framework having a specific surface area of greater than or equal to 5000 m2/g.
NOVELTY - The system has a temperature sensor (110) which senses the inner temperature of an air supply nozzle (120). A gas-exhaust valve (521) is provided in a fluid pressure gate (631,632) which is connected with a discharge pipe (620). An anaerobic reactor (20) is provided with a drain tank (630) that is provided with a vacuum valve (633). The aerobic reactor (10) and anaerobic reactor are installed in the transfer conveyor (11). The aerotropic reaction material is ejected through the vent (301) of the aerobic reactor to the anaerobic reactor.    USE - Continuous aerobic and anaerobic dry fermentation system used for dissolving organic waste such as food waste, wood, round waste and paper, and used in sewage disposal plant, waste water disposal plant, livestock excretion and stockbreeding farmhouse.    ADVANTAGE - The slaking process of the aerobic reactor and anaerobic reactor can be optimized. The processing speed of the continuous aerobic and anaerobic dry fermentation system can be improved effectively. The organic waste can be dissolved efficiently in the anaerobic reactor. The water control agent can be enhanced. The sealing of the continuous aerobic and anaerobic dry fermentation system can be maintained. The anaerobic digestion reaction can be induced efficiently. The methane can be obtained effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous aerobic and anaerobic dry fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous aerobic and anaerobic dry fermentation system.    Aerobic reactor (10)    Transfer conveyor (11)    Anaerobic reactor (20)    Temperature sensor (110)    Air supply nozzle (120)    Vent (301)    Gas-exhaust valve (521)    Discharge pipe (620)    Drain tank (630)    Fluid pressure gates (631,632)    Vacuum valve (633)
NOVELTY - Sludge decreasing method involves diluting complex microorganism solution using water, adding oxygen and molasses, cultivating the microorganisms, injecting the resultant cultivated complex microorganisms and sludge into a mixer, stirring, feeding the resultant mixture of cultivated complex microorganisms and sludge into a storage tank, separate reservoir or digestion tank, reducing sludge by stirring, maintaining the storage tank, separate reservoir or digestion tank at constant temperature, and supplying oxygen for promoting the metabolism of the complex microorganisms.    USE - Sludge decreasing method (claimed).    ADVANTAGE - The sludge decreasing method is economically carried out, by a simple process.    DETAILED DESCRIPTION - Sludge decreasing method involves diluting complex microorganism solution using water, adding oxygen and molasses in the obtained diluted complex microorganisms, cultivating the complex microorganisms by controlling temperature, uniformly stirring for preventing sedimentation, injecting the resultant cultivated complex microorganisms and sludge into a mixer, uniformly stirring, obtaining mixture of cultivated complex microorganisms and sludge, feeding the obtained mixture of cultivated complex microorganisms and sludge into a storage tank, separate reservoir or digestion tank, reducing sludge by stirring, maintaining the storage tank, separate reservoir or digestion tank at constant temperature, and supplying oxygen for promoting the metabolism of the complex microorganisms. An INDEPENDENT CLAIM is included for apparatus for sludge decreasing method.
NOVELTY - Lignocellulosic plant biomass is pretreated in fractionation process (I) to dissolve and recover hemicellulose to obtain a hemicellulose fraction. The remaining solids are treated with an ionic liquid and an anti-solvent for cellulose in fractionation process (II) to recover lignin fraction and cellulose fraction.    USE - Fractionation of lignocellulosic plant biomass e.g. plant-derived material, such as wood, woodchips, grass, sugarcane, bagasse, bamboo, and corn stover, into hemicellulose fraction (all claimed) used as feedstock for production of value-added products which may replace fuels and chemicals produced from fossil carbon resources.    ADVANTAGE - The method prevents degradation of hemicellulose. The native structure of lignin is preserved by preventing unwanted reactions, such as condensation reactions between various phenolic units in lignin. The ionic liquid can be recycled by cleaning using acid neutralization or melt crystallization.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the fractionation method of lignocellulosic plant biomass.
NOVELTY - Air conditioner refrigerant comprises 15-30 pts. wt. 1,2-difluoroethane, 20-40 pts. wt. 1,1,2-trifluoroethane, 10-30 pts. wt. 1,1,2,2-tetrafluoroethane, 5-30 pts. wt. vinylidene fluoride and 10 pts. wt. propane.    USE - Air conditioner refrigerant.    ADVANTAGE - The refrigerant has zero ozone depletion potential (ODP).
NOVELTY - Continuous fermentation method for producing lactic acid, involves adding substrate to reactor that contains lactic acid bacteria, mixing the substrate and lactic acid bacteria, granulating mixture, and fermenting granulated material using fermentation bacteria to obtain lactic acid.    USE - Continuous fermentation method for producing lactic acid (claimed).    ADVANTAGE - The method exhibits lactic acid production rate of 22-30 g/l/hour and substrate conversion rate of 80%, is cost-effective, and provides high yield.
NOVELTY - Method for recycling animal wastes, involves injecting cell membrane containing insoluble protein, and animal waste into ion decomposition apparatus, performing ion decomposition of insoluble protein into water-soluble organic acid, producing sterilized ion decomposition organic substance e.g. that comprises mixture of solid oil substance, animal waste, organic acid solution, and oil, and ejecting ion decomposed organic substance from a state of high temperature and high pressure to a normal temperature atmosphere.    USE - The method is useful for recycling animal wastes (claimed).    ADVANTAGE - The method removes pathogen by ion disintegrating animal waste, prevents generation of bad smell, and rapidly performs animal waste recycling process.    DETAILED DESCRIPTION - Method for recycling animal wastes, involves injecting cell membrane containing insoluble protein, and animal waste formed with cells containing water and oil into an ion decomposition apparatus, performing ion decomposition of insoluble protein into water-soluble organic acid including formic acid, acetic acid and lactic acid by raising ion concentration of cell sap by making the animal waste into a state of high pressure and high temperature, producing sterilized ion decomposition organic substance that comprises mixture of solid oil substance, animal waste, organic acid solution, and oil, and ejecting ion decomposed organic substance from a state of high temperature and high pressure to a normal temperature atmosphere. An INDEPENDENT CLAIM is included for animal waste recycling apparatus, which has an injection unit for injecting the animal waste to a high pressure heating container, where the high pressure heating container performs ion decomposition of organic substance, and an ion decomposition apparatus that decomposes animal waste under high pressure and high temperature and enhances ion concentration of water.
NOVELTY - The purifier has a bio-gas dissolution unit (200) that is connected with a pressure pump (300), to dissolve biogas flowed in from a bio-gas holder (100) with the water applied from outside. A safety valve (421) is installed in a communications path (420), to control the exhaustion of the gas through exhaust passage. The communications path is installed in the upper portion of segregation portion (400). A spraying device is installed in the lower portion of segregation portion. The material for removing carbon dioxide, is lime water or sodium hydroxide aqueous solution.    USE - Bio-gas purifier installed in sewage disposal plant.    ADVANTAGE - The extraction efficiency of the methane gas can be maximized. The purifying capacity of the purifier can be improved. The simple structure of the purifier can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-gas purifier.    Bio-gas holder (100)    Bio-gas dissolution unit (200)    Pressure pump (300)    Segregation portion (400)    Communications path (420)    Safety valve (421)
NOVELTY - Producing methane gas comprises separating a carbon monoxide gas stream within a blast furnace gas stream ejected from a carbon monoxide separator of a steel blast furnace gas, producing a hydrogen gas/carbon dioxide gas stream including hydrogen gas and carbon dioxide gas in a water gas shift reactor using carbon monoxide gas within the carbon monoxide gas stream, and producing the methane gas stream by a methanation process using hydrogen gas within the hydrogen gas/carbon dioxide gas stream and the carbon monoxide within the carbon monoxide gas stream.    USE - The method is useful for producing a methane gas (claimed).    ADVANTAGE - The method is capable of simply and easily producing the methane gas with high quality in an energy-effective manner and reducing the generation of the pollution problem.
NOVELTY - Preparation of jolkinolide B involves pulverizing Morinda officinalis root, sieving through 40-60 meshes, adding in extraction kettle, extracting ethanol aqueous solution with concentration of 75 volume% as entrainer using supercritical carbon dioxide extraction, collecting extraction liquid, recycling the ethanol with heptane, then providing heptane-ethyl acetate-acetonitrile-water using high-speed counter-current chromatography separation solvent system and drying.    USE - Preparation of jolkinolide B (claimed).    ADVANTAGE - The jolkinolide B is efficiently prepared with high yield without polluting the environment.
NOVELTY - Recovery unit of a system for hydrogen isotopic mass-spectrometric analysis of water and organic oxygen-containing compounds, made in form of a pipe furnace, solid-electrolyte electrochemical oxygen-conducting cell, placed coaxially in the pipe furnace and having a solid-electrolyte ceramic pipe with current leads, working electrodes deposited in form of films on its inner and outer sides, and a comparison electrode lying on the outer side of the solid-electrolyte pipe with a gap from the outer working electrode, and a control and information processing unit which is electrically connected to electrodes of the cell, electrically connected through current leads to electrodes of the cell; the cell is provided with an additional catalyst in form of platinum wire placed in the ceramic pipe with possibility of mechanical contact with the working electrode on its entire length and twisted at the ends, and units for connecting the cell with the system, which are made in form of metal housings with through-holes in which spacers and fixing screws are used to mount a capillary for feeding the sample on one side and the ceramic pipe of the cell on the other side. The twisted wire ends are placed in holes of the housings of the unit and are in contact with walls thereof.    USE - Chemistry.    ADVANTAGE - High reliability of the obtained isotope data owing to full control of the processes of decomposition of water molecules and organic oxygen-containing molecules in order to obtain hydrogen using a minimum analysed sample. 2 cl, 1 tbl, 2 dwg
NOVELTY - The system has up-flow septic tank (UST) reaction bath (200) for denitrifying the transferred nitrate with the sludge precipitated by a nitrobgacter. A water storage tank (500) separates the solid from liquid hydrolyzed at an acid formation tank (400). A methane gas generating bath (600) generates the methane gas from the effluent separated from the liquid in the water storage tank. A settling tank (700) ejects the sludge and the processing water from the aerated filter (AF) reaction bath (300).    USE - System for separating organic material and recovering biogas from foul water such as sewage, livestock waste water, agricultural effluent and industry wastewater.    ADVANTAGE - The removal of the phosphorus and ammoniac nitrogen can be enhanced effectively. The operation efficiency of the system can be improved. The generation rate of high-quality sludge can be increased. The cost reduction effect of the system can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for separating organic material and recovering biogas.    UST reaction bath (200)    AF reaction bath (300)    Acid formation tank (400)    Water storage tank (500)    Methane gas generating bath (600)    Settling tank (700)
NOVELTY - Manufacture of biodiesel involves mixing methanol and alkali catalyst with vegetable oil and treating ultrasonically.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel.
NOVELTY - A catalyst comprises 85-97 wt.% nickel oxide-alumina solid carrier and 3-15 wt.% sulfate ion. The molar ratio of nickel and aluminum is 0.1-1.    USE - Catalyst is used for manufacturing butane (claimed).    ADVANTAGE - The butane is efficiently manufactured using the catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst; and    (2) manufacture of butene.
NOVELTY - Invention relates to a method of producing liquid synthetic hydrocarbons from hydrocarbon gases, involving purification of starting material from sulphur compounds, steam-carbon dioxide catalytic conversion of the starting material purified from sulphur compounds at temperature of 950-1050 degrees C to obtain synthesis gas by supplying high-grade heat to the catalytic reactor and feeding into said reactor carbon dioxide separated from exhaust flue gases, and water vapour which is generated in a steam boiler which is heated by hot synthesis gas, subsequent catalytic processing of the synthesis gas via a Fischer-Tropsch technique, separating a mixture of liquid hydrocarbons from products obtained from synthesis gas processing and subsequent separation of the mixture into fractions of commercial grade hydrocarbons. The method is characterised by that at the outlet of the steam boiler, synthesis gas is divided into two streams, one of which is fed for catalytic processing in a Fischer-Tropsch synthesis reactor and the second stream is fed into a hydrogen production unit in which steam conversion of carbon oxide, separation of water and absorption of carbon dioxide are successively carried out, after which the purified hydrogen is fed into a desulphurisation unit for hydrogenation of organic sulphur compounds contained in the starting material and carbon dioxide separated during regeneration of the absorbent is mixed with the stream of carbon dioxide separated from flue gases and then fed into the catalytic reactor for steam-carbon dioxide conversion of the starting material.    USE - Chemistry.    ADVANTAGE - Method is independent of external hydrogen sources needed to carry out desulphurisation. 3 cl, 2 dwg
NOVELTY - The structure has a stack main portion that is connected in parallel manner and is provided with the stack valves (21,22). A unit cell powers the hydrogen generated by the first stack portion to the preset stack portion. A control unit supplies the respective water and current through the first stack valve based on the ON/OFF control of the first stacked switch (31), so that central valve (20) and central switch (30) operates the production of oxygen and hydrogen with the control unit.    USE - Structure of high capacity water electrolysis stack.    ADVANTAGE - The production capacity of the hydrogen can be improved through the water electrolysis. The power consumption of the stack structure due to the generated bubble can be reduced so as to produce the peak efficiency according to the load of the water electrolysis. The efficiency and convenient operation of the stack structure can be improved. The repair of the corresponding stack due to malfunction can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic views of the structure of high capacity water electrolysis stack.(Drawing includes non-English language text)    Central valve (20)    Stack valves (21,22)    Central switch (30)    Stacked switches (31,32)
NOVELTY - This utility model claims a kind of natural source multi-integrated life support system, a water processing unit, salt unit, a steam turbine generator, a condensing water processing unit, a solar light guide unit, a fresh water recycling treatment unit, a sewage processing unit, animal and plant waste recycling processing unit, internal combustion motor such as unit link, and generating the function comprises power supply for supplying purified water, light and so on. The utility model is uncovering the almost completely self-sufficient and does not need other external energy system, the living environment in the system can reach the range without public hazard, no toxin, and each unit can be full-automatic operation or semiautomatic operation, reduce the labour about 80%, so the cell can be completely self-sufficient, greatly reduce the material transportation cost and the environment protection problem the culture technology and natural and harmonious symbiotic ideal domestic boundary, especially with utility.
NOVELTY - This utility model claims a kind of livestock and poultry corpse harmless treatment and organic fertilizer manufacturing machine, comprising a crushing device and a stirring fermentation device, wherein the stirring device comprises a stirring yeast fermentation box, the stirring and fermenting box body is provided with a feeding port, a crushing device is connected with a material conveyer, a material output port of the material conveyer is connected with the feed port on the sealing with a material conveying pipe, a material conveying pipe and the stirring and fermenting box. The advantages can be realized in livestock and poultry corpse crushing and organic fertilizer manufacturing of integrated sealing process in the machine, avoids the pollution to the environment, at the same time, stirring and fermenting device adopts electric heating PLC full computer control, realizes the full automatic control, and it is safe and reliable.
NOVELTY - The utility model claims a kind of organic fertilizer production device system, comprising a granulator, wherein the granulator is a centrifugal pelletizer, wherein before granulating and separately connected with semi-wet material crusher, granulator. Compared with the existing technology, this utility model adopts semi-wet material to centrifugal granulation, granulating process does not generate dust pollution, the product has good homogeneity, a circular, large hardness, and is suitable for industrial production, storage and transportation.
NOVELTY - The utility model claims a crushing device, comprising a machine frame, a cylinder, a power source, a driving device, a cylinder body, a power source, a driving device arranged on the machine frame, the rotating shaft is provided with multiple rows of staggered crushing cutter, capable of adequately performing a crushing treatment of straw or dairy manure and so on food mixture, the machine frame is provided with a wheel and a handrail, which is good for machinery to move freely. This utility model is designed, fully grinding for a treatment of straw or dairy manure and so on food mixture, saving the culture medium for future and so on, and it is convenient to move, saves the labour and improves the efficiency.
NOVELTY - The utility model claims a kind of low carbon environment-friendly compressed form precise quantitative fertilizer production system, said production system comprises a raw material storage tank, a main spiral conveyer, spiral conveyor, a pressure forming machine, a finished product conveying belt, a finished product bin and a metering packing machine, the primary outlet spiral conveyer is connected with the main conveying belt of the main spiral conveyer at the lower end of the discharging port is connected with the feeding end of the spiral conveyor, the lower part of discharging port of the spiral conveyer is connected with a pressure forming machine of finished product conveying belt one end of the discharge hole of the pressure forming machine, and the other end is connected with the finished product storehouse, the finished product cabin conveyer belt connected to measuring and packaging. The system does not need coal and steam in the whole production process of the fertilizer, there is no waste water discharge, low dust, low noise, low cost, and even the fertilizer appearance shape and size, and small error.
NOVELTY - This utility model belonging to the technical field of fertilizer, specifically to a degradable bag fertilizer, the degradable fertilizer bag, comprising a bag body and degrade the fertilizer in the bag body, wherein the degradable bag body comprises an inner layer and an outer layer, the inner layer and the outer layer is provided with a retention layer. This utility model only watering water when using the water retention agent can be fully saturated, and then the utility model is directly buried in the soil, even 3-4 months without rainfall, irrigation, fertilization, fertilizer plant can ensure need of nutrient, water retention agent in the water plant can ensure need of water, the utility model solves the problem that the conventional irrigation and fertilizer caused by labour, avoids the environment pollution caused by rainwater utilization rate of fertilizer is low, at the same time, this utility model is featured with simple structure, convenient use, low cost and degradable bag body will naturally degrade in a certain period, it will not cause pollution to the environment.
NOVELTY - The utility model claims a biomass gasification reactor of new device, two-section oxygen-enriched steam biomass gasification reactor is composed of a gasification furnace and a chiller, which is connected with the connecting pipe. The gasification furnace, comprising an upper section and a lower section, the upper section is a material dispersing section, the lower section is the pyrolysis reaction section, the section of the middle part is provided with a fish-like the material hoisting device, the fish-like the material is a lower part of the semi-sphere, a bracket is fixed on a central axis of the gasification furnace is provided with a combustion gas on the fish the distributor side wall. A chiller, comprising laser cooling gas cooling section, a heat exchanger cooling section and a slag discharging system, laser cooling gas cooling section at the lower part of the chiller and the bottom is provided with the slag discharging system, the side wall are respectively provided with a generator cooling air inlet and water inlet, heat exchanger cooling section located on the upper part of the chiller is equipped with heat exchanger. Biomass gasification reactor of the utility model can efficiently improve the gas heat value, and generate the tar content in gas, which is mainly used to generate H2 and CO purifying process, which can be used for F-T synthesis process to generate gasoline and diesel oil, the utility model is also suitable for rural areas, forest region, it can carry out centralized processing of waste of crops, so as to avoid environment pollution and prevent the fire and improves the living quality of the farmers.
NOVELTY - This utility model claims a kind of is provided with easy to form the shape of the formed carbon and high temperature carbon product. The utility model is formed with carbon comprises carbonizing biomass raw material is formed by at least a reserved produced by decomposing wood tar and carbon particles of carbon product, the carbon product compression is set to form carbon with various shapes, by making the shaped charcoal to form is provided with a variety of shapes and high quality of product by a secondary high temperature carbonizing.
NOVELTY - Organic fertilizer comprises 10% manure, 19.7% edible fungi residues, 10% chicken manure, 20% corn straw powder and 0.3% effective microorganism (Em) stock solution.    USE - As organic fertilizer used in poultry (claimed).    ADVANTAGE - The fertilizer is low in cost and high in yield; and improves crop quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer, involving: putting organic fertilizer comprising manure, pig manure, chicken manure, edible fungi slag, corn straw powder, and Em primary liquid into the mixer according to the proportion, mixing and stirring uniformly, controlling temperature at greater than or equal to 15 degrees C in shallow type fermentation tank, fermenting organic fertilizer at environment temperature, controlling organic matter content of 40-60%, carbon nitrogen ratio is 30:1 to 35:1, water content is 50-65%, at temperature of 55-75 degrees C, maintaining for 5 days, the fermentation time is 8 days, deodorizing, sterilizing, removing the water, and obtaining produced organic fertilizer, mixing uniformly stirred material into the fermenting tank, fermenting the material, carrying out continuous aerobic fermentation by natural ventilation and turning the material in contact with the air providing the oxygen, where the fermentation cycle is 8 days, continuously throwing and scattering, ferment the material, decomposing the material after 8 days of continuous fermentation, organic fertilizer fermentation environment temperature is controlled at 15 degrees C, livestock manure organic fertilizer semi-finished product water content is controlled at 50%, the thickness is 1.3, decomposing the material volume reduction not less than 30%, water content is 25%, nitrogen is less than 20:1, the pH value is 6-8, the temperature is reduced to less than 30 degrees C, and the oxygen consumption speed is stable.
NOVELTY - Manufacturing biological fermentation composting raw materials, involves: taking raw materials e.g. chicken manure, sheep manure, cattle manure, pig manure, and domestic garbage, straw, rice bran, wheat bran powder; (2) fermenting the raw materials by stacking method; and (3) performing biological fermentation compost anaerobic fermentation to form high-efficiency biological fermentation compost.    USE - For production of biological ferment compost (claimed).    ADVANTAGE - The method controls environment pollution; improve land production; is capable of changing traditional agricultural production; has wide application range; and is economical and practical.    DETAILED DESCRIPTION - Manufacturing biological fermentation composting raw materials, involves: (1) taking raw material such as chicken manure, sheep manure, cattle manure, pig manure, and domestic garbage, straw, rice bran, wheat bran powder, etc; 5 wt.% humic acid and calcium content, adjusting pH value; deodorizing maturing agent and 0.02 wt.% raw materials; 1:700 to 1:1000 microbial agent; 1:700 to 1:1000 brown sugar; 100 times water; 0.005% boron, 10-14% iron, 12-16% manganese, 18% zinc, 8-12% phosphorus, 20-24% copper; nourishing; (2) fermenting the raw materials by stacking method; and (3) performing biological fermentation compost anaerobic fermentation to form high-efficiency biological fermentation compost.
NOVELTY - A kind of improved structure of biomass gasification furnace, comprising a biomass gasification furnace of biomass gasification furnace feeding method is closed the spiral feeding way, at the same time, increasing the positive pressure air inlet, that is to say, a small part of the gas of the fan into a feeding screw, a material intake air pressure to seal the feed intake air circuit is divided into a main channel and a branch, the main air flow path still enter into gasification furnace combustion reaction chamber, an air inlet branch connected with the storage hopper, an air inlet branch and the connection to the lower end of the centrifugal separation chamber, the air outlet of the position adjusting to the upper end of the pre-heating chamber from the combustion reaction chamber and provided with a valve air flow branch, it is convenient to control, increasing the screen position of the pre-heating room air outlet pipe, this utility model has good sealing effect, high utilization rate, an air path is smooth, gas furnace stroke.
NOVELTY - This utility model claims a biomass fuel block of continuous production system according to claims, wherein the production system comprises a system, the raw material crushing system, a raw material drying system, a pressing block forming system, fuel system cooling and drying and weighing and packaging system, wherein the system comprises a grabbing device and transporting device, wherein the raw material crushing system comprises a cutter machine, the crusher and the hammer machine, the raw material drying system is composed of a hot-blast stove, a rotary drum dryer, a draught fan, a cyclone dust collector, and the said pressing block forming system is composed of a high inclination-angle belt conveyor, a spiral conveying material, a platform, a 4-6 machine, and the cooling and drying of the molding fuel system is composed of a belt conveyer and a net chain cooling air, the utility model realizes the biomass fuel block of continuous production, to provide an important way for efficient use. The agriculture and forestry waste biomass fuel block, that is, treats the environment pollution and the agricultural production.
NOVELTY - This utility model claims a kind of engine carbon deposit cleaning double-connected automatic labelling machine of packing pot machine, the utility model is the condenser inlet and outlet of the electrolytic tank is connected with the inlet of the first gas-water separator of condenser, a lower part of the gas-water separator and a gas-water separator communicated with the lower part of the first gas outlet of the gas-water separator and a gas-water separator of gas inlet is connected with the solution outlet of the second gas-water separator with an electrolyte inlet of the electrolytic cell is connected with the pipeline, wherein the pipeline is a gas-water separator and electrolytic bath is provided with a circulating pump, a gas outlet of the second gas-water separator is connected with the lower part of the water tank through the pipeline fire arrestor is connected, the utility model in order to avoid engine in engine detonation or water removing carbon during the process, hydrogen and oxygen in the preparing process of strictly controlling the liquid level of the electrolyte, a liquid level, the content of water in the hydrogen oxygen, air supply, and the whole process is automatically finished.
NOVELTY - A kind of hydrogen fuel engine system, comprising a water electrolysis device (1), a hydrogen fuel engine (2) and a water tank (3), the water electrolysis device (1) comprises a hydrogen ionization chamber (5) and an oxygen ionization chamber (6), the water tank (3) water inlet is connected with the hydrogen ionization chamber (5) and an oxygen ionization chamber (6) is connected with the water inlet of the bottom and gas ionization chamber (5) and an oxygen ionization chamber (6) is a hydrogen outlet and oxygen outlet connected with the hydrogen-oxygen mixed gas storage tank (7) is connected with the air inlet, a gas storage tank (7) and the hydrogen fuel engine (2). This utility model is a raw material water, the ionized from the hydrogen and oxygen and is pressurized by combined into the engine combustion chamber by electrolytic water, which can solve the problem of hydrogen storage, transportation and station facility construction is not complete and energy recycling, exhaust pipe dropping water and so on.
NOVELTY - A kind of new-type biomass particle machine, comprising a machine frame with cross beam bracket and one side of the gear engaged with the gear teeth of the gear is provided with a groove, the gear two is equipped with a semi-shaft. This utility model is for producing granular efficiency is high, energy consumption is low and the cost is low; a stable, the structure is simple and the operation is convenient.
NOVELTY - Anti-staling agent comprises Chinese herbal medicine including 8-12 wt.% of galangal, 2-8 wt.% of radix stemonae, 5-10 wt.% of Encalyptus robusta, 3-8 wt.% of Saxifraga stolonifera, 5-10 wt.% of honeysuckle, 8-12 wt.% of berberine, 2-5 wt.% of Astragalus mongholicus, 2-8 wt.% of garlic, 3-10 wt.% of konjaku flour, 1-5 wt.% of agar, 1-5 wt.% of lecithin, 10-15 wt.% of starch and 50-80 wt.% of water.    USE - Used as an anti-staling agent.    ADVANTAGE - The anti-staling agent can be simply and economically prepared in an eco-friendly manner with good preservative effect and prolonged service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing anti-staling agent comprising (1) adding galangal, radix stemonae,Encalyptus robusta, Saxifraga stolonifera, honeysuckle, berberine, Astragalus mongholicus and garlic with water and ethanol in a container and then mixing and heating at a temperature of 200-350 degrees C and pressure of 20-100 MPa for 10-30 minutes, cooling the mixture at normal temperature and pressure, taking out the active ingredient and then drying at 20 degrees C, (2) pasting the corn starch or potato starch in a pasting machine and then gelatinizing at 98-180 degrees C, drying, and crushing to prepare gelatinized starch, and (3) adding konjaku flour, agar, and lecithin in a container and then mixing and stirring for 15-30 minutes.
NOVELTY - Producing bio-organic fertilizer involves diluting fresh sheep excrement in water for 48 hours stirring; diluting the fecal sewage with water at 50 degrees C and further extruding the obtained solid part after drying and crushing, mixing compound bacterial agent and stirring uniformly, pressing out excess air at 20-27 degrees C; performing anaerobic ferment to obtain fermentation product; performing aeration treatment for 12 hours; adding plant ash, adjusting the water content, adding effective microorganism and mixing; and performing anaerobic fermenting for 10-15 days to form bio-organic fertilizer.    USE - For producing bio-organic fertilizer (claimed).    ADVANTAGE - The method utilizes fresh sheep excrement which is more reasonable and high quality of the product; prepares fertilizer that provides less bad on crop; and does not cause waste.    DETAILED DESCRIPTION - Producing bio-organic fertilizer involves diluting fresh sheep excrement in water for 48 hours, where harmful substance and difficult smelling the odor is dissolved in water; fully stirring; filtering the impurity; removing lower layer sand particle; diluting the fecal sewage with water at 50 degrees C and further extruding the obtained solid part after drying and crushing, mixing compound bacterial agent and stirring uniformly, pressing out excess air at 20-27 degrees C; performing anaerobic ferment for 5 to 10 days to obtain fermentation product i.e. biological ferment feed raw material, such as a vacuum bag; performing aeration treatment for 12 hours; adding plant ash, adjusting the water content, adding effective microorganism and adequately mixing microbial inoculum; and performing anaerobic fermenting for 10-15 days to form bio-organic fertilizer.
NOVELTY - A biological organic fertilizer comprises 7-8 pts. wt. livestock manure, 0.5-1 pts. wt. brown sugar, 0.5-1 pts. wt. Bacillus subtilis, and 1-2 pts. wt. fermented product.    USE - As biological organic fertilizer (claimed).    ADVANTAGE - The fertilizer is efficient, environment-friendly, green, and use of water without pollution; does not create residue; has no toxic and side effect; improves the utilization rate of the nitrogen, phosphorus and potassium; and reduces the damage to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing aquiculture biologic organic fertilizer, involving mixing the 7-8 pts. wt. livestock manure, 0.5-1 pts. wt. brown sugar, 0.5-1 pts. wt. Bacillus subtilis, and 1-2 pts. wt. fermented product, and then stacking fermentation at 55-60 degrees C for 2-3 times to obtain the product.
NOVELTY - Composite microorganism bacterial fertilizer, comprises a widowed male microbial fertilizer and Pythium fungi (Trichoderma harzianum), where the widowed male Pythium and Trichoderma spores has ratio 1:4 to 1:2.    USE - In preventing and treating strawberry yellow leaf disease or strawberry root rot disease (claimed).    ADVANTAGE - The composition increase crop nutrition, is convenient to use, saves work, production efficiency, and has very obvious preventing and treating effect of strawberry disease.
NOVELTY - Multipurpose earthworm biological organic garbage processor, comprises a machine body (1) with a feeding port (5), where left and right two ends of the shaft is connected with the machine body from the ground to the bracket (2), a machine body is set on the side wall of the opening from inside to outside and mesh screen (3) is connected with the machine body, and a detachable sealed baffle plate is further equipped with a ventilating natural ventilation system.    USE - As multipurpose earthworm biological organic garbage processor (claimed) used for fermenting domestic garbage and feeding earthworm.    ADVANTAGE - The multipurpose earthworm biological organic garbage processor is rational in structure and design, has simple and convenient operation, and changes household garbage waste into earthworm biological multifunctional material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a multipurpose earthworm biological organic garbage processor.    Machine body (1)    Fixing bracket (2)    Mesh screen (3)    Push-pull type sealing clapboard (4)    Feeding port (5)    Air exchange hole (6)    Pipeline (8)
NOVELTY - A micro fertilizer comprises following raw materials: 5-10 parts by weight (pts. wt.) amino-group state selenium and/or amino-group state zinc, 40-50 pts. wt. water soluble carbon source and nitrogen source, and 40-50 pts.wt. Bacillus subtilis and vesicular-arbuscular (VA) mycorrhizal fungi mixed bacteria liquid, where the weight ratio of the carbon and nitrogen (C:N) source is 15-20:0.5-1.2, and ratio of the Bacillus subtilis and VA mycorrhizal fungi is 1:0.8-1.2.    USE - As micro fertilizer for improving black tea plant quality (claimed).    ADVANTAGE - The micro fertilizer has high efficiency; provides healthy and strong growth of black tea plant; and also strengths photosynthetic efficiency of the black tea plant.    DETAILED DESCRIPTION - A micro fertilizer for improving black tea plant quality comprises following raw materials: 5-10 parts by weight (pts. wt.) amino-group state selenium and/or amino-group state zinc, 40-50 pts. wt. water soluble carbon source and nitrogen source, and 40-50 pts.wt. Bacillus subtilis and vesicular-arbuscular (VA) mycorrhizal fungi mixed bacteria liquid, where the weight ratio of the carbon and nitrogen (C:N) source is 15-20:0.5-1.2, and ratio of the Bacillus subtilis and VA mycorrhizal fungi is 1:0.8-1.2. The amino-group state selenium is selenium cystine, selenomethionine or selenium-methionine. An INDEPENDENT CLAIM is included for preparation of the micro fertilizer involving mixing the each of the above raw material, setting in the reactor under oxygen condition at 30-35 degrees C, mixing and stirring, fully contacting air environment, and fermenting for 10-15 days to obtain fertilizer mother liquor.
NOVELTY - Liquid fertilizer comprises 1.8-2 wt.%, preferably 2 wt.% sorghum straw, 1-1.2 wt.%, preferably 1 wt.% brown sugar, 5-6 wt.%, preferably 6 wt.% ammonium sulfate, 2.5-3 wt.%, preferably 2.5 wt.% zinc sulfate, 2.5-3 wt.%, preferably 3 wt.% potassium dihydrogen phosphate, 2.5-3 wt.%, preferably 2.5 wt.% magnesium sulfate, 2.5-3 wt.%, preferably 3 wt.% boric acid, 1.5-2 wt.%, preferably 1.5 wt.% ammonium molybdate, 2-2.5 wt.%, preferably 2.5 wt.% composite enzyme and rest water.    USE - For backlight source illuminant of liquid fertilizer (claimed).    ADVANTAGE - The liquid fertilizer provides strong root and stem, flower fruit preservation, coloring, improves the yield and improve the quality and composite function, has strong immunity and control ability of various plant diseases and insect pests.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparing backlight source illuminant of liquid fertilizer involving sorghum stalk after fermentation to obtain fermentation liquid, using water to dilute to 6-8 baume degree, crop and soil spraying to the plant crop in the ditch, where the spraying amount is 90-110 t/hm2, and spraying the second antenna cover film, and the plant of the exposed soil surface which is spraying before sprout; and    (2) preparation of liquid fertilizer involving: adding 1.8-2 wt.% sorghum straw, to water, and 1-1.2 wt.% brown sugar, 5-6 wt.% ammonium sulfate, 2.5-3 wt.% zinc sulfate, 2.5-3 wt.% potassium dihydrogen phosphate, 2.5-3 wt.% magnesium sulfate, 2.5-3 wt.% boric acid, 1.5-2 wt.% ammonium molybdate and 2-2.5 wt.% composite enzyme, at 2-100 wt.% at normal temperature and fermenting for 15-18 days, then filtering the solid.
NOVELTY - A ploughing-free composite microorganism fertilizer, comprises 10-25 per tons polyacrylamide, 10-30 per tons Bacillus subtilis, 5-25 per tons Bacillus laterosporus, 5-20 per tons diethyl aminoethyl hexanoate, 1-4 per tons polyaspartic acid, 20-50 per tons ethylene diaminetetraacetic acid (EDTA), 10-30 per tons urea, 5-20 per tons potassium fulvate, and rest is organic filler.    USE - As ploughing-free composite microorganism fertilizer (claimed) used in crop planting.    ADVANTAGE - The ploughing composite microorganism fertilizer has high microbial activity, strong stability, can effectively improve the soil granule structure, remove the hardening of the soil, enhances soil infiltration capacity, promote the growth of beneficial microorganisms in the soil, improves the utilization rate of the fertilizer, promote root growth, resist root crop disease, and has obvious effect.
NOVELTY - Tail gas recycling system of melamine production device comprises a melamine production device and urea production device. A tail gas outlet of the melamine production device is connected with a medium-pressure recycling system of the urea production device by an ejector.    USE - Used as a tail gas recycling system of melamine production device.    ADVANTAGE - The device: has simple structure and reduces processing steps; is easy to operate, energy saving, safe and reliable, economical and environmentally friendly; and improves the conversion rate in urea synthesis, produces high yield, reduces raw material consumption and solves water balance disorder in the urea system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the tail gas recycling system of melamine production device (Drawing includes non-English language text).
NOVELTY - This utility model belongs to the field of new energy field, specifically is a kind of external heat type rice hull continuous carbonization device, comprising a feeding device, a destructive distillation furnace, a dust remover, a primary tar filter, a condenser, a secondary tar filter, a desulfurizer, a blower, an air storage tank, a liquor storage tank, a carbon tank and a carbon recycling device, wherein the dry distillation furnace through the gas pipeline dust remover are orderly connected in series, a primary tar filter, a condenser, a secondary tar filter, a desulfurizer, a blower, an air storage tank, wherein the condenser is connected with the liquid pipe and the liquor storage tank, the dry distillation furnace is a feeding output end of lower part, the lower end is connected with a carbon tank, the input end of the carbon recycling device is connected with the carbon tank. This utility model gas product and recovery can supply a resident user, liquid product recovery can be wood vinegar and wood tar production raw material, solid carbon recovery and can be used as active carbon and white carbon black production raw material, energy-saving and environment-friendly, does not pollute the environment.
NOVELTY - A kind of new biomass gasification machine, comprising a filtering water tank, a gasification furnace, a desulfurizer, a high-pressure water pump, atomizing separator, dehydrator and odour removing chamber, wherein the air outlet of the gasification furnace through the gas-guide tube is connected with a filtering tank, a filtering water tank is connected on the air inlet of the desulfurizer through multi-stage cooling pipe, the high pressure water pump is connected with the air inlet and the water outlet is connected with the water tank, the upper part is connected with the separator, the atomizing air inlet and the atomization separator dehydrating device, the air outlet is connected to the odour removing chamber. This utility model is continuous work by not providing a lot of hot water energy, for the user for heating and bathing, it not only saves energy, but also is convenient to use. And will not be blocked pipe;
NOVELTY - This utility model claims a boiling type biomass gasification system, comprising a feeding device, a fluidized bed type biomass gasification furnace, the lower is the boiling type biomass gasification furnace comprises a reaction section and tail ash section, the reaction section and tail ash section, the reaction section and tail ash and section is provided with a fire grate, wherein the reaction section is a cylinder vertically arranged, the side part of the reaction section is provided with a feeding port, the feeding port is located in the middle of the reaction section, the reaction section of the top seal, the upper part of the side is provided with a fuel gas outlet, the tail ash is conical hopper-shaped, is located at the lower part of the reaction section, the bottom of the section is provided with a tail ash outlet, the side part of the tail ash. is provided with an air inlet, the air inlet is connected with an air inlet pipeline. Relative to the fluidized bed, the utility model is a gasification furnace, gas flow rate, gas carrying a solid material, so as to make the gas containing little ash content, because the gasification medium through the air inlet, and the air inlet is located at the side part of the tail ash section, it can smooth the deslagging. Relative to fixed bed and said short because of the utility new-type gasification furnace for pyrolysis and gasification of garbage fuel time, so fuel gas tar content is low, so as to prevent tar, blocked pipeline.
NOVELTY - This utility model claims a vertical biomass gasification furnace air inlet device, a combustion fuel layer on the bottom layer, the air inlet device is divided into two layers, the first ignition by the ignition device to form the high and low burning layer, a burning layer is a layer to generate carbon dioxide, high combustion layer for reducing layer, the carbon dioxide and the carbon contact for reducing layer glowing reduction reaction to generate combustible gas carbon monoxide. A discharge pipe (3) vertically, the hearth (2) is a feeding port (4) is uniformly distributed outlet pipe (3) is divided into longer short wind pipe and the air outlet pipe, and a longer air tube and a short air outlet tube are adjacent to each other, the utility model is biomass gasification furnace gasification and, through longer short wind pipe and the air outlet pipe are adjacent to each other are distributed to realize wind and wind pressure uniform in the hearth to make the two layers of combustion, combustion uniformly, so as to control the temperature of the hearth is between 600 degrees and 650 degrees, designing the drain pipe and a drain valve is connected with the waste outlet opening, which is good for preventing air channel.
NOVELTY - This utility model claims a bulk garbage combustible and straw through continuous pyrolysis and gasification device, comprising a vent hole set on the upper part of the furnace body is furnace base, furnace body supporting leg of the furnace body, the bottom of the furnace body is set on the ventilating grate, ash tray, ash disc transmission system, and fan, wherein the furnace body is a furnace body is integrated with the lower furnace body device of the middle furnace body is integrated with the furnace body middle section of the upper furnace body, and furnace cover and the hydraulic pressure is set on the upper section of the furnace body top of the device. This utility model solves the problem that the existing garbage processing process, the water content is too high because of garbage, so as to brings great difficult to clean and burning; The new bulk garbage combustible and straw through continuous pyrolysis and gasification furnace, burning can the same reduction effect is good, but also will not lead to image for burning soot, especially produce. Also capable of carrying out use of waste heat, so as to the effect of saving energy.
NOVELTY - This utility model claims a biomass gasification furnace tar separating device, a blower (1) of the air pipe (3) and the hearth (12) of the air inlet pipe (9) through the water container (5) is connected with the water container (5) is provided with a water valve (4), the bottom is provided with a drain valve (7), the water container (5) of the top end is provided with a water level detector (8). The water level detector (8) for outputting signal and the water inlet valve (4) is connected with the input signal. Air inlet pipe and air outlet pipe is connected with the hearth by a container filled with water is provided with barrier action of tar in the water container when the stove close. A stove starts to work, water container water outlet pipe and air inlet pipe. Repeatedly a device capable of the ventilation or close tar function.
NOVELTY - This utility model claims a biomass gasification furnace hearth air inlet device, air inlet device is located on the furnace feeding port (6), an air channel of the hearth air inlet device is the radial direction of the annular structure, the annular air channel through the air inlet pipe and an air inlet valve connected with the air inlet, the air outlet of the annular air outlet is horizontal direction, vertical direction air outlet, in the one kind of or more inclined air outlet. The annular air channel is divided into upper annular air duct (9) and the lower annular air duct (10). To realize wind and wind pressure uniform through the annular air channel and horizontal direction, vertical direction and/or oblique air outlet adjacent to each other, in particular an annular air passage is divided into upper annular air channel and the lower layer annular air channel, which can make the hearth in the two layers of combustion, combustion uniformly, so as to control the temperature of the hearth is between 600 degrees and 650 degrees, a drain pipe and a drain valve is connected with the waste outlet opening is provided, which is good for preventing air channel.
NOVELTY - The utility model claims a residential neighborhood marsh gas using system, belonging to the technical field of renewable energy source, wherein it uses present mature ground source heat pump technology and marsh gas using a butt joint, paving the concrete of the methane purifying tank by the water inlet pipe of the air conditioner side of ground source heat pump system, the ground source heat pump air conditioning in winter to heat to the methane purifying tank, lifting the temperature to improve the fermentation efficiency domestic sewage and increase effect of methane gas, the utility model technical solution not only the domestic sewage and the fecal sewage of residential zone passes through pipe collected marsh gas purifying pond through ground-source heat pump biogas purifying pond, heating to make the domestic sewage and processing up to the national secondary discharge standard, at the same time, it can ensure the generated marsh gas in winter for 2/building method, the utility model is good for environment protection and use of the reproducible resource, has good social benefit, resident natural marsh gas and saves family expense, and it has certain economic benefit.
NOVELTY - The furnace has a furnace main body provided with a dynamic furnace (1), a hearth (2), a fan (7) and a blast pipe (8). The hearth is provided with a heat storage chamber (3) that is provided with multiple heat absorbing blocks (4). The heat storage chamber is provided with a fuel gas pipe (5). The hearth is fixed with a smoke filtering cover (12) that is provided with a filter screen (13). An air inlet and an air outlet of the fan are respectively connected with an air inlet pipe and a smoking pipe (9). The smoking pipe is provided with a switch.    USE - Dynamic biomass gasification furnace.    ADVANTAGE - The furnace can effectively store large amount of heat energy by the chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dynamic biomass gasification furnace in a partial section.'(Drawing includes non-English language text)'    Dynamic furnace (1)    Hearth (2)    Heat storage chamber (3)    Heat absorbing blocks (4)    Fuel gas pipe (5)    Fan (7)    Blast pipe (8)    Smoking pipe (9)    Smoke filtering cover (12)    Filter screen (13)
NOVELTY - The furnace has a furnace main unit that is provided with an upper hearth (5), lower hearth (6), high temperature zone (7) and a base (8). The upper hearth is provided with an air outlet pipe (9) having a chimney (10) provided with a chimney valve (11). The upper portion of the high temperature zone is provided with a water inlet pipe (14) and an annular water sleeve (18). An air inlet pipe (20) is provided with an air inlet valve (21). A right end of the annular air inlet groove (19) is connected with the base provided with an ash outlet (22).    USE - Split-type double-hearth gasification furnace used for gasification of coal and biomass such as crop straw.    ADVANTAGE - The gasification of coal can be improved. The energy can be saved. The emission can be reduced. The full use of the energy can be realized. The waste of heat energy can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) indoor heating system; and    (2) bed system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the split-type double-hearth gasification furnace.    Upper hearth (5)    Lower hearth (6)    High temperature zone (7)    Base (8)    Air outlet pipes (9,20)    Chimney (10)    Chimney valve (11)    Water inlet pipe (14)    Annular water sleeve (18)    Annular air inlet groove (19)    Air inlet valve (21)    Ash outlet (22)
NOVELTY - The device has a hopper (1) connected with a feeding system (2) that is connected with a fluidized bed coke combustion system (5). A fluidized bed catalyst regeneration system (7) is connected with a gas inlet and a discharging port. The discharging port is connected with a biomass pyrolysis gasification system (3). A catalyst separation system (8) is connected with the discharging port. The biomass pyrolysis gasification system is connected with an air inlet.    USE - Biomass pyrolysis gasification and coke oil catalytic cracking device.    ADVANTAGE - The device realizes highly efficient biomass gasification and transformation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pyrolysis gasification and coke oil catalytic cracking method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass pyrolysis gasification and coke oil catalytic cracking device.'(Drawing includes non-English language text)'    Hopper (1)    Feeding system (2)    Biomass pyrolysis gasification system (3)    Fluidized bed coke combustion system (5)    Fluidized bed catalyst regeneration system (7)    Catalyst separation system (8)
NOVELTY - The device has a main body provided with a cracking gas storage tank (1) and a cracking gas pass water tank (4). A RY molten salt pump is connected with a cyclone separator (12) that is connected with an inlet pipe. A solid product collector (13) is connected with a cyclone separator (12). A cone cracking reactor (9) is fixed with a biomass storage bin (8) and a condenser (5). A molten salt storage tank (11) is linked with a liquid collector (10). The condenser is fixed with the liquid collector. An upper part of the cone cracking reactor is connected with an electric motor (6).    USE - Molten salt biomass quick thermal cracking device.    ADVANTAGE - The device is inexpensive, and has high heat energy utilization rate. The device increases yield of biomass fuel and realizes continuous feeding.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a molten salt biomass quick thermal cracking device.    Cracking gas storage tank (1)    Cracking gas pass water tank (4)    Condenser (5)    Electric motor (6)    Biomass storage bin (8)    Cone cracking reactor (9)    Liquid collector (10)    Molten salt storage tank (11)    Cyclone separator (12)    Solid product collector (13)
NOVELTY - Preparing cornstalk cured fuel in cold region, comprises (i) crushing cornstalk in the cold region, where the crushed cornstalk is 22-25 cm long; (ii) spraying and stirring according to a ratio of the total weight of the crushed cornstalk in kilogram to the volume of biogas slurry after livestock manure fermentation, where the ratio is 35:(0.9-1.1); (iii) covering the resulting crushed cornstalk by a plastic film, and placing in an environment at 15 plus minus 5 degrees C for 2 hours, or under sunshine at more than 0 degrees C for 2 hours; and (iv) pressing the resulting crushed cornstalk to obtain cured fuel rod.    USE - The method is useful for preparing cornstalk cured fuel in cold region (claimed).    ADVANTAGE - The method: scientifically and reasonably utilizes physical and chemical properties of the cornstalk in cold region; finishes processing of cured fuel without adding any industrial adhesive additive; and has simple process, high curing rate and good mechanical property of the fuel rod; and is environmentally friendly.
NOVELTY - The method involves adding an electrolyte solution by a micro-algae electrolytic cell. A planar porous electrode material is provided with a substrate material. The substrate material is formed on the micro-algae electrolytic cell. A micro-algae photo-electrode is provided with an anode and a cathode. The electrolyte solution is added with an electron mediator. The micro-algae electrolytic cell is provided with electrons and protons. A surface of the substrate material is formed on an electrode electric part. The electrolyte solution is added with the anode and the cathode.    USE - Visible-light-driven water splitting microalgae electrolytic cell hydrogen producing method.    ADVANTAGE - The method enables reducing electrode preparing cost and improving hydrogen-producing efficiency. The method enables separating hydrogen in an effective manner, so as to ensure continuous and stable process.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view representation of a visible-light-driven water splitting microalgae electrolytic cell.'(Drawing includes non-English language text)'
NOVELTY - The system has a circulating fluidized bed biomass gasification furnace and a parabolic slot type solar heat collector that are connected together in a parallel manner. Low-temperature heat exchange fluid i.e. water, is discharged from an organic working fluid evaporator. A part of the organic working fluid evaporator is fixed with a circulating fluidized bed biomass gasification furnace. Organic working fluid is passed into a steam turbine. A condenser condenses steam turbine exhaust gas that is returned to the organic working fluid evaporator to realize thermal circulation process.    USE - Solar energy and biomass energy complementation organic rankine cycle thermal power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solar energy and biomass energy complementation organic rankine cycle thermal power generation system.'(Drawing includes non-English language text)'
NOVELTY - The ignition system has a burner (1) that is provided at the bottom of an air inlet. A pair of material returning valve (3,5) is provided with a steam inlet. A boiler ignition device is provided with a boiler burner and a hearth. The lower layer of boiler burner is provided with a gas lighter and a dust hopper. Each layer of boiler burner is set to 2.5-3.5 meter. A reaction device is provided in a gas outlet of igniter, and is equipped at lower layer of the burner.    USE - Biomass pyrolysis ignition system of double-fluidized bed.    ADVANTAGE - Since the pulverized coal discharged from the burner is ignited after the gas is combusted to reach the combustion temperature of the pulverized coal, so that the boiler ignition can be fulfilled effectively. The high-temperature gas for the high-capacity pulverized coal boiler ignition stage of a power plant can be provided, so that the oil ignition mode can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass pyrolysis ignition method of double-fluidized bed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reaction device of biomass pyrolysis ignition system. (Drawing includes non-English language text)    Burner (1)    Smoke separator (2)    Material returning valves (3,5)    Pyrolyzer (4)    Gas separator (6)
NOVELTY - This utility model claims a kind of is provided with external heating device and an auxiliary heating device of methanol evaporator. The methanol evaporator comprises an evaporator shell, an evaporator shell body is set with a bracket, the lower end is provided with a steam outlet at the top of the evaporator shell body, wherein a steam outlet is provided with a foaming device, is provided with a methanol fuel feeding port, the feeding in the upper part of the evaporator shell body is set on one side of straight into the inner wall of the evaporator shell body at the bottom of the pipe, the upper part of the shell of the evaporator is provided with a anti-boiling board with methanol fuel inlet on the outside of the evaporator shell body lower part is provided with an electric heating device, the lower part of the shell is provided with the evaporator temperature at the evaporator end of the shell is provided with a manometer and a safety valve interface, a liquid level meter is set on one side of the evaporator, the evaporator is set at the bottom of the shell discharging end, and it further can be equipped with a sleeve by using waste heat of the auxiliary heating device in the methanol evaporator shell side, the auxiliary heating device for heating main body is made of a heat exchanger, an auxiliary heating device main body and a methanol evaporator. This utility model is novel and capable of greatly improving the combustion efficiency of the combustion methanol, in particular the combustion efficiency of the crude methanol, so as to reduce the fuel consumption.
NOVELTY - A feeding mechanism of the utility model claims a biomass gasification furnace, comprising a guide rail and a guide rail in the gasification furnace, an upper guide rail and a lower guide rail is equipped with a movable vehicle, the mobile vehicle is set with moving car for pushing operation of the moving cylinder, the moving vehicle is equipped with a feeding hopper, the moving car is provided with the feeding hopper is connected with the feeding port, the moving vehicle is set with a compacting air cylinder, a driving shaft vertical to the compaction cylinder is set with downwards, pressing cylinder driving shaft is equipped with a sealing element. This utility model is convenient for feeding, feeding process is smooth, the gasification furnace for continuously and safely.
NOVELTY - This utility model claims a kind of integrated device, especially relates to one kind of rice straw compost for integrated device, belonging to the agricultural machinery of environmental manufacturing technology field. A kind of providing not only a corrosion in the composting process can protect the environment, but also to stalk the orange, the nutrition fertilizer according to by rotten conversion of more balanced to rice straw compost for integrated device. The integrated device is provided with a raw material feeding port are orderly arranged from the top down of rice stalk crushing area, a primary stack fertilizer field and a secondary stack fertilizer field, wherein the rice stalk crushing area and each of the compost field, one of the composting region and the secondary compost discontinuous section is provided with a rice stalk input port, the rice stalk crushing area of the inner part is set with crushing the rice straw at the top of the rice stalk crushing area, compost field in the first time of the side wall of the upper part side wall of the stack fertilizer field is a time which is provided with a finished product fertilizer;
NOVELTY - A kind of roller type hydraulic machine, relating to the environment-friendly device for disposing solid waste. A machine frame, big arm, a roller device and a hydraulic device, the middle part of the roller device and the lower part is welded, device, composed of left and right two hydraulic motors driving the left and right two sets of roller is set symmetrically distributed along the axial direction on the outer side surface of the cylinder is rectangular plane blade. The hydraulic motor is directly the power to the roller, reduces the middle transmission link, so it greatly improves the power transmission efficiency and reliability, improved blade structure, it has low noise, low energy consumption, high production efficiency, and the structure is reasonable, the sludge turning effect is good.
NOVELTY - A biomass carbonizing furnace, comprising a heating furnace and a carbonization furnace, heating furnace according to the bottom of the inner cavity is a conical structure and is provided with a fire grate and an ash, a carbonization furnace at the bottom is provided with a thermoelectric couple. This utility model is biomass carbonizing furnace has simple structure, convenient use, perfect, the design of the fire grate and an ash greatly improves a direct carbonization furnace body inclined pouring furnace dust of working mode, at the same time, use of the thermocouple is convenient for the operation of the monitoring of the carbonization temperature.
NOVELTY - This utility model claims a kind of continuous biomass carbonization device, comprising a combustion chamber, a coking chamber, a carbon box, the carbon, the continuous biomass carbonization device also comprising a feeding mechanism, a feeding cylinder of the feeding mechanism is connected with the upper part of the combustion chamber, the combustion chamber is on the upper end of the cylinder body, and the lower end is connected with the carbonization chamber, the circumference direction of a uniformly distributed gas distribution passage, the outer periphery is provided with a gas flow channel, the gas flow passage is set on one side of the gas outlet, the lower part of the carbonizing chamber is provided with a valve and a steam inlet, a carbonization chamber and the coking chamber matched with the shape of the cross section of the inner cavity port is connected with the carbon outlet of the carbon tank, the collecting carbon box central axis is provided with a carbon outlet mechanism, a carbon box is a sandwich carbon collector, one end passes through the outer side water interlayer and is provided with a carbon outlet and biomass carbon gas outlet. This utility model can side, edge, side carbon, realizing continuous biomass carbonization, the carbonization efficiency.
NOVELTY - This utility model claims a biomass gasification furnace, overcomes the problem that the biomass gasification furnace gasification gas purity is low, flammability, tar purifying effect is bad and so on. The biomass gasification furnace includes the gasification furnace, a transmission pipeline, a condenser, an air outlet pipe and an air inlet pipe, a biomass gasification device comprises a tar purifying device, a tar purifying device is located in the gasification furnace, a tar purifying device is correspondingly connected with the head end and the tail end is connected to the inner tube with a catalyst, the inclined angle of the is more than 30 degree and less than less than 90 degree, the condenser is a condensed water tank, is connected with the head end and the tail end is connected to air outlet tube, the inclined angle is more than 90 degree and less than less than 150 degrees. Is provided with catalytic coke oil and steam in the hearth, it can improve the quality of the combustion gas. This utility model has low cost, simple structure, high purifying quality and so on.
NOVELTY - This utility model claims a kind of biomass, city waste pyrolysis gas generating furnace, wherein it is composed of upper, middle and lower sections, the upper section is a cracking raw material drying section, middle section is cracking-gasification section, the lower section is a heat recovery section. This utility model not only can conveniently and effectively provide the heat needed by cracking, but also can effectively prevent the gas with the original raw material, at the same time making cracking there is no oxygen and waste direct contact reaction, and it will not produce dioxin poisonous gas, so as to prevent the secondary pollution.
NOVELTY - A kind of biomass particle production system, comprising a biomass pellet fuel forming machine, cutter, dust discharging material storage device, a spiral feeder, a drier, a feeding blower, a storage silo connected with the spiral feeder, a spiral feeder and a spiral feeding machine, cutter passes through dust discharging material storage device is connected to the discharge hole of the feeding blower, a storage silo through dryer and the feed port of the spiral feeding machine is connected with the spiral feeding machine of the forming machine is connected with the feeding port. This utility model has simple structure with high efficiency, high yield, low cost, not easy to be damaged and durable, it does not need frequent maintenance and long service life, its structure is compact, the production system is featured with simple structure, fast production speed and efficiency is high, the production of the granular fuel tightly compact, not only flame-resistant but also is convenient to store.
NOVELTY - This utility model claims a fuel device field, specifically relates to a hydrogen generator, comprising an insulating box body, a plurality of metal baffle plate and an even number of carbon, wherein the carbon number of said metal baffle plate is equal to the vertical of the metal baffle plate and carbon plate alternately in the insulating box body, the carbon plate is connected with a wire, and is provided with an air hole on the insulating box body. The device using the electrolysis method can be the water into oxygen and hydrogen, then the oxygen and hydrogen and decomposing a gas hole respectively flow to different places is convenient to use. The structure is simple, green and environment-friendly, simple operation and strong practicability.
NOVELTY - A kind of biomass gasification furnace, comprising a gas producer, a secondary combustion furnace, gas furnace is an interlayer water wall, a secondary combustion furnace is connected with the gasification chamber, the other gas generating furnace and a secondary combustion furnace are respectively provided with a water inlet pipe I, a water inlet pipe II, a water outlet pipe I and II is connected with the water outlet pipe is connected with the heating pipeline. This utility model makes full use of vast rural areas widely in all kinds of organic impurities, the combustible gas generated by the reaction for production of life, so improves the quality of life of, on the other hand, it also avoids using other fuel energy and discharge, in addition, the utility model further is provided with reliable work, convenient use and good use effect and so on.
NOVELTY - For preparing anti-tumor medicine, 4-formyl-3-hydroxy-1,9-dimethyl-11-oxo-11H-dibenzo(b,e)(1,4)dioxepine-6,8-dicarboxylic acid 8-methyl ester (I), is used. The antitumor medicine is formulated in the form of injection, tablet or capsule.    USE - For preparing anti-tumor medicine for treating tumor (i.e. liver cancer, leucocythemia or pancreatic cancer) (claimed).    ADVANTAGE - The present anti-tumor medicine is liver cancer resistant medicine; and utilizes naturally occurring products. The compound (I) does not have any toxic and side effects, has high biological utilization degree, stable performance, and is environment-friendly.
NOVELTY - Carbon dioxide fixation involves placing underground water or hot spring water which has iron content in indoor snow (I) while cooling by refrigeration, applying pressure to snow, and taking carbon dioxide and methane.    USE - Carbon dioxide fixation used in offices.    ADVANTAGE - Global warming is stopped.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a system used for carbon dioxide fixation. (Drawing includes non-English language text).    Cold gas output opening (HA)    Drainage pump (HE)    Dissolution precipitation water tank (HI)    Snow (I)    Pressure ventilating fan (RO)
NOVELTY - The cell has a modifier supplying reformed fuel to a fuel electrode side of a fuel cell stack. A controller controls taking-out of electric power while controlling a fuel supply apparatus, a water supply apparatus and an oxidizing agent gas supply apparatus. A fuel cell stack performs a shutdown stop in a state more than oxidation temperature. A shutdown stop circuit reduces temperature of the fuel electrode side and an oxidizing agent gas pole side before performing shutdown stop process.    USE - Solid oxide fuel cell for generating electric power.    ADVANTAGE - The fuel cell performs the shut down stop process, and fully suppresses the oxidation of the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a timing diagram illustrating an operation of a fuel cell apparatus at a time of emergency shut down. '(Drawing includes non-English language text)'
NOVELTY - Antibiotic residue in milk contains penicillin G, ampicillin, cloxacillin, gentamicin, streptomycin, and Terramycin (RTM: Oxytetracycline).    USE - Analysis of antibiotic residue in milk for developing control measures on use of antibiotics based on antibiotic prophylaxis standard (claimed).    ADVANTAGE - Analysis of antibiotic residue in milk promotes economic development, reduces dairy farmer loss, is environment-friendly, and safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for liquid phase chromatography-mass spectrometry (LC-MS-MS) for qualitative and quantitative detection of antibiotic residue.
NOVELTY - Integrated water electrolysis system of decomposing ammonia to produce hydrogen gas purifier, relating to electrolytic hydrogen production field. An outer cylinder and an inner cylinder, a heating device is set in the inner part of the inner cylinder, heating device comprises an electric heating element, a protective sleeve, an electric heating element is set on the protection sleeve, a protective sleeve is welded on one end of the inner cylinder, and the exposed outer cylinder is provided, and the other end is vertically extends into the inner part of the inner cylinder is set between the molecular sieve and the inner wall of the outer wall of the inner cylinder are respectively provided with working gas outlet, molecular sieve inlet on the upper part of the outer side wall of the working air inlet is set on the out tube wall of the protective sleeve of the outer cylinder, set with molecular sieve outlet at the lower part of the outer side wall. The utility model a purifying and separating device based on the traditional gas, the separated structure is optimized, the gas purifier the volume is greatly reduced the original function based on the device in a fully optimized, at the same time, the equipment material cost is reduced.
NOVELTY - This utility model claims an automatic feeding straw microwave carbonization device, belonging to the technical field of machinery, comprising a containing chamber, the upper part is provided with a feeding port, the bottom is provided with discharging port of carbonization furnace, a carbonization furnace is fixed with a feeding mechanism on one side of the bracket, the feeding port of the upper part of the feeding mechanism is provided with a feeding hopper, the discharge hole of the lower part is set with a discharging machine, wherein the side of at least one carbide furnace capable of continuously generating the microwave generator, the microwave generator is connected with the chamber of the microwave guide tube with silicon carbide furnace, the upper part of the feeding hopper is further provided with an automatic conveying straw into feeding hopper of the conveying device. This utility model is generated by microwave generator of the microwave direct the straw and so on agricultural waste carbon, solves the problem that the traditional agricultural biological carbon technology not only pollute the environment, also waste resource and so on, it has energy-saving, green and environment-friendly and so on.
NOVELTY - Organic and energy recycling system, comprising a biogas generating pool, marsh gas station, urban organic garbage recycling processing station, rural straw purchase processing station, organic fertilizer factory, marsh gas generating pool is provided with a sewage inlet and organic garbage, straw input opening, a sewage inlet is connected with the urban sewage pipe network, organic garbage, straw input opening and recycling treatment station passes through the pressure transporting pipe and organic waste, rural straw purchase processing station, marsh gas generating pool outlet leading to the marsh gas station through gas transmission pipeline, a marsh gas station through a gas pipe network is sent to the user, a marsh gas generating tank is further provided with biogas, biogas outlet, biogas slurry and biogas residue biogas liquid discharge pump through the biogas slurry and biogas residue transportation pipeline and the pipeline on the biogas slurry and biogas residue organic fertilizer is conveyed factory. It can make sewage, urban organic garbage and rural straw into useful marsh gas and organic fertilizer, reduces the environment pollution, improving soil structure, to produce green organic food and reduce the occurrence of the modern diseases.
NOVELTY - Fertilizer comprises 7-8 wt.% urea, 37-39 wt.% diammonium phosphate, 9-11 wt.% potassium sulfate and dry biogas residues (remainder).    USE - As fertilizer for watermelons (claimed).    ADVANTAGE - The fertilizer increases yield and improves quality of the watermelons. The preparation of the fertilizer enables innovative and effective utilization of the biogas residues, hence secondary pollution resulting due to the biogas residues is reduced. The fertilizer substitutes existing inorganic fertilizer used for agricultural production of the watermelons.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves mixing the above-mentioned raw materials in predetermined weight proportions, uniformly mixing obtained admixture and granulating the admixture to obtain granules having particle diameter of 4 mm.
NOVELTY - A thiourea huperzine A compound (I), is new.    USE - New thiourea huperzine A compound is used for preparing pesticide for preventing and/or treating agricultural pests chosen from Brevicoryne brassicae, armyworm and Tetranychus cinnabarinus (claimed).    ADVANTAGE - The thiourea huperzine A compound can be prepared with simple and easy operation. The corrected mortality of the B.brassicae can reach 85% when the concentration of the compound is 2000 mg/kg. The corrected mortality of the T.cinnabarinus can reach 68% when the concentration of the compound is 1000 mg/kg. The compound provides environmentally-friendly pesticides. The compound provides basis for screening derivates with higher activity of the compound.    DETAILED DESCRIPTION - A thiourea huperzine A compound of formula (I), is new.    R=methyl, cyclopentyl, cyclohexyl, phenyl, halophenyl, 4-acetylphenyl, naphthyl, thiophene or furan.    An INDEPENDENT CLAIM is included for preparation of thiourea huperzine A compound (I).
NOVELTY - Catalyst comprises either: zinc oxide and the oxide of a second metal, where the second metal is potassium, sodium, calcium, magnesium, tin, aluminum, lanthanum, silicon, carbon, iron, cobalt, vanadium, praseodymium, cerium, ytterbium, copper, silver, titanium and/or zirconium; or zinc oxide mixed with the oxide of second metal, where the second metal is more electronegative than zinc.    USE - The catalyst is useful for catalyzing a reaction, which is an esterification reaction of the free fatty acid and/or a transesterification reaction of glyceride (all claimed) for biodiesel production.    ADVANTAGE - The catalyst: simultaneously catalyzes the transesterification reaction of the glyceride and the esterification reaction of the free fatty acid; minimizes the ratio of methanol to oil to 9:1, thus greatly decreasing the methanol recovery cost; is less corrosive and minimizes the environmental problems associated with homogeneously catalytic methods; and has the potential to make biodiesel production more profitable by utilizing unrefined or waste oils in biodiesel production, thus reducing the cost of oil feedstock and significantly minimizing the biodiesel production cost; and is highly active and can be easily separated and recovered from biodiesel products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a process comprising contacting a material that comprises a glyceride with an alcohol in the presence of the catalyst, such that at least some of the glyceride is converted into the corresponding alcoholic ester of the glyceride.
NOVELTY - Treating a lignocellulosic biomass, comprises combining a lignocellulosic biomass feedstock with a pretreatment composition including 50-70 vol.% of an aqueous organic solvent, up to 10 vol.% of an alkaline component, and up to 10 vol.% of an oxidizing agent.    USE - The lignocellulosic biomass is useful for: forming pulp or paper; and forming a biofuel including ethanol or diesel (all claimed).    ADVANTAGE - The method is capable of treating lignocellulosic biomass in an economical and less energy consuming manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) forming a biofuel, comprising treating the lignocellulosic biomass, and fermenting the one or more fermentable sugars to form the biofuel; and    (2) the pretreatment composition for the lignocellulosic biomass.
NOVELTY - System (I) (200) comprises: a leaching system (202) configured to receive biomass and leach the biomass such that water soluble combustion unfriendly chemical components present in the biomass are leached into an effluent; and a torrefaction reactor (215) configured to receive the leached biomass and heat the biomass to generate torrefied biomass.    USE - The system is useful for biomass fuel production and integrated biomass and biofuel production (renewable coal replacement fuel (RCRF) production).    ADVANTAGE - The system: is substantially environmentally neutral and reduces content of combustion unfriendly chemical components in the RCRF through leaching and torrefaction; reduces or eliminates pollution and/or reduces exposure to environmental statutes and regulations; and exhibits less handling costs, reduced transportation, and less capital intensive and operating costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system (II) comprising: leaching system configured to receive biomass and rinse the biomass such that combustion unfriendly chemical components present in the biomass are leached into an effluent; the torrefaction reactor; and an algaculture production system configured (e1) to receive at least a portion of the effluent from the leaching system, and (e2) cultivate algae in a liquid comprising the portion of the effluent received from the leaching system.    DESCRIPTION OF DRAWING(S) - The figure illustrates a block diagram of selected components of integrated biomass and biofuel production system.    System (200)    Leaching system (202)    Preheater (213)    Torrefaction reactor (215)    Furnace (222)
NOVELTY - Strain Penicillium sp. PBT-2 extracted from samples of humic pod mixed with cereal straw and having polyfunctional properties and promoting increased productivity of agroecosystem, participating in processes of transformation of organic remains of natural origin, is deposited in the Departmental Collection of Beneficial Microorganisms of Agricultural Purpose of the Russian Academy of Agricultural Sciences (RCAM) (GNU VNIISHM) under the registration number RCAM 01017 and may be used in transformation of organic remains of natural origin.    USE - Biotechnologies.    ADVANTAGE - Improved productivity of agroecosystem.3 ex
NOVELTY - A kind of neomycin refining post device, comprising a rotating salt tank, rotating salt tank is provided with a stirring rod, the stirring rod one end is connected with the electric motor and the rotating salt tank is connected through with the carbon outlet of the bottom end and the top end of the hopper pipe. This utility model adopts a structure that adds a dust processing device the carbon interface, can conveniently and safely process and discharge of active carbon dust, improve the dust flying everywhere influence the work body health of the worker, condition of the electric appliance, improves the production efficiency, reduces the potential safety hazard.
NOVELTY - The method involves selecting biological oil containing two hydrogen active components as raw material. Raw material oil and hydrogen gas are passed through a hydrogenation active component of a catalyst bed layer that is arranged in a section of a reaction region. Platinum and palladium are separated from an active metal component using a hydrogenation modification catalyst. Hydrogen is separated from the raw material oil, where the hydrogen separated oil is fractionated in a fractionating tower to obtain naphthal and low freezing point diesel oil.    USE - Hydrogenation method for producing high-quality low solidifying point motor fuel from biological oil.    ADVANTAGE - The method enables ensuring stable operation and service life of the motor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a hydrogenation method.'(Drawing includes non-English language text)'
NOVELTY - Fertilizer comprises sheep manure, chicken manure, bran, fine sand and water in a mass ratio of 12-14:5-7:35-40:5-7:35-40.    USE - The fertilizer is useful for planting organic fruit (claimed).    ADVANTAGE - The fertilizer is easy to prepare as it contains wide material source and has high nutrient balance and enables to improve disease resistance and quality of the fruit with high yield, thus economic benefits of the fruit growers is greatly increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the fertilizer, which involves (a) mixing sheep manure, chicken manure, bran, fine sand and water, stirring uniformly, and stacking the mixed mixture into a ladder shaped stack at a height of at least 6 m, (b) generating 5-8 holes per m2 of the stack, where the diameter of the holes is 5-8 cm, and the holes are uniform from upper end to lower end of the stack, (c) covering the fertilizer using plastic thin film, where the width of the middle portion of the plastic film is 30-40 cm, and the length of the plastic film is consistent with the length of the compost stack, (d) detecting the temperature of the stack, when the temperature reaches 60-65 degrees C, turning the stack and repeating the stacking step, and (e) repeating steps (a)-(d), until the fertilizer has 90% or more Actinomycetes and no fishy smell.
NOVELTY - A distillers grains acid-base modified adsorption material has adsorption removal rate of about 90-99% and adsorption capacity of about 500 mg/g on lead(II) ion, cadmium ion, mercuric ion, chromium (III) ion, hexavalent chromium ion, silver ion, cupric ion and zinc(II) ion in heavy metal wastewater.    USE - Distillers grains acid-base modified adsorption material is used for preparing fuel ethanol by fermentation (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of distillers grains acid-base modified adsorption material, which involves subjecting distillers grains to acid addition, alkali addition, blending, microwave heating, liquid slag separation, washing and drying.
NOVELTY - The method involves introducing the warm air generated by marsh gas furnace into the high temperature air inlet (32) of drier (3). The material in the dryer is dried and the waste heat is emitted out through waste heat air outlet (34) of drier. The discharged waste heat is introduced into air inlet (22) of hot air distribution device (2). The organic garbage is discharged into fermentation tank (1) through feeding port (10). The heat is generated to promote fermentation of organic garbage and the heat is induced into marsh gas furnace through exhaust pipe.    USE - Method for rapidly fermenting organic household garbage.    ADVANTAGE - The process quickly ferments the organic garbage in an efficient manner at short time period, and speeds up the household garbage treating speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermentation device for organic garbage.    Fermentation tank (1)    Hot air distribution device (2)    Drier (3)    Feeding port of fermentation tank (10)    Air inlet of hot air distribution device (22)    High temperature air inlet of drier (32)    Waste heat air outlet of drier (34)
NOVELTY - Method for production of bio-organic fertilizer involves using 70-80 pts. wt. cassava starch processing waste residue, 10-20 pts. wt. bran, 10 pts. wt. sweet potato, 10 pts. wt. straw, 0.1-0.2 pts. wt. fungi and 0.2 pts. wt. brown sugar.    USE - The method is useful for production of bio-organic fertilizer (claimed).    ADVANTAGE - The fertilizer improves soil and product quality and safety and protects environment as it recycles cassava starch processing waste residue. The method reduces production cost.
NOVELTY - The movable microbial fermentation system has a control room (2) which is connected with a fermentation room (1). The control room and fermentation room are fixedly arranged above a movable platform (3). The inclined pedal (24), fermentation room, and the control room are sequentially arranged.    USE - Movable microbial fermentation system used in agricultural microbial fermentation.    ADVANTAGE - The system can be easily dismantled. The complete farmland distributed straw waste fermentation can be ensured, so that labor and raw material transportation costs are reduced. The system is simple in structure. The farmland distributed straw wastes are reasonably utilized, so that environment is beautified. The resource recycling of the system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the movable microbial fermentation system.    Fermentation room (1)    Control room (2)    Movable platform (3)    Blower (20)    Inclined pedal (24)
NOVELTY - Organic fertilizer comprises 20-30 pts. wt. straw, 20-40 pts. wt. livestock manure, 10-20 pts. wt. urea, 10-20 pts. wt. bone powder, 5-10 pts. wt. humic acid and 5-10 pts. wt. trace element.    USE - As organic fertilizer.    ADVANTAGE - The method enables to reduce production cost of the fertilizer, and agricultural waste products, thus environment is improved. The organic fertilizer is 10-30% highly efficient compared to common fertilizers and environmentally-friendly as it doesn't contains hazard resources that are responsible for air and water pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) weighing the above-mentioned raw materials, (b) mixing straw, livestock manure, urea and bone powder and fermenting at 25-45 degrees C for 20-40 days, and (c) removing the fermented material and adding humic acid and trace element and mixing uniformly.
NOVELTY - Green organic fertilizer comprises 10-40 pts. wt. corn straw, 20-40 pts. wt. chicken manure, 10-20 pts. wt. urea, 10-40 pts. wt. montmorillonite and 1-10 pts. wt. organic amine salt.    USE - As green organic fertilizer.    ADVANTAGE - The organic fertilizer is environment-friendly and has 20% high fertilizing efficiency compared to ordinary fertilizer. The method enables to reduce waste and production cost by utilizing agricultural waste products, thus environment is clean.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves mixing the above-mentioned raw materials except organic amine salts and fermenting at 25-40 degrees C for 20-40 days, and uniformly mixing the obtained fermented material with organic amine salts.
NOVELTY - Preparation of tigogenin involves adding solid superacid (as catalyst), Sisal saponoin slag and water into a reaction tank, stirring uniformly, heating at 135-140 degrees C under pressure of 0.25-0.3 MPa, hydrolyzing for 2-4 hours, and then neutralizing, extracting, concentrating and purifying.    USE - Preparation of tigogenin (claimed).    ADVANTAGE - The method enables preparation of tigogenin having high purity with high yield, by environmentalally-friendly process.
NOVELTY - Method for preparing vitamin B12, involves fermenting, hydrolyzing and filtering cyan compound, converting cyan compound into cyanide, and crystallizing and drying crystals, where the cyan compound in the cyanide conversion is an iron-cyan complex, reaction concentration is 200-4000 mu g/ml, pH value of the reaction system is 3-8, reaction temperature is 50-120 degrees C, and reaction time is 0.5-6 hours.    USE - The method is useful for preparing vitamin B12 by a fermentation (claimed).    ADVANTAGE - The method is environmentally-friendly, simple and cost-effective, and has high conversion efficiency and overcomes conversion of vitamin B12 by sodium cyanide.
NOVELTY - Preparing (E)-2-cyano-N,N-diethyl-3-(4-hydroxy-3-methoxy-5-nitro-phenyl)-acrylamide (V) comprises nitrating (E)-2-cyano-N,N-diethyl-3-(4-hydroxy-3-methoxy-phenyl)-acrylamide (IV) with a nitrating agent in the presence of a catalyst.    USE - The process is useful for preparing (V) that is used to prepare (I) (claimed), where (I) is used for adjuvant treatment of Parkinson's disease. No biological data given.    ADVANTAGE - The process: is performed under simple and mild reaction conditions; and provides (V) that prepares (I) (greater than 90% and greater than 99.5% E-isomer) under non-hazardous conditions, environment friendly, easy to handle reagents and reduced reaction times, and by utilizing low energy and environment friendly demethylation step.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing (IV) comprising: condensing 4-hydroxy-3-methoxy-benzaldehyde (II) with 2-cyano-N,N-diethyl-acetamide (III) to produce a reaction mixture; and adding (IV) as a seed to the reaction; and    (2) preparing entacapone (I) comprising demethylating (V) in the presence of an organic base and acid at below 100 degrees C.
NOVELTY - Production of alkaline fertilizer comprises mixing phosphate rock tailings or low grade phosphate rock and insoluble potassium-containing rock at a mass ratio of 1:0.4-0.9, adding coke or mixture of anthracite and coke by 4-10 wt.% raw material, and uniformly mixing; grinding to obtain powder; adding water to powder to obtain block material; sintering at 1000-1250 degrees C for 30-150 minutes to obtain sintered clinker; and quenching to 80-110 degrees C for 1-20 seconds using water, drying, crushing, and grinding.    USE - Method for producing alkaline fertilizer (claimed).    ADVANTAGE - The method is simple and easy to operate and has low cost. The product is nutrient-rich and environment-friendly and has stable quality.
NOVELTY - This utility model claims a kind of a plurality of fermentation chamber of the marsh gas tank, comprising a tank body with an inner cavity, the upper part is provided with the tank body and the tank body is connected with the inner cavity of the feeding pipe, a discharging opening and an air guide pipe, the upper part of the inner cavity of the tank body is an air storage chamber, is set on the tank body top part of the gas-guide tube is connected with air chamber is connected with the bottom of the tank body is provided with at least one baffle plate, the inner cavity of the tank body is divided into at least two fermentation chamber, a feeding pipe and a discharging port are respectively connected with the two sides of the fermentation chamber. Using a plurality of fermentation chamber of the biogas pool organic material in a fermentation chamber, the organic substance by the microorganism adequately.
NOVELTY - This utility model claims a kind of deposition with a methane tank, comprising a tank body with an inner cavity, the tank body is provided with the upper part of the inner cavity of the tank body is connected with the inner cavity of the feeding pipe, a discharging opening and an air guide pipe is an air storage chamber, the upper part of the pool body, the gas-guide tube is connected with air chamber is connected with the bottom of the pool body is provided with not the tank body separated clapboard and the lower clapboard divides the inner cavity of the tank body part into a fermentation chamber and a deposition chamber, the feeding pipe is connected with the settling chamber, a discharge port is connected with the fermentation chamber, not to generate biogas residue and biogas liquid separating marsh gas by the marsh gas tank can ferment, can be separated to remove the clean is convenient to respectively recycle the biogas residue and biogas slurry, in addition, the marsh gas tank is a clean biogas residue not with the microorganism in the biogas liquid, which is good for the remaining in the organic matter in the fermentation chamber to ferment.
NOVELTY - This utility model claims a kind of bed with desulphurization of the marsh gas tank, comprising a tank body with an inner cavity, wherein the upper part of the inner cavity of the tank body is the lower part of the inner cavity of the air storage chamber, the tank body is fermentation chamber, the upper part of the pool body is provided with a fermentation chamber and a discharge port of the feed pipe, the top of the tank body is provided with an air storage chamber is connected with a gas-guide tube, a gas storage chamber is provided with a desulphurization bed, bed for the sulfureted hydrogen and carbon dioxide in marsh gas into elemental sulphur, which avoids the corrosion of hydrogen sulphide metal device of marsh gas and harm the health of human body, improve the safety of the marsh gas. In addition, the desulfurizing bed is set on the marsh gas tank, it does not need to set the desulfurizing tower, the marsh gas desulfurization cost, which is more convenient for popularization and application.
NOVELTY - This utility model claims an integrated biological turntable sewage treatment device, referring to the field of sewage treatment device, comprising a rotor unit and a shell unit, the rotor unit comprises a driving device, the driving device is driven to rotate by the main shaft, the upper part is fixed on the main shaft and are arranged in at least one stage of disk unit of the rotating shaft, wherein each level disc unit along the main shaft axial direction, and the adjacent disk on the main shaft axial direction, only the adjacent sides to form extending along the main shaft axial direction is S shaped flow passage. The utility model is provided with low energy consumption, small floor space, stable structure and plate using a long service life; Matched with the biological turntable sewage treatment technology arrangement structure is flexible and convenient and economical and practical.
NOVELTY - An eco fertilizer is prepared by mixing organic substances and inorganic substances containing nitrogen and phosphorus elements to obtain mixed material; adding first composite microorganism, uniformly stirring, and controlling moisture content at 50-60 wt.%; naturally fermenting in aerobic environment at not greater than 60 degrees C; drying at less than 40 degrees C and controlling water content less than or equal to 30 wt.%; adding second composite microorganism and uniformly stirring; and granulating.    USE - Method for preparing eco fertilizer (claimed).    DETAILED DESCRIPTION - An eco fertilizer is prepared by mixing organic substances and inorganic substances containing nitrogen and phosphorus elements to obtain mixed material; adding first composite microorganism, uniformly stirring, and controlling moisture content at 50-60 wt.%; naturally fermenting in aerobic environment at not greater than 60 degrees C; drying at less than 40 degrees C and controlling water content less than or equal to 30 wt.%; adding second composite microorganism and uniformly stirring; and granulating. The first composite microorganism is Bacillus, lactic acid bacteria, yeast, and/or actinomycetes and has viable count of greater than or equal to 1 billion/g. The second composite microorganism is Bacillus, lactic acid bacteria, yeast, silicate bacteria, photosynthetic bacteria, and/or actinomycetes and has viable count of greater than or equal to 10 billion/g.
NOVELTY - Granular fertilizer is prepared by performing liquid submerged fermentation and cultivation process by processing functional microorganisms and raw materials, subjecting the bacterial liquid to centrifugation, and subsequently adding 5% granulating materials when a composite microorganism fertilizer is granulated so as to product the composite microorganism granular fertilizer of which the number of the effective viable-organisms is more than or equal to 0.5 billion/g.    USE - Granular fertilizer.    ADVANTAGE - The granular fertilizer has total nitrogen, phosphorus pentoxide and potassium oxide content of more than 10%, organic medium of more than 40%, effective viable count of more than 5 hundred million/g, mixed bacterium of less than 30% and water of less than 10%, and storage stability of 18 months, and is cost-effective. The fertilizer exhibits good effect even at less dose, improves soil granule structure, and suppresses crop soil-borne infection.    DETAILED DESCRIPTION - Granular fertilizer is prepared by performing liquid submerged fermentation and cultivation process by processing functional microorganisms and raw materials in a 3724 gauss magnetic field environment to be domesticated for 13 hours when having the most number of vegetative bodies, so that to improve stress resistance and preservation time of beneficial bacterium, after the domestication, subjecting the bacterial liquid to centrifugation at 6000 rotations/minute, so that the viable-organism count is more than 20 billion, and subsequently adding 5% granulating materials when a composite microorganism fertilizer is granulated so as to product the composite microorganism granular fertilizer of which the number of the effective viable-organisms is more than or equal to 0.5 billion/g.
NOVELTY - Preparation of nutritional biogas slurry biological water flush fertilizer involves adding monosodium glutamate waste liquid to biogas liquid, adjusting the pH value to 6-7, stirring the mixture, allowing to react for two days, adding microbial agent to the reacted mixture, stirring, fermenting the mixture for 5-10 days, adding microelements and calcium ammonium nitrate to the fermented mixture, stirring the mixture and fermenting product.    USE - The method is useful for preparing nutritional biogas slurry biological water flush fertilizer (claimed).    ADVANTAGE - The method is simple and cost-effective, enables microbes to propagate by taking the waste liquor as matrix, reduces the using cost of microbes and improves the soil aggregate structure.
NOVELTY - A nitrate enzyme fertilizer is prepared by mixing aniseed and micro-stirring, granulating, inspecting, packaging, and storing; mixing agricultural calcium ammonium nitrate and magnesium nitrate hexahydrate agent and uniformly stirring; mixing boric acid, sodium iron EDTA and zinc nitrate hexahydrate and uniformly stirring; uniformly mixing aniseed with the first and second mixtures and stirring; and high-pressure spraying with metal enzyme fertilizer, and uniformly mixing water-soluble powder-shaped calcium magnesium nitrate enzyme fertilizer.    USE - Preparation method of nitrate enzyme fertilizer (claimed).    ADVANTAGE - The method is unique and easy to operate, has novel design, advanced technology, wide application and low cost, improves the fertilizer's effect, and activates the soil retention of insoluble calcium magnesium nitrate fertilizer. The fertilizer has long efficiency and has great practicability.    DETAILED DESCRIPTION - A nitrate enzyme fertilizer is prepared by mixing aniseed and micro-stirring, granulating, inspecting, packaging, and storing; mixing 40-88 wt.% agricultural calcium ammonium nitrate and 10-50 wt.% magnesium nitrate hexahydrate agent into 1-8 m stainless steel blender, and uniformly stirring; mixing 0.3-2.5 wt.% boric acid, 0.2-3 wt.% sodium iron EDTA and 0.5-2.5 wt.% zinc nitrate hexahydrate into 0.5-1.2 m stainless steel blender, and uniformly stirring; uniformly mixing with aniseed and the first mixture on 2-10 m stainless steel blender, and stirring; and high-pressure spraying with 0.1-1 wt.% metal enzyme fertilizer, and uniformly mixing water-soluble powder-shaped nitrate calcium magnesium nitrate enzyme fertilizer.
NOVELTY - Organic fertilizer comprises 200-250 kg clean soil, 100-150 kg tea seed cake, 200-300 kg wheat straw powder, 150-180 kg excrement, 80-100 kg corn flour, 50-80 kg rice hull, 1-1.5 kg urea, 60-90 kg sawdust, 0.5-0.8 kg enzyme and 150-180 kg water.    USE - As organic fertilizer.    ADVANTAGE - The fertilizer improves physical, chemical and biological characteristic of soil for growth of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) mixing the above-mentioned raw materials uniformly and fermenting the mixture, until the moisture content reaches 45%, (b) adding corn flour and strain to the mixture for increasing the sugar content for fermenting bacteria, and adding water and stirring uniformly, (c) stacking the stirred material to 1 m height and 1.8 m width, and covering the stack with hemp sheet for aerobic fermentation, and (d) fermenting for 3-5 days and packing the dried manure in small bags.
NOVELTY - A composite fertilizer comprises 52-55 wt.% biological bacteria solution culture, 41-45 wt.% amino acid primary powder, 2.8-3.3 wt.% zinc sulfate, 3-4.63 wt.% boric acid, 0.05-1 wt.% sodium molybdenum dihydrate, and 0.12-1.5 wt.% manganese sulfate trihydrate. The composite fertilizer is prepared by placing bacteria solution culture in 3724 Gaussian strong magnetic field environment, performing acclimatization for 24 hours, completely dissolving amino acid primary powder in bacterial solution culture, adding inorganic salts and trace elements, dissolving, and filtering.    USE - Composite fertilizer.
NOVELTY - The utility model claims a sewage purifying device, especially relates to a kind of combined type ecological purifying cage, comprising a protection device and at least one cleaning unit cage body, the cage for purifying unit comprises an outer frame and a biological filler is set in the outer frame, the outer frame is set on the inner wall filler bracket, the biological filler fixed on the packing support, the outer frame is further provided with a connecting piece. This utility model is a sewage collecting and purifying system, using biological contact oxidation and a current-pushing purification principle, the sewage directly inserting combined type ecological purifying cage for conveying and purifying, wherein the device mainly for deeply processing and recycling domestic sewage, industrial waste water and landscape, river water pollution and so on purifying, is not limited by the field, can be set on the sewage pipeline, river, water, landscape water body such as in the system, which is provided with good water quality, low investment, small floor area (or not), permanently fixed facility, it is convenient to install, disassemble and maintain and so on.
NOVELTY - The utility model relates to a sewage processing device, a simple structure, high intensity, simple production technique, small floor area, low cost, packaging, transportation, construction, convenient installation, and can be adjusted in the volume of the micro-organism treatment pond according to the field actual, comprising a hollow cylinder body and a detachable hollow two ends of left and right end covers, a hollow cylinder composed of a cylinder body and the lower cylinder body by a fixing device and a splicing.
NOVELTY - This utility model claims a kind of improved elliptical double-air a commercial household marsh gas pool, comprising a marsh gas tank body, a feed pipe, a discharge pipe, wherein the biogas pool body is elliptic, inside of which is provided with yeast, storage chamber, a water pressure, the fermentation of the marsh gas tank body lower part of the storage chamber are two and are respectively located on the left and right sides of two sides of the upper part of the methane tank body, wherein the water pressure of the fermentation chamber is set on the upper part in the middle of the upper part of the marsh gas tank, the feeding pipe and the discharging pipe, the lower end is set in the fermentation of the lower part of the active layer, the lower end of the discharging pipe is higher than the discharge tube in the clear liquid layer in the fermentation of the following , the feeding pipe of the feeding opening of the outlet. This utility model has reasonable structure design, improves the feeding and discharging part, which is more suitable for industrial production and transportation, which is more suitable for actual production marsh gas tank for rural area, and it can effectively improve the marsh gas fermentation yield.
NOVELTY - This utility model claims a kind of portable methane tank stirrer, wherein the device comprises a piston rod, a piston, a stirrer main pipe, a liquid absorbing pipe, a one-way valve I, a one-way valve II and a liquid discharging pipe, by repeating the operation piston rod that is capable of can, stirring methane tank fermentation product of the utility model is provided with simple structure, convenient use, good stirring effect and low cost;
NOVELTY - This utility model claims a kind of new-type garbage bin, comprising a box body, the box body is provided with two communicated fermenting chamber; the top end of the barrel body is provided with a barrel cover, the lower part of the barrel cover is provided with a sealing cover, a side of the barrel body is provided with a collecting tank, a drier and a processor, the lower end of the barrel body are respectively provided with a valve. This utility model is a creative design, capable of recycling the garbage to generate marsh gas again makes full use, which not only effectively process garbage further to reach the purpose of energy-saving and environment-friendly, economical and practical.
NOVELTY - This utility model claims a kind of hydraulic marsh gas tank, belonging to a kind of anaerobic fermentation device, the utility model is hydraulic marsh gas tank, comprising a fermentation tank, a fermenting tank and the tank cover is sealed is further provided with a drainage passage is connected with the material pipe for feeding and water pressure chamber for adjusting the pressure of the marsh gas, the upper part of the fermenting tank there is marsh gas storage, the lower part of the fermentation tank for containing yeast water, the upper part of the marsh gas storing and water pressure, the water pressure and the fermenting tank, the said water discharging channel is connected with the water outlet is set on the water pressure chamber and connected with the lower part of a spacing. The upper part of the marsh gas storing and water pressure chamber is connected with the can avoid sinking because the fermentation tank and leakage accident. In addition, the utility model is hydraulic marsh gas tank is provided with high-efficient air supply pressure constant, it is safe for the special improving water pressure chamber and so on.
NOVELTY - A new marsh gas tank in cold area, the utility model claims a renewable sources utilization field, especially relates to a kind of new slag removing machine for methane tank in cold area. A kind of cold of new slag removing machine for methane tank, comprising a methane tank main body, the peripheral wall of the marsh gas tank main body is provided with a connecting rib, the connecting rib is provided with a supporting rib, the top of the marsh gas tank is provided with a top cover, the top cover to form a sealing body through a connecting rib, a supporting rib with the marsh gas tank main body, one side of the marsh gas tank is provided with a feeding port, and the other side is provided with a discharging port, the feeding port is higher than the discharge port, the upper part is provided with the gas pipe, the inner wall of the marsh gas tank is provided with a fixing ring, the fixing ring is provided with a coil, the coil is a water inlet pipe by the controller connected with the solar heat collector, the coil is connected with the solar energy heat collector. This utility model beneficial effects: rational structure, convenient installation, fast use is provided with a feeding port and a discharging port on the wall of the marsh gas tank main body, it can automatically clear the residue in the tank, which avoids artificial periodically a cleaning pool, decumbent corydalis tuber also can realize natural gas in cold winter.
NOVELTY - The utility model claims a marsh gas tank of the test device, a temperature control testing device, especially a kind of pressure free movable biogas tank, belonging to the technical field of automatic control. Marsh gas pool temperature control testing device temperature controller II is connected with the constant temperature water tank, the right side of the constant-temperature water tank interface marsh gas tank through a water inlet pipe, a water outlet pipe back to the constant temperature water tank through pump, the input end of the pump is connected with the temperature controller I, a temperature probe I by marsh gas tank the upper part hole extends into the pool, marsh gas tank upper part inserting the bottle through gas tube, the gas bottle is connected with a relief port, collecting the lower part water through the pipeline, the position of the water collecting bottle is higher than the movable frame is divided into upper and lower two layers, the upper layer is a controller I, a controller II, a collecting bottle, a constant-temperature water tank suspending and fixing on the lower part of the upper-layer board, marsh gas tank is placed on the lower layer plate. This utility model claims a movable biogas pool as a control test device, which can realize automatic control, high flexibility and at the same time, it has simple structure and convenient use.
NOVELTY - A mixotrophic Scenedesmus sp. ZTY1 (CGMC 7059) is new.    USE - The Scenedesmus sp. ZTY1 is used for sewage treatment, preferably for the treatment of municipal wastewater effluent of the primary settling tank (all claimed).    ADVANTAGE - The Scenedesmus sp. ZTY1 can grow stably in actual sewage (non-sterile), is heterotrophic and environment-friendly, and can be used in effective, low cost, easy, simple and convenient sewage treatment.
NOVELTY - The sunlight utilization system has a hydrolyzing unit which disassembles electrolyte solution using sunlight energy and comprises a pair of electrode at which an optical semiconductor catalyst is supported by one side and irradiated to optical semiconductor catalyst. A gas supply section (71) has a path for supplying hydrogen and oxygen generated by disassembly of electrolyte solution with respect to gas utilization apparatuses (70). The gas supply section distributes quantity of hydrogen and oxygen according to required amount of hydrogen and oxygen of each gas utilization apparatus.    USE - Sunlight utilization system comprising gas utilization apparatus e.g. air conditioner (claimed), domestic electrical appliance, gas stove, water heater and gas air conditioner.    ADVANTAGE - Since the hydrogen and oxygen are distributed and supplied with respect to several gas utilization apparatus according to required amount of hydrogen and oxygen of each gas utilization apparatus, the hydrogen and oxygen are efficiently utilized simultaneously by several gas utilization apparatuses according to the energy needed in user lifestyle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas utilization apparatus of gas distribution control unit. (Drawing includes non-English language text)    Heat exchanger (21)    Air supply line (30)    Pressure gauges (35,36)    Gas utilization apparatus (70)    Gas supply section (71)
NOVELTY - The system (1) has an electric power supply unit which supplies electric power with respect to the electrode. A sunshine measure measuring measures the sunshine degree with respect to electrode. A switching element (82) is provided in the electric power supply line from electric power supply unit to electrode. A switch control unit switches the switching element between ON state and OFF state. The switch control unit makes variable according to the sunshine degree measured in the sunshine measure measuring unit among the switching frequency of switching element, and a duty ratio.    USE - Sunlight utilization system for hydrolyzing water into hydrogen and oxygen used for fuel cell reaction.    ADVANTAGE - The removal of generated gas and an intermediate product is performed efficiently according to the sunshine degree. The time-dependent deterioration of the performance of sunlight utilization system which hydrolyzes using photo-electrode can be suppressed effectively. The impurity is efficiently removed from the electrode according to the quantity of deposited impurity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for control method of sunlight utilization system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sunlight utilization system. (Drawing includes non-English language text)    Sunlight utilization system (1)    Hydrolyzing module (2)    Control circuit (80)    External power supply (81)    Switching element (82)
NOVELTY - Use of bacterial fertilizer including potassium, nitrogen and stomatotaxic and/or stomatophiles bacteria and having pH of 8-7.2, preferably 7, for foliar application, is claimed, where: stomatotaxic bacteria have an ability to move a phylloplane surface towards stomatal guard cells and the stomatophiles bacteria have an ability to anchor on or near the stomatal guard cells when: the nitrogen nutrition index is greater than or equal to 1; the nitrate content of stem based juice or leafstalk juice is 101-150 wt.%, preferably 120 wt.%; and/or the nitrate content of xylem sap is 6-14 moles/l, preferably 10 moles/l.    USE - The bacterial fertilizer is useful for nitrogenous reinforcement of natural killer synergy in winter crops such as winter cereals such as wheat and barley or rape oilseed. No biological data given.    ADVANTAGE - The bacterial fertilizer promotes the integration of the nitrogen cycle in protein synthesis thus improving growth rate of the crops.    DETAILED DESCRIPTION - Use of a bacterial fertilizer, comprising potassium, nitrogen and stomatotaxic and/or stomatophiles bacteria and having pH of 8-7.2, preferably 7, for foliar application, is claimed, where: stomatotaxic bacteria have an ability to move a surface of phylloplane towards the stomatal guard cells and the stomatophiles bacteria have an ability to anchor on or near the stomatal guard cells when: the nitrogen nutrition index is greater than or equal to 1; the nitrate content of stem based juice or leafstalk juice that represents a stock of ions present in the plant is 101-150 wt.%, preferably 120 wt.% of the triggering threshold value of a supplementation of nitrogen fertilizer; and/or the nitrate content of xylem sap is 6-14 moles/l, preferably 10 moles/l.
NOVELTY - Plant growth regulator is prepared by using 20-40 ml gibberellin, 250-350 g cytokinin, 20-45 g penetrating agent, 160-200 ml 50% glucose, 5-20 g red pigment, 15-30 ml 5% of 2,4-dichlorophenoxyacetic acid, 60-100 g cream cymoxanil and 5-7 kg water.    USE - The plant growth regulator is useful for preventing disease (claimed) and resisting, grafting eggplant, increasing flower of tomato and retaining fruit.    ADVANTAGE - The plant growth regulator is environmentally-friendly, and provides high yield, and producing disease free, innocuous and deformity-free high quality fruits and vegetables.
NOVELTY - Micro-storage straw feed is obtained by preparing EM bacterial stock solution to obtain activated bacterial liquid, diluting the activated bacterial liquid, obtaining fermented liquid, placing the straw in the fermentation pool to seal, uniformly adding fermentation liquid, carrying out anaerobic fermentation for 3-7 days, the adding fermentation liquid (50-70), yeast, soybean, rice and beer, uniformly mixing, drying and granulating the obtained product to obtain feed.    USE - The micro-storage straw feed is useful for breeding animals.    ADVANTAGE - The feed is cost-effective and highly nutritious.
NOVELTY - Bi-grade anaerobic fermentation device, using bi-grade anaerobic tower ferment. Fully utilize natural resource, prolific gas, improving the living rate. The main frame comprises a primary anaerobic tower, a secondary anaerobic tower, biogas concentrated tank, an aerobic filter tank, biological oxidation pond, a secondary anaerobic tower is provided with an overflow pipe, a guide two-stage anaerobic tower.
NOVELTY - This invention claims a kind of marsh gas tank, the tank body of the marsh gas tank comprises anti-seepage layer, an inner layer, an outer layer and an insulating layer, wherein the inner layer and the outer layer are formed a space is provided with an opening between the inner layer and the outer layer is sealed on the impermeable layer is fixed on the inner layer of the whole inner wall, the heat preservation layer is located at the bottom of the marsh gas tank body and/or side wall of the represented by the inner layer and the outer layer, wherein the inner layer, the outer layer is provided with a gap for a concrete layer and glass fibre reinforced plastic layer is any one of the insulating layer and the inner layer, outer layer. Compared with the existing technology, the embodiment of the inner wall of the marsh gas tank is provided with an insulating layer, so it can reduce the marsh gas pool temperature with diffusion speed, improving heat-insulating effect, which is good for fermentation and improves the producing speed and efficiency.
NOVELTY - This invention claims a kind of marsh gas tank, the tank body of the marsh gas tank comprises anti-seepage layer, an inner layer, an outer layer and a heat preservation layer, wherein the inner layer and the outer layer are formed a space is provided with an opening and connected with the inner layer and the outer layer, the said anti-seepage layer is fixed on the inner layer of the whole inner wall, the heat preservation layer is located at the bottom of the marsh gas tank body and/or the side wall of the inner layer and the outer layer of a. In addition, further comprising: a heating coil and a circulating pump, wherein the heating coil is set between the bottom of the marsh gas tank body and/or the side wall of the heat preservation layer and the inner layer, the circulating pump is connected with one end of the heating coil pipe is connected with a hot water pump in the heating coil. Compared with the existing technology, the embodiment of the inner wall of the marsh gas tank is provided with an insulating layer, so it can reduce the marsh gas pool temperature with diffusion speed, improving heat-insulating effect, which is good for fermentation and improves the producing speed and efficiency.
NOVELTY - This invention claims a kind of marsh gas pool, comprising at least two single biogas tank, wherein at least two single biogas pool the top is an arched structure, and at least two of the single space of marsh gas tank at a predetermined level as follows. Compared with the existing technology, the marsh gas the embodiment of the tank of every single marsh gas tank are provided with large volume, large because each of the tank body can be considered a single span ratio of the marsh gas tank and tank wall bearing quality of the vector of the marsh gas tank is low, reduces the construction difficulty, and can flow because of the fermentation liquid at least two single biogas tank, so it can use a set of monitoring device is capable of the marsh gas tank for feeding, discharging, liquid level, temperature, acidity-basicity monitor.
NOVELTY - This utility model claims a thermal power plant using marsh gas starting and stopping combustion and stable combustion device, belonging to the field of energy utilization technology field. Device structure is as follows: the gas production tank, fine processing device, a dryer, a compressor, an air storage tank, a booster fan, air control valve, air gun are orderly connected through pipelines, gas production tank is the other one pipeline at the bottom of the plant near residential user, air storage tank is provided with a drain valve is provided with an exhaust valve, the booster fan with a bypass, the booster fan between the compressor and an air storage tank, a gas flow booster fan and the air pipe before the mixing is equipped with a check valve, the air entering the branch, a CH4 concentration monitoring instrument and the branch and gun control valve for air to enter each device is connected to a power plant DCS system by means of hard wiring, so as to realize the monitor of whole device, an automatic control and markers in linkage disequilibrium therewith. The device is simple in structure, convenient to maintain, capable of automatically controlling and improves the efficiency of the boiler in the power plant, and reduces the energy consumption.
NOVELTY - This utility model claims a kind of energy saving biomass biogas pool, belonging to the new energy utilization technology field. Marsh gas tank is embedded underground, a bearing supporting or hanging, smoke channel is arranged outside the marsh gas tank, the smoke channel is boiler smoke passes through, so as to heat the marsh gas tank, the two sides of the smoke channel are respectively provided with a soot blowing gun, which is used for blowing the smoke channel wall and the marsh gas tank wall surface of the dust, gas passage is arranged at the bottom of the ash for discharging dust and as the maintenance opening of the smoke channel is set with a stirring the material in the marsh gas tank of the stirrer in the middle shaft of the marsh gas tank, the flue gas channel inlet and outlet part of the adjusting valve capable of adjusting the gas flow, smoke channel, the tail part of the smoke channel is provided with a boiler smoke flow provide traction power of the draught fan. This utility model has simple structure, convenient maintenance, and improves the efficiency of the boiler in the power plant, reduces the boiler chimney dust is discharged into the atmosphere, which is good for protecting environment.
NOVELTY - A horizontal anaerobic reactor and anaerobic reaction system, comprising a reactor shell body, stirring device, which is set in the reactor shell body, the axis of the stirring device is parallel to the axial line of the reactor shell, a driving device, is set at the outer side of the first end of the reactor shell body and used for driving the stirring device to rotate, feeding opening set at the upper part of the first end of the reactor shell body for conveying reactants into the reactor shell body, and a biogas residue discharging device from the reactor shell body is opposite to the first end of the second end of the lower part passes through the second end of the reactor shell body extends upwards to the outside of the reactor shell body, so that the reactant after the reaction generated biogas residue. The device can meet the wet fermentation and dry fermentation process, and can be applied to different properties of the material.
NOVELTY - This invention claims a kind of marsh gas pool discharging control system, the system comprising: a gas production for gas detector detecting a marsh gas tank with the detector output, which is used for comparing the detected output with the preset threshold value, and when the detected is less than or equal to the preset threshold value, generating the discharge signal and send to the controller of the discharge pump is set at the bottom of the marsh gas tank, connected with the controller, and the controller is used for generating the discharge signal to the biogas liquid in the marsh gas tank pump discharge pump of marsh gas tank. Compared with the existing depending on human experience, the system capable of performing quantitative analysis to control output of the marsh gas tank so that it can more accurately marsh gas generating capacity of the marsh gas tank, carrying out judgment, and when the gas generating ability, it can make the biogas in the biogas pool discharging, it is convenient to change the biogas slurry in the marsh gas tank, the output of the marsh gas tank can be continuously balancing, is convenient for the user to use the marsh gas.
NOVELTY - This invention claims a kind of marsh gas pool pH value control system, the system comprising: a set of the marsh gas tank, and is used for stirring the liquid in the marsh gas tank of the stirrer, disperse arranged in different areas in the marsh gas tank, which is used for a plurality of pH sensor detects the pH value in different areas of the biogas slurry in the biogas pool, and a plurality of the pH sensor is connected, used for making a plurality of pH sensor detects the pH value obtained by two, and comparison between any two of the pH value of the difference value and the preset pH value of the size of the first comparator, a mixer, a comparator that is connected for presetting the pH difference value when the difference value is more than between any two of the pH value, stirring to generate signal and sending it to the blending signal generation unit. With the existing technology, the system can carry out stir according to the specific condition in the marsh gas tank, the flexibility is good, it can better control the pH value in the marsh gas tank to avoid the different areas and large temperature difference;
NOVELTY - This invention claims a kind of marsh gas pool gas speed control device, wherein the device comprises: a high pressure air storage tank, air storage tank for detecting the high pressure of the gas pressure value of the gas pressure sensor and the gas pressure sensor is used for detecting the gas pressure value to the first pressure comparator to compare with the preset first pressure value, and a stirrer, a first pressure sensor, which is used for when the detection is less than or equal to the gas pressure value of the preset low pressure value, the control mixer according to the control of the stirring speed and stirring frequency. Compared with the existing technology, the device of the invention can improve the high pressure in the air storage tank of the biogas residual quantity in the state the user, ensuring the user can be continuously used.
NOVELTY - Tablet comprises medicated micropill with 34-40 mesh particle size and tableting auxiliary material, where the medicated micropill comprises sitafloxacin or its salt as active ingredient, auxiliary material and ethanol aqueous solution and the weight ratio of medicated micropill and tableting auxiliary material is 1:2-5, preferably 1:4.    USE - As tablet containing sitafloxacin (claimed).    ADVANTAGE - The tablet is stable, simple to prepare and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of above-cited tablet which involves (a) adding ethanol aqueous solution to sitafloxacin or its salt, and auxiliary material to prepare soft material, extruding and rolling to prepare medicated micropill and (b) adding auxiliary material to the obtained medicated micropill.
NOVELTY - Biological preparation of Sophora alopecuroides total alkaloid includes cleaning S. alopecuroides fruit, refluxing extracting with methanol, filtering, recovering methanol, concentrating, adjusting the pH with hydrochloric acid, standing, filtering, passing the filtrate through macroporous resin adsorption column, washing impurities, eluting to obtain total alkaloid semifinished product, recycling methanol in the eluate, concentrating and drying, passing the total alkaloid semifinished product through silica gel chromatography column, eluting, and refining.    USE - Biological preparation of S. alopecuroides total alkaloid (claimed).    ADVANTAGE - The method achieves S. alopecuroides total alkaloid of greater than 65% and high extraction purity, is convenient and fast, and has abundant raw material sources and low production cost.    DETAILED DESCRIPTION - Biological preparation of S. alopecuroides total alkaloid comprises cleaning S. alopecuroides fruit, adding 15-20 times by weight of 85-100% methanol, reflux extracting for 120-180 minutes, filtering, recovering methanol in the filtrate, concentrating to obtain concentrated liquid having 3-5 Baume, adjusting the pH with hydrochloric acid at 2.5-3, where the volume ratio of hydrochloric acid and concentrated liquid is 1:1, standing for 20-40 minutes, filtering, passing the filtrate through HPD400, HPD100, DM-130, or AB-8 macroporous resin adsorption column, washing impurities with water, washing impurities with 5-20% methanol, eluting with 50-80% methanol to obtain total alkaloid semifinished product, recycling methanol in the eluate, concentrating and drying, passing the total alkaloid semifinished product through silica gel chromatography column, eluting with acetone-methanol at 1-3:1 volume ratio, eluting with acetone-methanol at 5-7:1 volume ratio, and refining to obtain the product.
NOVELTY - The device has a sewage collecting tank (3) formed with a sewage channel (2). A regulating pool (6) is connected with a sewage pipe (5) and a stirrer (7). A bottom part of an adjusting pool (10) is connected with a conveying pump (11) that is connected with a material pipe (12). The adjusting pool is connected with a marsh gas fermentation tank that is connected with the material pipe. A sand settling channel (8) is connected with a baffle plate (9) that is provided with a grid (13). The sewage channel is provided with another grid (1).    USE - Marsh gas raw material pre-processing device for a fire-damp cooker.    ADVANTAGE - The sand settling channel is formed between a mixing tank and the adjusting pool so as to change sewage flow direction for depositing sand, thus improving mud removing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a marsh gas raw material pre-processing device.    Grids (1, 13)    Sewage channel (2)    Sewage collecting tank (3)    Sewage pipe (5)    Regulating pool (6)    Stirrer (7)    Sand settling channel (8)    Baffle plate (9)    Adjusting pool (10)    Conveying pump (11)    Material pipe (12)
NOVELTY - Wet-process production of potassium dihydrogen phosphate comprises adding phosphoric acid to phosphate rock, reacting at 30-70 degrees C for 1-3 hours, separating solid and liquid, taking filtrate to obtain desulfurized phosphoric acid; concentrating, adding potassium chloride, reacting at 60-100 degrees C; adding pH regulator, adjusting pH to 4.7-7, separating solid and liquid, taking filtrate; adding phosphoric acid, regulating pH to 3-4.7; and cooling and crystallizing, separating solid and liquid, and drying crystal.    USE - Method for producing potassium dihydrogen phosphate via wet-process (claimed).    ADVANTAGE - The method reduces corrosion of equipment and consumption of energy. It is environment-friendly.
NOVELTY - Kitchen garbage site comprehensive processing method involves grinder for cleaning hopper (1), inclined inserting pipe (2), one-way check valve (3), main pipe (5), collecting tank (6), marsh gas generator (7) and filter (4), where grinder for cleaning hopper through the inclined inserting pipe is connected with main pipeline is connected with main pipe lower end is connected with collecting tank, and main pipe upper end outlet with filter, collecting tank connected with output end of marsh gas generator through conveying pump, one-way check valve is installed on inclined inserting pipe.    USE - As kitchen garbage site comprehensive processing method (claimed), used for treatment of fragile e.g. resident, dining hall, catering enterprises.    ADVANTAGE - The kitchen garbage site comprehensive processing method is low investment, good economic benefit, and there is no environment pollution.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of kitchen garbage site comprehensive processing method.    Hopper (1)    Inclined inserting pipe (2)    One-way check valve (3)    Filter (4)    Main pipeline (5)    Collecting tank (6)    Marsh gas generator (7)
NOVELTY - This utility model claims a proliferation biological fluidized bed reactor, comprising a reactor main body, is provided with a reflowing sludge inlet, nutrient , an exhaust port on the reactor main body, a compressed air inlet and a sludge outlet, the reactor main body from the top side of the bottom layer is provided with an aeration biological domestication proliferation nutrient filling layer and fluidized bed layer, aeration layer with the reactor body to the bottom for deodorization microorganism bacterial sludge chamber, a fluidized bed layer to form a cavity, a sludge outlet and deodorizing microorganism bacterial sludge chamber, a return sludge inlet, nutrient , the air outlet are connected with the cavity in the aeration distribution layer is provided with aerator, the aerator is connected with the compressed air. This utility model is a natural microorganism purifying and deodorizing, it can make sewage processing biochemical reaction generated in the process of to the heterotrophic and capable of self-autotrophy culture, domestication, modified to advantage deodorizing microorganism flora, and can improve the dominant flora activity and proliferation thereof.
NOVELTY - Stenotrophomonas maltophilia CM-NRD3 having a preservation number of CCTCC NO: M2012455, is new.    USE - The Stenotrophomonas maltophilia is useful for denitrifying nitrogen in biological sewage (claimed).    ADVANTAGE - The Stenotrophomonas maltophilia has strong denitrification ability, and can remove the chemical oxygen demand in the sewage or water with low carbon to nitrogen ratio.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) use of Stenotrophomonas maltophilia CM-NRD3 for denitrifying nitrogen in biological sewage.
NOVELTY - Composite microbial inoculum comprises Bacillus beringensis with preservation number of China general microbiological culture collection center (CGMCC) No.6611, Rhodobacter sphaeroides with preservation number of CGMCC No.6613 and Zymomonas mobilis with preservation number of CGMCC N0.6612 in a mass ratio of 0.5-1.5:0.5-1.5:0.5-1.5.    USE - The composite microbial inoculum is useful for processing livestock and poultry waste (claimed).    ADVANTAGE - The inoculum increases protein content of waste to ensure pathogenic microbial growth with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite microbial inoculum comprising culturing the Bacillus beringensis, Rhodobacter sphaeroides and Zymomonas mobilis in a inclined plane culture medium with a pH value of 5.8-7.2 at 28-37 degrees C for 33-96 hours, storing in a refrigerator at 4 degrees C, enlarging seed culturing in 2-3 rings inclined plane of liquid culture medium, shaking the liquid seed culture to obtain bacteria liquid at 26-30 degrees C for 24-48 hours, and culturing solid seed culture in a solid expanded culture medium with an inoculation amount of 4-5% at 28-37 degrees C for 33-96 hours.
NOVELTY - Aerobic denitrifying bacteria for sewage treatment, where the strain is identified by 16S rDNA molecule as Rhodococcus erythropolis (CCTCC M 2011211), is new.    USE - The aerobic denitrifying bacteria is useful for sewage treatment to degrade nitrate nitrogen and nitrite nitrogen pollutants in water (claimed).    ADVANTAGE - The bacteria have good removal capability of nitrate nitrogen (up to 3.01 mgN/(g.L.H)) and nitrite nitrogen (up to 1.8 mgN/(g.L.H), and ensures economical denitrification method.
NOVELTY - A desulfurization system (20) has fuel supply portion (2) for supplying hydrocarbon fuel containing water and sulfur compound to back stage, and desulfurizing portion (3) for desulfurizing the hydrocarbon fuel supplied from the fuel supply portion at 150-400 degrees C using desulfurization catalyst containing nickel. The content of the water in the hydrocarbon fuel is 0.2-5 volume% with respect to total content of the hydrocarbon fuel.    USE - Desulfurization system is used for hydrogen production system for fuel cell system (all claimed).    ADVANTAGE - The fuel cell system provided with the desulfurization system has excellent desulfurization characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system (30);    (2) fuel cell system (1);    (3) desulfurization of fuel; and    (4) manufacture of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the fuel system. (Drawing includes non-English language text)    Fuel cell system (1)    Fuel supply portion (2)    Desulfurization portion (3)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - A Clostridium clariflavum CL-1 strain which is thermophilic anaerobic cellulose decomposer microbe deposited under FERM P-22178, is new.    USE - The Clostridium clariflavum CL-1 strain is useful for preparing composition for cellulose decomposition treatment; and for collecting biogas (all claimed).    ADVANTAGE - Compared with the conventional thermophilic anaerobic cellulose decomposer microbe, the Clostridium clariflavum CL-1 strain exhibits excellent cellulose decomposition process capability. The method for cellulose decomposition treatment is highly efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a method for cellulose decomposition treatment comprising contacting cellulose or a cellulose containing material, and Clostridium clariflavum CL-1 strain, along with thermophilic methane producer, at anaerobic environment of 45-65 degrees C; (2) a method for collecting biogas comprising collecting the methane gas containing biogas from the method above; and (3) a composition for a cellulose decomposition process comprising Clostridium clariflavum CL-1 strain, and thermophilic methane producer.
NOVELTY - Water-treatment method involves separating an aqueous layer containing glycerol and oil layer containing fatty acid from crude glycerol waste liquid, and denitrifying the aqueous layer using organic carbon source by biological nitrification denitrifying process in presence of heterotrophic microorganisms.    USE - Water-treatment method used for manufacture of biodiesel fuel (claimed).    ADVANTAGE - The method is carried out efficiently and economically.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of biodiesel fuel;    (2) denitrificator;    (3) manufacture of denitrificator; and    (4) water-treatment system.
NOVELTY - A fuel cell system comprises fuel generating part which generates a fuel by a chemical reaction, a fuel cell part which produces electric power using the fuel supplied from the fuel generating part, and a circulating system which forcedly circulates gas using mechanical energy between the fuel generating part and the fuel cell part. The fuel generating part is arranged between the fuel cell part and the circulating system.    USE - A fuel cell system.    ADVANTAGE - The fuel cell system has high output stabilization capability.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a fuel cell system.    Heater (4)    Container (5)    Piping (7)    Power supply (8)    Load (9)
NOVELTY - Integrated system has a flame generation unit for heating biomass and water to generate steam in the vessel. The solid content of water is processed by enzymatic hydrolysis by using enzyme and alcohol in a reactor for cleaning the biomass. A buffer solution is provided for controlling the pH during the enzymatic hydrolysis. The system also has an outlet, heat exchangers, pressure controllers and plates.    USE - Integrated system for producing ethanol (claimed).    ADVANTAGE - The integrated system enables to produce ethanol efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of ethanol, which involves preheating biomass and performing enzymatic hydrolysis of the biomass in presence of chemical or biological catalysts, and then separating lignin rich residue.
NOVELTY - The system has a solid-liquid-separation device (11) that is provided with a filter medium (13) which is immersed in an anaerobic-treatment liquid (12). A filtrate (22) is provided in a gas-liquid separator (21). A filtrate flow path (17) is connected with gaseous-phase portions (14,23) of the gas-liquid separator and filtrate extraction side of the filter medium. The gas flow paths (32,34,36) which are provided with a pressure reduction unit (31) connects to the gaseous-phase portion of the gas-liquid separator for pressure-reducing the gaseous-phase portion.    USE - Processing system of anaerobic-treatment liquid such as industrial wastewater, kitchen waste water and organic refuse generated from sewage, excrement, livestock farming excrement, foodstuff factory and paper making plant.    ADVANTAGE - Since the processing system of the anaerobic-treatment liquid can be installed compactly, the filtration of the anaerobic-treatment liquid and collection of biogas can be performed efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing method of anaerobic-treatment liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing system of anaerobic-treatment liquid.    Solid-liquid-separation device (11)    Anaerobic-treatment liquid (12)    Filter medium (13)    Gaseous-phase portion (14)    Filtrate flow path (17)    Gas-liquid separator (21)    Filtrate (22)    Gaseous-phase portion (23)    Pressure reduction unit (31)    Gas flow paths (32,34,36)
NOVELTY - Producing ethanol from lignocellulosic biomass, involves (a) pre-processing lignocellulosic biomass, (b) processing cellulose fraction obtained in process (a) with cellulose hydrolase, (c) carrying out ethanol fermentation by mixing saccharification biomass and yeast which are obtained in process (b), (d) separating solid and liquid fermented material obtained in process (c), and (e) repeating processes (a)-(d) for twice or more times, where the yeast obtained in process (d) is used as all or one portion of the yeast to-be-used in step (c) in the next cycle.    USE - The method is useful for producing ethanol from lignocellulosic biomass (claimed). The ethanol is used as biofuel.    ADVANTAGE - The method enables to mass produce ethanol from lignocellulosic biomass cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition, which comprises yeast for producing ethanol from lignocellulosic biomass, where the yeast is transformed yeast, and one, two or types of enzymes chosen from ferulic acid esterase, beta -glucosidase, beta -galactosidase, and pectinase, are expressed in the yeast.
NOVELTY - Preparing 2-(3,4-difluorophenyl)cyclopropanamine (IX) or its salt, comprises: (a1) providing 2-(3,4-difluorophenyl)cyclopropanecarbohydrazide (V); (a2) converting the hydrazide of (V) to give 2-(3,4-difluorophenyl)cyclopropanecarbonyl azide (VI); and (a3) converting (VI) to give (IX).    USE - The process is useful for preparing (IX), where (V), (A) or (B1) and (IX) are useful for preparing ticagrelor (claimed) which is useful for treating or preventing thrombotic events e.g. stroke, heart attack, acute coronary syndrome or myocardial infection with ST elevation, other coronary artery diseases and arterial thrombosis and other disorders related to platelet aggregation. No biological data given.    ADVANTAGE - The process utilizes environmentally friendly and non-explosive reagents and is industrially applicable and economical.    DETAILED DESCRIPTION - Preparing 2-(3,4-difluorophenyl)cyclopropanamine of formula (IX) or its salt, comprises: (a1) providing 2-(3,4-difluorophenyl)cyclopropanecarbohydrazide of formula (V); (a2) converting the hydrazide of (V) to give 2-(3,4-difluorophenyl)cyclopropanecarbonyl azide of formula (VI); and (a3) converting the (VI) to give (IX), where chiral center asterisk is in its (R) or (S) configuration. INDEPENDENT CLAIMS are also included for:    (1) the (1R,2R)-2-(3,4-difluorophenyl)cyclopropanecarbohydrazide (V) and their stereochemical isomeric forms;    (2) (2E)-3-(3,4-difluorophenyl)-N-methoxy-N-methylacrylamide (A) and its steriosomeric form or (1R,2R)-2-(3,4-difluorophenyl)-N-methoxy-N-methylcyclopropanecarboxamide (B1) and its steriosomeric form; and    (3) crystalline hydrochloride salt of (IX) which is 2-(3,4-difluorophenyl)cyclopropanaminium.
NOVELTY - Biological liquid fertilizer, and its preparation method are claimed. The preparation method involves using 3720 gausses of magnetic field to perform microbial acclimation for 24 hours during bacterial culture, thus the salt resistance capability and permeation resistance capability of the target microorganism are greatly increased and the target microorganism is adaptive to an environment at a total nutrient salt concentration of 15%, and compounding 15% inorganic nutrient in a biological bacterium liquid, where the total nutrient content is 15(5-0-10).    USE - As biological liquid fertilizer.    ADVANTAGE - The fertilizer has total nutrient of not less than 15%, active viable count of not less than 10 billion/ml, infectious microbe % of not greater than 15%, and quality guarantee period of not less than 18 months, reduces fertilizer investment of farmers, saves fertilization time and labor cost, increases both production and income, and is adaptive to production and application of biological organic and inorganic composite fertilizer.
NOVELTY - Purification of carotene comprises cutting Chenopodium album, cleaning, draining and drying; grinding, adding extractant, extracting, reversing flow of water in continuous dynamic flow and extracting 2 times; filtering crude extract; microfiltering, ultrafiltering to remove impurities and obtaining semi-carotene in an amount of 30% or more; concentrating under reduced pressure and recycling petroleum ether to obtain concentrated solution having a specific gravity of 1.01-112; and spray drying to 70-85 degrees C to obtain carotenoid product with more than 90% content.    USE - Method of purifying carotene (claimed).    ADVANTAGE - The method is fast, environment-friendly and mild, has no sample loss and saves solvent. The product has high purity.    DETAILED DESCRIPTION - Purification of carotene comprises cutting C. album into small pieces, cleaning, draining and drying to ash with moisture content below 5%; grinding, adding extractant, extracting using microwave countercurrent extraction, where microwave power is 300-800 watts, extraction time is 60-80 minutes and extraction temperature is 90-100 degrees C, reversing flow of water in continuous dynamic flow and extracting 2 times; filtering crude extract for 2 times; microfiltering, ultrafiltering to remove impurities, where temperature is 20-40 degrees C, pressure is 0.1-0.6 MPa, and obtaining semi-carotene in an amount of 30% or more; concentrating under reduced pressure and recycling petroleum ether to obtain concentrated solution having a specific gravity of 1.01-112; and spray drying to 70-85 degrees C to obtain carotenoid product with more than 90% content.
NOVELTY - Organic matter liquid is prepared using yeast culture solution, residual discharge liquid without Saccharomycetes, lysine fermentation broth, lysine residual discharge liquid, glutamic acid fermentation broth, acid hydrolyzed bean cake amino acid solution, acid hydrolyzed feather amino acid solution or amino acid solution of enzymolysis fish protein as raw material, where the pH value of the organic matter liquid is 3-4, the organic matter content of the organic matter liquid is 2-50%, and the chlorine element content of the organic matter liquid is 1-15%.    USE - The organic matter liquid is used as foliar fertilizer raw material (claimed).    ADVANTAGE - The organic matter liquid can replace the raw material glutamic acid fermentation mother solution of the existing fertilizer, to prepare the fertilizer in the regions in which monosodium glutamate industry is absent. The organic matter liquid improves growth of the plants.
NOVELTY - Preparation of 4-amino-1-methyl-3-n-propyl-pyrazole-5-carboxamide comprises reacting 1-methyl-3-n-propyl-pyrazole-5-carboxamide in organic solvent with fuming nitric acid or mixed acid to obtain 4-nitro-1-methyl-3-n-propyl-pyrazole-5-carboxamide; and reacting with zinc metal and ammonium salt in ionic liquid solvent.    USE - Method for preparing 4-amino-1-methyl-3-n-propyl-pyrazole-5-carboxamide (claimed).    ADVANTAGE - The method is easy to control the reaction, and has less environmental pollution. The solvent recovery can reduce cost and emissions.
NOVELTY - Preparation of sildenafil intermediate 4-amino-1-methyl-3-n-propyl-pyrazole-5-carboxamide comprises reacting 1-methyl-3-n-propyl-pyrazole-5-carboxamide and bromide in organic solvent to obtain 4-bromo-1-methyl-3-n-propyl-pyrazole-5-carboxylate; and reacting with ammonia or ammonia alcohol solution in the presence of a base.    USE - Method for preparing sildenafil intermediate 4-amino-1-methyl-3-n-propyl-pyrazole-5-carboxamide (claimed).    ADVANTAGE - The method is more efficient, environment-friendly, and suitable for industrial production.
NOVELTY - Fertilizer is prepared by (a) obtaining slurry, (b) adding concentrated sulfuric acid to dilution tank, adding water slowly to the tank to obtain diluted acid, and (c) adding the slurry obtained in step (a) to pelletizer and injecting the ammonia into the pelletizer, adding the diluted acid to the obtained product, granulating and drying the obtained product, and adding microbial inoculum to the dried product and uniformly mixing the product.    USE - As fertilizer.    ADVANTAGE - The fertilizer has excellent nitrogen fixing capacity and water conservation effect.    DETAILED DESCRIPTION - Fertilizer is prepared by (a) adding potassium hydrogen sulfate to trough and adding water to the trough and stirring the obtained product, pumping the obtained product into tubular reactor with liquid ammonia, adding urea, monoammonium phosphate and humic acid to the reactor, and stirring the obtained product with magnesium and calcium to obtain slurry, where the ratio of potassium hydrogen sulfate to liquid ammonia is 1:1.1, (b) adding 98% concentrated sulfuric acid to dilution tank, adding water slowly to the tank to obtain diluted acid, where the weight ratio of sulfuric acid and water is 2:1, and (c) adding the slurry obtained in step (a) to drum pelletizer and injecting the liquid ammonia into the pelletizer, adding the diluted acid to the obtained product, granulating and drying the obtained product, and adding microbial inoculum to the dried product and uniformly mixing the product, where the mass ratio of slurry, ammonia, diluted acid and microbial inoculum is 100:3:2:1, and the microbial inoculum comprises 3 pts. wt. Bacillus subtilis, 2 pts. wt. B.megaterium and 2 pts. wt. Azotobacter chroococcum. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves performing the above-mentioned steps.
NOVELTY - Biomass sandy soil modifying agent comprises 48.0-70.0 mass% organic matter, 0.3-0.6 mass% total nitrogen, 0.2-0.5 mass% phosphorus, 0.3-0.5 mass% potassium, 0.025-0.032 mass% hydrolyzable nitrogen, 0.092-0.11 mass% rapidly available phosphorus, and 0.18-0.22 mass% rapidly available potassium.    USE - Biomass sandy soil modifying agent.    ADVANTAGE - The biomass sandy soil modifying agent has abundant raw material resources, simple and easy production, low production cost, and no pollution and ensures no soil hardening.
NOVELTY - A biomass briquette is prepared by crushing maize straw to obtain maize straw powder, predipping powder with alkali solution, filtering, adding alkali solution, high temperature steaming, adding crushed low heat value (LHV) coal, adding coal additive, uniformly mixing with water, extrusion molding, and high-temperature drying.    USE - Method for preparing biomass briquette (claimed).    ADVANTAGE - The method improves combustion characteristics and thermal utilization.
NOVELTY - A biomass curing-forming fuel comprises 82.8-82.96 wt.% straw, 7 wt.% sawdust, 10 wt.% coal powder, 0.02-0.1 wt.% combustion promoter, 0.01-0.05 wt.% sulfur-fixing agent, and 0.01-0.05 wt.% dust-settling agent.    USE - Biomass curing-forming fuel.    ADVANTAGE - The fuel has alkanolamine compound which reduces the discharge of sulfur dioxide, and dust-settling agent which can reduce the melting point of ash. The method has high combustion efficiency, no slag, ash, black smoke and excess heat, has complete combustion, and is clean and sanitary.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass curing-forming fuel comprising removing sand and metal impurities of straw, crushing to obtain powder having grain diameter of 5-30 mm and moisture content of 20-30%, mixing straw, sawdust and coal powder to obtain mixed material, dissolving combustion promoter, sulfur-fixing agent and dust-settling agent in water, adding into mixed material, uniformly stirring and mixing to form wet material, curing for 10 minutes, forming into granular, columnar, spherical or block shape in extruding machine, drying, screening, measuring, and packaging.
NOVELTY - Healthcare product comprises 1000 pts. wt. medicinal alcohol, 6-16 pts. wt. Bletilla striata, 4-10 pts. wt. Angelica dahurica, 12-18 pts. wt. borneol, 8-12 pts. wt. camphor powder, 20-26 pts. wt. methylparaben and 4-12 pts. wt. glycerol.    USE - The healthcare product is useful in wet tissue for shortening external hemorrhoid recovery time, shortening the anus rupture healing time, alleviating pains caused by anus rupture because of dry stool and the anus pains caused by external hemorrhoids, and treating pruritus vulvae.    ADVANTAGE - The healthcare product has anus position cleaning and disinfecting efficacies, provides clean environment to patients, is convenient to use, produces no residues after use, and suitableness for all populations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the healthcare product, which involves immersing B.striata, A.dahurica and camphor powder in medicinal alcohol, standing for one month, removing residue, adding methylparaben and glycerol to obtained mixture, mixing the obtained mixture, and adding the obtained mixture in a spray bottle.
NOVELTY - Preparing wormcast-based liquid fertilizer substrate solution, involves mixing and stirring the wormcast with water according to a proper weight ratio to obtain earthworm extract mixture, inputting into surging pool, inputting oxygen to surge the earthworm extract mixture for several hours from bottom portion of the surging pool in all directions, participating insoluble impurities to the bottom portion of the surging pool after stewing, and extracting the upper clear liquid and filtering, deslagging and purifying the upper clear liquid.    USE - The method is useful for preparing wormcast-based liquid fertilizer substrate solution (claimed).    ADVANTAGE - The method is simple. The wormcast-based liquid fertilizer substrate solution prepared by the method is highly nutritious, convenient to use, and environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing wormcast-based liquid fertilizer substrate solution, involves mixing and stirring the wormcast with water according to a proper weight ratio to obtain earthworm extract mixture, inputting into surging pool, inputting oxygen to surge the earthworm extract mixture for several hours from bottom portion of the surging pool in all directions, and hence several nutrients substances in wormcast, earthworm secretions, earthworm eggs, earthworm body decomposed products and nutrient substances related to the earthworm are fully dissolved, participating insoluble impurities to the bottom portion of the surging pool after stewing, and extracting the upper clear liquid and filtering, deslagging and purifying the upper clear liquid.
NOVELTY - A grade lifting process for light-emitting diode chips with different quality marsh gas involves inoculating microalgae using super-micro-algae with photosynthetic carbon fixation ability which gradually fixes carbon dioxide in marsh gas to reactor using biogas as culture medium in which biogas slurry is fermented biogas slurry, carrying intake air quality parameter test gas such as methane and carbon dioxide with high volume ratio, absorbing a part of carbon dioxide to methane using lime water pre-processing gas, and controlling marsh gas residence in the reactor using light source.    USE - Grade lifting process for light-emitting diode chips with different quality marsh gas.    ADVANTAGE - Grade of the marsh gas is improved. The method has strong practicability, high economic benefit, simple and easy and convenient operation.    DETAILED DESCRIPTION - A grade lifting process for light-emitting diode chips with different quality marsh gas involves inoculating microalgae using super-micro-algae with photosynthetic carbon fixation ability which gradually fixes carbon dioxide in marsh gas to reactor using biogas as culture medium in which biogas slurry is fermented biogas slurry, carrying intake air quality parameter test gas such as methane and carbon dioxide with high volume ratio, absorbing a part of carbon dioxide to methane using lime water pre-processing gas, controlling marsh gas residence in the reactor using light source to light until the stationary phase to micro-algae growth, inoculating the proliferated microalgae to reactor, controlling upper level of marsh gas entering into the reactor using air valve, and repeating the steps.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro-algae biogas lift grade of the multilevel series connection type photoreactor system. (Drawing includes non-English language text).
NOVELTY - Preparation of fenchone comprises providing 75% fenchol having a concentration of 95-98%, 3% dehydrogenation catalyst, 16% xylene, 4% acetic anhydride, and 3% sulfuric acid.    USE - Preparation of fenchone (claimed) used for preparing chiral medicine, pesticide, industrial paint, vinyl resin, and acrylic resin.    ADVANTAGE - The method uses more than 95% purity fenchol as raw material and recyclable solvent, has high conversion rate and environmental protection, saves cost, and provides product with antibacterial, sterilizing, and insecticidal activity.
NOVELTY - Method involves removing dyes contaminants from wastewater obtained in textile refining process by using microbial consortium comprising fungus Trametes versicolor and bacteria Pseudomonas putida. A multi-agency system and metabolic model are designed and coupled with multispecies microbial consortia, where crops are selected for determination of growth conditions. Bleaching and enzyme activities processes are performed with maintain parameters and evaluation of bleaching tests.    USE - Method for degradation of acid red 27 dye for use in wastewater and contaminated soil treatment and biotechnology field, such as development of clinical diagnostic system, production of biopharmaceuticals, nutraceuticals, biofuels, biocosmetic, biopolymer and obtaining metabolic products of plant cell cultures and animal cells.
NOVELTY - A bioenergetic installation comprises receiving container with device of mixing initial feedstock, connected through delivery pump with methan-tanks, gas holders for storing biogas and line of its withdrawal, crusher-paste former of solid organic waste, device for hydro-wave processing of drains and effluent, methan-tank filter, and device is equipped by electronic control unit.    USE - As bioenergetic installation (claimed).    DETAILED DESCRIPTION - A bioenergetic installation comprises receiving container with device of mixing initial feedstock, connected through delivery pump with methan-tanks, gas holders for storing biogas and line of its withdrawal, crusher-paste former of solid organic waste, device for hydro-wave processing of drains and effluent, methan-tank filter, and device is equipped by electronic control unit. Where the installation has at least two methan-tanks with built-in each of them mixers, the gas holder and a tints from the container of effluent, which has complete cycle of digested, where receiving container and installation for thickening of drains and effluent are made by two-section, and the receiving section of container has device for introducing the accelerators of methane digested, furthermore, installation supplied with connected with the methan-tank filter for cleaning effluent from the ammonia, where device is equipped by the electronic control unit, connected electrically to the crusher-paste former, by mixers, with the device for introduction of the accelerators of methane infusions.
NOVELTY - The hydrogen generating system (100) has a supply unit (118), coupled to gas filter (106), which is configured to supply generated hydrogen and oxygen to an internal combustion engine. A first ceramic filter (116) is coupled to supply unit and a second ceramic filter (114) is coupled between the gas filter and a reaction container (102), consisting of electrolyte solution containing potassium hydroxide. The first ceramic filter and the second ceramic filter are made up of at least one material selected from the group comprising inorganic, non-metallic, crystalline oxide nitride and carbide.    USE - Hydrogen generating system for internal combustion engine of vehicle.    ADVANTAGE - Enhances the flame velocity and permits the engine to operate with leaner fuel mixtures since the generated gas is filtered and supplied to an internal combustion engine of the vehicle along with a hydrocarbon fuel. Increases the efficiency of the engine and reducing harmful gas emissions from the engine by enhancing the flame velocity and permits the engine to operate with leaner fuel mixtures. Allows the generated gas to pass though the pores but prevents fire from passing through the pores by using the ceramic filter walls. Provides a uniform flow of gas to the internal combustion engine and reduces the load on the vehicle battery by utilizing only a 3 volt direct current supply. Prevents backfire by providing a safety feature for the vehicle. Provides an easy to install and cost effective system which do not require changes to be made in the vehicle by using the ceramic filters.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the system for generating hydrogen and oxygen.    Hydrogen generating system (100)    Reaction container (102)    Gas filter (106)    Second ceramic filter (114)    First ceramic filter (116)    Supply unit (118)
NOVELTY - The bimetallic catalyst comprises a platinum and palladium in atomic ratio of 1:3. Support is provided, which has sulfur content.    USE - Bimetallic catalyst for sulfated zirconium oxide.    ADVANTAGE - The bimetallic catalyst ensures high complete dechlorination of chlorinated compounds.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for preparing bimetallic catalyst for platinum and palladium supported on sulfated zirconium oxide; and    (2) a hydrodechlorination process for chloromethane, which involves using gas stream.
NOVELTY - Converting Galilee basin coal to methanol in or near to the Galilee basin and pipelined to the Gulf of Carpentaria for loading into and export in bulk liquid carriers for ultimate use in methanol-to-power systems involves processing known means; and reacting carbon dioxide (CO2) which is released in the coal-to-methanol process, and hydrogen which is produced by known solar energy-based means, to produce additional methanol for shipment from the Gulf of Carpentaria.    USE - The process is useful for converting Galilee basin coal to methanol in or near to the Galilee basin and pipelined to the Gulf of Carpentaria for loading into and export in bulk liquid carriers for ultimate use in methanol-to-power systems (claimed).    ADVANTAGE - The process eliminates the need to ship Galilee Basin coal through the Great Barrier Reef; and provides a shorter shipping distance to premium Asian markets for Galilee Basin coal and solar-based energy.
NOVELTY - The tube (300) has a tube main portion (100) and a conductive medium. A hole is provided in one side of the tube main portion. A membrane is provided to surround a hole. The membrane is provided to block the water molecule. A catalyzed electrode material is provided in the hole. The electrode material is provided with the platinum, palladium, ruthenium, iridium, cobalt molybdenum and cobalt molybdenum alloy.    USE - Tube for collecting hydrogen, used in device for splitting water (claimed).    ADVANTAGE - Since the gap between the hydrogen electrode and the photoelectrode is removed, the membrane area is reduced. The carrier of the electron generated in the photoelectrode on the transparent conductivity glass is collected smoothly. The photoelectric conversion efficiency of the hydrogen collecting tube is improved. Since the light well reaches the photoactive surface of the photoelectrode, the hydrolysis efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for splitting water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for splitting water.    Device for splitting water (10)    Tube main portion (100)    Tube for collecting hydrogen (300)
NOVELTY - Preparation of diafenthiuron comprises reacting 2,6-diisopropyl-4-phenoxyaniline and phosgene in the presence of calcium carbonate, reacting obtained N-(2,6-diisopropyl-4-phenoxyphenyl)isocyanate with tert-butylamine, and reacting obtained 3-(2,6-diisopropyl-4-phenoxylphenyl)-1-tert-butyl urea with phosphorus pentasulfide in the presence of potassium carbonate.    USE - Process for preparing diafenthiuron (claimed) used as insecticide and acaricide.    ADVANTAGE - The process is simple and has mild reaction conditions, inexpensive raw materials and low toxicity.
NOVELTY - A kind of food garbage processing device, wherein it is as follows: it comprises a pouring pool, food grinder, a pressurizing water tank, centrifugal solid-liquid separation device, an oil-water separating device for food and drink garbage entering the food grinder by pouring tank, crushing by a pressurized water tank to the centrifugal solid-liquid separation device, and carrying out solid-liquid separation, the liquid is conveyed to the separating barrel oil-water separating device, an oil-water separation device by the second pressing water tank is provided with a third probe for detecting the liquid level, which respectively are used for the first probe controls the water control valve is opened, and a second probe controlling the oil pump for controlling the water outlet control valve is closed and the third probe oil gas pump is stopped, oil-water separating in the separating barrel. It can make the oil in food waste is separated from the food waste oil into fuel, so as to solve the problem of oil on the source, at the same time reducing water system pressure, increases the energy utilization rate and protect the environment.
NOVELTY - Producing hydrogen using waste glycerol (crude glycerol), comprises culturing a facultative anaerobe in an aerobic condition, fixing the facultative anaerobe in an immobilized carrier, and culturing the immobilized facultative anaerobe in a culture medium including waste glycerol in an anaerobic condition.    USE - The method is useful for producing hydrogen using waste glycerol such as crude glycerol (claimed), where the hydrogen is useful for production of biodiesel.    ADVANTAGE - The method ensures efficient, convenient, rapid and easy production of hydrogen with increased yield and without environmental pollution.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a method for producing hydrogen using waste glycerol (Drawing includes non-English language text).
NOVELTY - Producing breathing slender bamboo tube type bar organic fertilizer, involves collecting livestock excretions organic compound and food waste organic compound, dehydrating moisture in the livestock excretions and food waste and drying mixture, pulverizing dried mixture, mixing the organic substance in first mixing tank and drying the mixture, pulverizing the dried mixture, mixing deodorizing agent, heating the mixture, adding alive microorganism fermenting agent, and maturing the mixture, and analyzing and determining production components of the organic fertilizer.    USE - The method is useful for producing breathing slender bamboo tube type bar organic fertilizer using live stock excretion and food waste, which is used for supplying nutritious oxygen to plants.    ADVANTAGE - The method enables to produce breathing slender bamboo tube type bar organic fertilizer is environmentally-friendly.    DETAILED DESCRIPTION - Method of producing breathing slender bamboo tube type bar organic fertilizer, involves removing metals using magnet and removing plastic vinyl using filtering sieve and wind force to collect livestock excretions organic compound and food waste organic compound and to select first harmful material, dehydrating moisture in the livestock excretions and food waste and drying in first drying furnace, pulverizing dried mixture, mixing the organic substance without moisture in first mixing tank and drying the mixture, pulverizing the dried mixture, mixing deodorizing agent (zeolite, yellow soil powder, and activated charcoal) to remove harmful smell, and making moisture of 10-30% or less with the dried mixture, heating the mixture to sterilizes harmful smell and bacteria, decreasing the temperature to 50 degrees C, adding alive microorganism fermenting agent, and maturing the mixture for 5 days, and analyzing and determining production components of the organic fertilizer.
NOVELTY - The pyrolysis device has a feeding hopper and a buffer hopper that are equipped in a load cell. A transfer conveyor is provided for transferring an organic waste chip from a chip storage compartment. The organic waste is stored in an oil collection tank with a fixed quantity. Carbon residue (78) of carbon residue processing unit is thermally decomposed in a pyrolyzing furnace (53). A scraper apparatus is installed to remove the adhered adhesive with the thermally decomposed organic waste chip.    USE - Pyrolysis device of organic waste.    ADVANTAGE - Since the scraper apparatus is installed to remove adhered adhesive with organic waste chip thermally decomposed in pyrolyzing furnace, the thermal cracking of chip and accident including the explosion and fire can be prevented. Thus, the protection and safety of pyrolysis device can be improved. The carbon residue of organic waste can be recycled effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon residue processing unit.    Pyrolyzing furnace (53)    Carbon residue (78)    Damper (90,91)    Magnetic stripe (92)    Supply pipe (99)
NOVELTY - The device has an air channel (13) matched with a fuel gas outlet (10). A lower air channel (5) is matched with a feeding port (4). The air channel is formed with an upper air channel (12) and the lower air channel. The lower air channel is matched with upper and lower positions of a hearth (2). A governing air outlet (3) is annularly formed at a periphery of the feeding port. The upper air channel and the governing air outlet are formed in a nozzle.    USE - Biomass gasification furnace positive and negative bidirectional air inlet device.    ADVANTAGE - The device controls temperature of the hearth.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace positive and negative bidirectional air inlet device.    Hearth (2)    Governing air outlet (3)    Feeding port (4)    Lower air channel (5)    Fuel gas outlet (10)    Upper air channel (12)    Air channel (13)
NOVELTY - Producing 99.99999% optoelectronic-grade ultra-pure ammonia from 99.9% industrial liquid ammonia using three-tower rectification method, is claimed.    USE - The method is useful for producing 99.99999% optoelectronic-grade ultra-pure ammonia from 99.9% industrial liquid ammonia using three-tower rectification method (claimed).    ADVANTAGE - The method is environmentally friendly, and obtains ultra-pure ammonia, which meets the optoelectronic semiconductor epitaxial requirements.
NOVELTY - Preparing potassium from biomass fuel boiler ash comprises: adding water into the biomass fuel boiler ash, sufficiently stirring the mixture until a leachate is up to the weight of over 1.2 g/ml, filtering slurry to obtain the leachate and ash, and then carrying out solid-liquid separation on the leachate to obtain a transparent solution; (ii) neutralizing the solution, then, stirring the solution, concentrating and crystallizing the solution; and centrifugally dehydrating the solution until the content of crystals is smaller than 5%, and finally crushing the crystals.    USE - The method is useful for preparing potassium from biomass fuel boiler ash (claimed).    ADVANTAGE - The potassium salt is produced by utilizing the waste acid and the biomass fuel boiler ash so that the waste is recycled, and the environment pollution is reduced. The method has reliable and sufficient raw material source, low production cost, small investment, rapid effect, convenience for popularization and high production benefit; is simple, reduces the technical control step, and is easy to control; and adopts closed type production so that the environment is not polluted.    DETAILED DESCRIPTION - Preparing potassium from biomass fuel boiler ash comprises: adding water into the biomass fuel boiler ash in the mass ratio of 1:1.5-2.4, sufficiently stirring the mixture for 2-4 hours until a leachate is up to the weight of over 1.2 g/ml, filtering slurry to obtain the leachate and ash, and then carrying out solid-liquid separation on the leachate to obtain a transparent solution; (ii) neutralizing the solution by using waste acid with the mass concentration of 9-92% until the pH value is 2-6, then, stirring the solution for 10-20 minutes, and then, concentrating and crystallizing the solution; and centrifugally dehydrating the solution until the content of crystals is smaller than 5%, and finally crushing the crystals to 50-200 meshes.
NOVELTY - Treating sludge comprises: adding 75-90% of sludge water content into a reaction kettle, injecting saturated steam in the sludge at a pressure of 1.5-2.5 MPa and a temperature of 150-185 degrees C, and keeping the solution for 0-25 minutes and the performing thermal hydrolysis on the sludge; carrying out mechanical dewatering on the sludge using a removing solvent and a cement cake to obtain a dehydrated sludge; and performing anaerobic digestion on the solution with a liquid marsh gas.    USE - The method is useful for treating sludge of organic solid waste.    ADVANTAGE - The method is capable of treating sludge with less energy consumption in an economic manner.
NOVELTY - Preparation of (8S,13S,14S,17R)-13-methyl-17-(2-methyl-1,3-dioxolan-2-yl)-1,2,4,6,7,8,12,13,14,15,16,17-dodecahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolan)-17-ol (ulipristal acetate) involves: reacting (8S,13S,14S)-13-methyl-1,2,6,7,8,12,13,14,15,16-decahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolan)-17(4H)-one (II) with trimethylsilyl, followed by reacting with methyl Grignard reagent in presence of hydrochloric acid, and then with ethane-1,2-diol in presence of p-toluene sulfonic acid and a catalyst.    USE - In preparing (8S,13S,14S,17R)-13-methyl-17-(2-methyl-1,3-dioxolan-2-yl)-1,2,4,6,7,8,12,13,14,15,16,17-dodecahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolan)-17-ol (ulipristal acetate) (claimed).    ADVANTAGE - The process is simple, easy to control reaction condition, provides ulipristal acetate with high yield, and is environmental-friendly.    DETAILED DESCRIPTION - Preparation of (8S,13S,14S,17R)-13-methyl-17-(2-methyl-1,3-dioxolan-2-yl)-1,2,4,6,7,8,12,13,14,15,16,17-dodecahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolan)-17-ol (ulipristal acetate) involves: reacting (8S,13S,14S)-13-methyl-1,2,6,7,8,12,13,14,15,16-decahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolan)-17(4H)-one (II) with trimethylsilyl in presence of Lewis acid or inorganic alkali, to obtain (8S,13S,14S,17R)-13-methyl-17-(trimethylsilyloxy)-1,2,4,6,7,8,12,13,14,15,16,17-dodecahydrospiro(cyclopenta(a)phenanthrene-3,2'-(1,3)dioxolane)-17-carbonitrile (III); reacting the compound (III) with methyl Grignard reagent in presence of hydrochloric acid, to obtain (8S,13S,14S,17R)-17-acetyl-17-hydroxy-13-methyl-4,6,7,8,12,13,14,15,16,17-decahydro-1H-cyclopenta(a)phenanthren-3(2H)-one (IV); and reacting the compound (IV) with ethane-1,2-diol in presence of p-toluene sulfonic acid and a catalyst to obtain the ulipristal acetate.
NOVELTY - Manufacture of solid charcoal in compression molding mode involves using raw materials containing fuel wood, shrubs, branches, bark, wood processing residuums or discarded artificial boards, which do not need to be smash and are directly formed through a pressing machine in a mold pressing mode, heating the pressed materials and a mold for carbonization in a carbonizing furnace, carbonizing the pressed materials in the mold, cooling, and demolding.    USE - Manufacture of solid charcoal in compression molding mode (claimed).    ADVANTAGE - The method enables economical manufacture of solid charcoal in compression molding mode with high yield and charcoal obtaining rate in a short period of time by carbonizing process hot condition and anaerobic condition.
NOVELTY - Bamboo or processing residue of bamboo which is not smashed is directly formed through pressing machine by mold pressing mode, pressed materials and mold are carbonized in carbonizing furnace by heating, pressed materials are carbonized in mold and subjected to cooling demolding, to obtain solid bamboo charcoal.    USE - Manufacture of solid bamboo charcoal (claimed).    ADVANTAGE - The method enables manufacture of solid bamboo charcoal by resisting internal stress produced by pressing materials and expansibility produced by heating, and by providing heat transfer and oxygen-free combustion needed by the carbonizing process.
NOVELTY - Straw raw material is pressed by mold pressing without smashing, straw and mold are heated, supplied into carbonization furnace, carbonized and subjected to cooling and demolding, to obtain straw carbon.    USE - Manufacture of straw carbon (claimed).    ADVANTAGE - The method enables preparation of straw carbon by resisting internal stress generated from pressing of the straw and expansive force generated from follow-up heating, and by providing required heat transfer and oxygen-free burning.
NOVELTY - The pyrolysis device has furnace cover (3) that is arranged at top of hearth (2). An air outlet (101) communicated with the hearth, is formed in furnace main portion (1). A heat collector (4) is arranged around the hearth. A water inlet (401) and a water outlet (402) of the heat collector are made to penetrate the furnace main portion, and are connected with water storage buffer tank (5) of heat supply system. A carbon outlet (102) is provided at bottom of the furnace main portion. A distributor (7) is arranged on hearth, and is connected with motor which is arranged on furnace cover.    USE - Multifunctional pyrolysis device of agriculture waste source pyrolytic carbon gasification comprehensive conversion system.    ADVANTAGE - The pyrolysis device is provided with simple structure and low maintenance cost. Since excess heat produced by pyrolysis is transmitted to heat supply system through heat collector to supply hot water to user, heat utilization ratio of the pyrolysis device is improved. The production efficiency of pyrolysis device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional pyrolysis device of agriculture waste source pyrolytic carbon gasification comprehensive conversion system.    Furnace main portion (1)    Hearth (2)    Furnace cover (3)    Heat collector (4)    Water storage buffer tank (5)    Distributor (7)    Air outlet (101)    Carbon outlet (102)    Water inlet (401)    Water outlet (402)
NOVELTY - A Bacillus amyloliquefaciens strain (S1) preserved under preservation number (CGMCC NO: 5436) is new.    USE - In the preparation of medicine for inhibiting plant pathogenic bacteria, where the plant pathogenic bacteria comprises fruit rot bacteria, potato early blight bacteria, cabbage black spot disease bacteria, cotton verticillium, apple rot, apple wheel thread pathogenic bacteria, and apple leaf disease bacteria; and for the preparation of bacterial fertilizer (claimed).    ADVANTAGE - Clinical study shows that, the present Bacillus amyloliquefaciens strain provides greater than or equal to 50% peanut fruit rot control effect, and increases 10-20% emergence rate. The Bacillus amyloliquefaciens strain has a growth-promoting effect; and provides fertilizer which is less toxic and non-pathogenic for human and animal, does not pollute the environment and has low production cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a bacterial fertilizer comprising the strain (S1) and adjuvant;    (2) preparation of bacterial fertilizer involving placing strain (S1) in potato glucose liquid culture medium at temperature of 30-37 degrees C and stirring speed of 200-220 rpm for 12-16 hours to obtain first culture; putting first culture in potato glucose liquid culture medium at temperature of 30-37 degrees C, and stirring speed of 200-220 rpm for 22-26 hours to obtain second culture; transferring second culture to solid fermentation culture medium, shaking at 30-37 degrees C for 120-160 hours to obtain product, where the solid fermenting culture medium comprises 26-30 parts by weight (pts. wt.) wheat bran, 7-9 pts. wt. cotton seed skin, 2.5-4 pts. wt. peanut cake powder, and 40-45 pts. wt. water.
NOVELTY - A Pseudomonas fluorescens ZJB09-108 strain (S1) preserved in the China Centre for Type Culture Collection, under preservation number (CCTCC No: M2012539), is new.    USE - As catalytic agent for preparing trans-4-(aminomethyl)cyclohexanecarboxylic acid (claimed) which is used in the toothpaste for preventing gingival bleeding.    ADVANTAGE - The fluorescent Pseudomonas fluorescens ZJB09-108 strain provides mild synthesis reaction condition; provides simple and environment-friendly preparation of trans-4-(aminomethyl)cyclohexanecarboxylic acid; and also provides trans-4-(aminomethyl)cyclohexanecarboxylic acid having good application prospect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing trans-4-(aminomethyl)cyclohexanecarboxylic acid by using the strain (S1) as catalytic agent involving inoculating strain (S1) in slant culture medium at 2-37 degrees C for 2-48 hours to obtain slant strain, where the slant culture medium comprises 5 g/l beef extract, 15 g/l peptone, 3-10 g/l NaCl, 15-20 g/l agar and water as solvent, where the initial pH is 6.5-8; inoculating obtained slant strain into seed culture medium at 25-37 degrees C for 18-20 hours to obtain seed liquid, where the seed culture medium comprises 5 g/l beef extract, 1-20 g/l starch, 1-20 g/l glucose, 1-20 g/l glycerol, 1-15 g/l peptone, 3-10 g/l NaCl, 0.5-2 g/l K2HPO4.3H20, and water as solvent, where the initial pH is 6.5-8; and adding obtained seed liquid into the fermentation medium, and fermenting at 25-37 degrees C for 18-48 hours, centrifuging obtained culture solution, washing, collecting wet cells, where the fermentation medium comprises 5 g/l beef extract, 20 g/l starch, 20 g/l glucose, 20 g/l glycerol, 1-15 g/l peptone, 3-10 g/l NaCl, 0.5-2 g/l K2HPO4.3H20, and water as solvent, where the initial pH is 6.5-8.
NOVELTY - The method involves oxidizing a pulverized coal slurry by adopting an oxidizing agent to generate carbon dioxide. A filter is utilized for filtering the carbon dioxide from coal. An anode chamber is connected with an electrochemical reaction tank. The anode chamber is connected with the filter. The filter is connected with the electrochemical reaction tank. The anode chamber is connected with a liquid storage tank. The oxidizing agent is added with the coal. A sulfonic acid proton exchange film is connected with the electrochemical reaction tank.    USE - Method for producing pure hydrogen and carbon dioxide from coals.    ADVANTAGE - The method enables prolonging the service life of an electrolysis reactor, reducing manufacturing cost and preventing an environment from being polluted.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an electrochemical reaction tank.
NOVELTY - The heater has a slag chamber and a pipe component connected with a first main combustion chamber. The main combustion chamber is connected with a cylindrical section of a gasification chamber. The gasification chamber is fixed with a reverse cone. The gasification chamber is formed with a gasification chamber gas-distributing hole. A pipeline is connected with a second main combustion chamber. A third combustion chamber is fixed on an inverted conical section of air holes. An outer wall of the first main combustion chamber is provided with heat conducting fins.    USE - High-efficient biomass fuel water heater. Uses include but are not limited to a coal production industry, a school, a hotel, a hospital and a cell.    ADVANTAGE - The heater has scientific and reasonable structure, and is sulfur-free and non- toxic.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high-efficient biomass fuel water heater.
NOVELTY - The utility model claims a biomass gasification furnace, comprising a furnace body, a furnace cover, an air inlet and an air outlet, wherein the furnace is covered on the upper end of the furnace body, the air inlet and air outlet is set on the furnace body, and connected with the inner cavity of the furnace body, the diameter of the middle section of the furnace body is connected to the middle section of the furnace body is less than the diameter of the upper section and the lower section, the air inlet, the air outlet is connected at the lower section of the furnace body, the furnace body from top to bottom in turn is provided with a drying area, area above the combustion zone, reducing zone and gray area, a drying area, area, a combustion area, reducing zone are set on fire grate, a fire grate and a gray area, the air inlet pipe is connected with the burning area, the air inlet pipe is set on the upper part of the air outlet pipe, reduces the generation of tar in the furnace body, preventing pipe blockage caused by stopping repair, improves the working efficiency, and the air inlet pipe and the combustion area and improve the burning efficiency of the interior material, increases the combustion temperature in the furnace body, improves the practicability.
NOVELTY - The tower has a biomass raw material storage tank (1), drying section, distillation section, cooling chamber (6) and flue gas treatment system. The drying section has an upper drying tower (2) and lower drying tower (3). The distillation section has upper distillation tower (4) and lower distillation tower (5). The storage tank, upper and lower drying towers, upper and lower distillation towers and cooling chamber are arranged orderly from top to bottom. The flue gas treatment system is connected with the air inlet and air outlet of drying section and distilling section.    USE - Groove-type horizontal cross-flow biomass destructive distillation tower.    ADVANTAGE - The distillation tower with high production rate, high heat energy utilization rate and small equipment volume enables direct heating mode and indirect heating mode. The distillation tower is made of heat-resisting material, so that corrosion is prevented and long service life is achieved with low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using groove-type horizontal cross-flow biomass destructive distillation tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the groove-type horizontal cross-flow biomass destructive distillation tower. (Drawing includes non-English language text)    Biomass raw material storage tank (1)    Upper drying tower (2)    Lower drying tower (3)    Upper distillation tower (4)    Lower distillation tower (5)    Cooling chamber (6)
NOVELTY - The device has a container formed with an air inlet and an air outlet that are respectively matched with upper parts of a washing chamber and a gas-liquid separating chamber. The container is filled with purifying solvent. The upper part of the washing chamber is provided with a spraying head that is fixed with a bottom part of the container. A gas conveying pipe is fixed with the upper part of the washing chamber. The gas-liquid separating chamber is connected with the conveying pipe. Two gas flow baffle plates are respectively arranged at two sides of the gas-liquid separating chamber.    USE - Purifying device for an agricultural waste resource pyrolysis gasification system.    ADVANTAGE - The device is compact in structure, and has high resistivity, and realizes washing and gas-liquid separating processes and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a purifying device.
NOVELTY - A hot charcoal plastics molding raw materials comprising fuel wood, shrubs, branches, bark, wood processing residue or waste artificial board with alkali lignin bi-components, is subjected to hot forming by hot compression plasticizing molding, resulted materials are cut into required specifications using saws, supplied into carbonization furnace, carbonized and cooled, to obtain hot compression plasticizing molding charcoal.    USE - Molding of hot charcoal plastics molding (claimed).    ADVANTAGE - The method enables preparation of hot plastics molded charcoal having high heat value.
NOVELTY - A biomass gasification furnace ash discharge device, comprising a gate, a gate and a control motor, the upper gate connected to biomass gasification furnace ash outlet, the lower gate is provided with a tapered funnel, a conical hopper is inclined, a conical funnel large-calibre end is located on a gate lower part, small caliber end is inserted into water tank; between the upper gate and the lower gate is provided with memory cinder box, the upper box is provided with ash discharging port, wherein the control motor through the gate on the upper part pull rod is connected with the gate through a connecting rod. This utility model has simple structure, high degree of automation, the efficiency is high, the ash is ash will not cause the working environment pollution, ensure the ash will not leak under anaerobic condition gasification furnace combustion efficiency is high and further improve the gasification furnace gasification effect.
NOVELTY - An air inlet device of biomass gasification furnace, comprising a gasification furnace, a burner, on the side wall of the gasification furnace is welded with air inlet pipe, the air inlet pipe protruding through the furnace body centre, the upper part is air inlet pipe of the furnace body is provided with multiple blowing from the left to the right, one end of the furnace body is provided with a protruding buckle cover and the other end is connected with an air blower, the air inlet pipe of the blower is connected to the end of the upper part of the branch pipe. When the utility model ensures combustion oxygen adequately, which greatly improves the fuel utilization rate, and is simple in structure, safe and reliable, convenient to use, and it is very suitable for popularization and application for vast rural areas.
NOVELTY - Biodiesel is prepared by stirring sodium hydroxide (NaOH) and/or potassium hydroxide (KOH) in ethanol and mixing animal fat and plant oil to obtain uniform transparent homogeneous system, adding methanol, performing transesterification reaction, and synthesizing potassium fatty acid ethyl esters.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - Preparation of biodiesel is simple and has quick reaction, low production cost, low energy consumption, and high oil conversion rate.
NOVELTY - Invention relates to biotechnology and bioenergy and can be used in recycling livestock wastes and for producing biogas. The biogas apparatus has a vessel for preparing starting material, a pipe for feeding the prepared mass, a pump for feeding material, a pipe for removing the obtained sludge, a vessel for spent substrate, a system for treating, collecting, storing and processing biogas and a bioreactor, having at least three cylindrical concentrically arranged vessels: an outer vessel for conducting a psychrophilic step of anaerobic fermentation of the biomass, a middle vessel for the mesophilic step of fermentation and a central vessel for the thermophilic step of fermentation. The outer and middle vessels are linked to each other in the bottom part, and the middle and central vessels are linked to each other in the top part. The apparatus if equipped with a microwave radiator with radiation frequency of 2450 MHz, placed in the central vessel of the bioreactor such that it enables metered and uniform heating of the biomass on its entire volume. A bladed mixer is installed in each of the outer and central vessels.    USE - Chemistry.    ADVANTAGE - Invention provides uniform heating on the entire volume of a bioreactor, high degree of decomposition of biological wastes and high output of biogas.1 dwg
NOVELTY - Preparation of sulbenicillin sodium involves condensing sulfophenylacetic acid and acyl chloride to generate mixed anhydride, condensing the mixed anhydride and protected 6-APA under an anhydrous condition, de-protecting, obtaining sulbenicillin acid, reacting the obtained sulbenicillin acid with sodium isooctoate, obtaining salt, and crystallizing. The purity of sulbenicillin sodium is more than 99.2%.    USE - Preparation of sulbenicillin sodium (claimed).    ADVANTAGE - The sulbenicillin sodium is economically and efficiently prepared with high yield without polluting the environment, by a simple method.
NOVELTY - A kind of efficient oxygen generator, comprising a closed shell (4), wherein the shell (1) is provided with a water inlet (7), the upper part of the hydrogen-oxygen output port (6) and a safety valve (5), the shell (1) along the vertical direction is provided with more than one of the large sleeve (1), a big sleeve (1) is coaxially provided with a small sleeve of electrically conductive material that is, large sleeve (1) and the small sleeve are respectively provided with a plurality of through-hole, the big sleeve (1) passes through the first electrode leads and electric control device and the direct current power supply is electrically connected with the small sleeve passes through the other end of the first electrode lead and an electric control device with the direct current power supply is electrically connected with the shell (1) is located in the big sleeve (1) is provided with a magnetic rod along the vertical direction (2), and the magnetic rod (2) is wound with an electromagnetic coil, the electromagnetic coil and the electromagnetic frequency generator (3) electrically connected with each other. The purpose is to provide a kind of small volume, capable of being mounted on a vehicle with limited space place, generating efficiency is high for efficient hydrogen-oxygen generator.
NOVELTY - The ultrasonic atomizing device has a mist condensation device that is composed of a vibrator (17a,17b) and a piston (12). The cylinder is divided into compression cylinders (11a,11b). A material outlet (14,16) and material inlet (7,9) are provided in the each compression cylinder. The material inlets of condensation device are connected with ultrasonic atomizing tank (2). The material outlets of condensation device are communicated with an inlet of the collector. The two compression cylinders alternatively compress ethanol and discharge ethanol to collector (19).    USE - Ultrasonic atomizing device for producing fuel ethanol.    ADVANTAGE - The mist recovery efficiency is improved. The structure of the ultrasonic atomizing device is simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ultrasonic atomizing method for producing fuel ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ultrasonic atomizing device for producing fuel ethanol.    Ultrasonic atomizing tank (2)    Material inlet of compression cylinders (7,9)    Compression cylinders (11a,11b)    Piston (12)    Material outlets of compression cylinders (14,16)    Vibrators (17a,17b)    Collector (19)
NOVELTY - The method involves adapting biological oil as raw material oil. The raw material oil and hydrogen are mixed under hydrogenation condition, to be passed through first stage hydrogenation reaction zone. The hydrogen-rich gas separated from stream generated by hydrogenation is recycled. The separated liquid is entered into second stage hydrogenation modification reaction zone. The sub-hydrogen gas separated from oil generated by second stage hydrogenation is recycled. The separated liquid product is subjected to fractionation to obtain naphtha and low freezing point motor fuel.    USE - Hydrogenation method for producing low freezing point motor fuel from biological oil e.g. vegetable oil such as soybean oil, peanut oil, castor oil, rapeseed oil, corn oil, olive oil, palm oil, coconut oil, tung oil, linseed oil, sesame oil, cotton seed oil, sunflower seed oil and rice bran oil and animal oil such as butter, lard, mutton fat and fish oil (all claimed).    ADVANTAGE - The activity stability of the catalyst can be ensured. The stable and long period hydrogenation operation can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process of producing low freezing point motor fuel from biological oil. (Drawing includes non-English language text)
NOVELTY - The device has a machine frame whose top is provided with storage tank (7). The storage tank is provided with a spray head. The spray head is provided above the feed hopper (16). The pipe of the nozzle (15) is provided with a switch. The feed hopper is provided at the bottom of magnetic separation disc. The vibration separation sieve (24) is provided with recycle plastic outlet (22). The recycle plastic outlet is connected with fertilizer outlet (26).    USE - Device for producing fertilizer by utilizing household garbage.    ADVANTAGE - The device is provided with the magnetic separation disc, so that steel, iron and other metals can be separated from the household garbage. The separation sieve is arranged, so that paper and recycled plastic in the household garbage can be separated from organic substances serving as organic fertilizers. The device can automatically spray biological strains to the household garbage, so that the organic substances can be fermented to form the organic fertilizers. The device is simple in structure. The manufacturing cost of the device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing fertilizer by utilizing household garbage.    Storage tank (7)    Nozzle (15)    Feed hopper (16)    Recycle plastic outlet (22)    Vibration separation sieve (24)    Fertilizer outlet (26)
NOVELTY - Rubber accelerator (N-(oxidiethylene)-2-benzothiazoyl sulfenamide) is prepared by dissolving M(2-mercaptobenzothiazole):morphine with weight ratio of 1:9, heating solution to 50-60 degrees C, adding hydrogen peroxide while maintaining reaction temperature, evaporating excess liquid under vacuum pressure, crystallizing, filtering to obtain solid material, washing with water, and drying.    USE - Preparation of rubber accelerator (N-(oxidiethylene)-2-benzothiazoyl sulfenamide) (claimed).    ADVANTAGE - Preparation of rubber accelerator recycles used water and does not emit wastewater or waste gas which makes it environment-friendly.
NOVELTY - A carbon-based solid acid contains fresh fruit shell as raw material in which solid acid is prepared by injection molding and has specific surface area of 1000 m2/g and acid value of greater than or equal to 2.5 mmol/L.    USE - A carbon-based solid acid (claimed).    ADVANTAGE - Preparation cost is reduced, utilization rate of fruit shell is improved, reaction condition is safe, product has good color, and carbon-based solid acid has large specific surface area with good catalytic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of carbon-based solid acid which involves drying fruit shell, washing with water repeatedly until there is no impurity, placing cleaned fruit shell into oven to dry, crushing to 10-50 meshes, activating fruit shell according to ratio material:liquid of 1:2-20 g/ml in 20-50 wt.% activator solution for 2-12 hours, adding soaked fruit shell in drying box to remove residual water, heating under protective atmosphere to 400-600 degrees C for 2-15 hours, grinding activated carbon into powder, boiling in acid solution, filtering, rinsing with distilled water, drying to obtain activated carbon material, sulfonating activated carbon material at 80-200 degrees C using sulfonating agent solution for 6-15 hours in which ratio activated carbon material:sulfonating agent solution is 1:5-20 g/ml, slowly pouring mixed solution of sulfonated material into cold water and continuously stirring, filtering, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the preparation of carbon-based solid acid from fresh fruit. (Drawing includes non-English language text).
NOVELTY - This utility model claims a kind of vehicle-mounted fuel microwave plasma system for decomposing ammonia to prepare hydrogen on line. The magnetron comprises a pipe part, the microwave part and a control part, the microwave by the magnetron base a circulator connected to the magnetron power supply control device used for adjusting the magnetron power supply voltage so as to make the magnetron output power continuously adjustable, comprising ignition chamber and the reaction chamber, an ignition chamber and the reaction chamber, and are respectively connected with the two output end of the circulator, the circulator 2 a bent waveguide is respectively connected with the ignition chamber and the reaction chamber is connected with a tuning reflector on the bend waveguide circulator and ignition chamber, wherein the control part is mainly composed of industrial, temperature and pressure sensor and a flow meter, the collected by a signal collecting point information and analysis, control the whole system to work in a process. This utility model solves the problem that the small volume, light weight, intelligent control, microwave output power continuously adjustable, low temperature, low pressure environment operation and so on.
NOVELTY - This utility model claims a kind of fast high-acidity grease deacidification device, comprising a condensing pipe, esterification reactor, molecular sieve packed column and so on, the top part of the column at the bottom of the condensing pipe is connected with molecular sieve to fill, and it is connected to the bottom of the esterification reactor through pipeline, the water generated by esterification reaction with methanol steam as gas in the form of belt, and is condensed into liquid water, the water is absorbed by the molecular sieve packed column, the irreversible reaction to generate ester to a direction to reach the high-acidity grease fast reducing acid of liquid methanol in the esterification reactor to take part in the reaction, realizes the recycling of methanol recycling, high-acidity grease for the cup biodiesel by acid as raw material. Is provided with a simple structure and high efficiency, low energy consumption and so on.
NOVELTY - This utility model claims a kind of solid acid catalytic acid grease device for continuously preparing biodiesel, comprising a raw material mixer, a metering pump, a heater, a ester exchange reaction tower and distillation tower, this utility model make the material after stirring continuously to react in the reaction device layer, the product is easy to separate and reduce the production cost of the energy at the same time, the production method is greatly simplified, there is no pollution and the economic benefit is improved.
NOVELTY - Household garbage is carbonized by performing compression molding on organic fines crushed and selected from household garbage, putting organic fines subjected to compression molding into carbonizing furnace for carbonization in which green bricks of organic fines subjected to compression molding are put into set of iron cages and fed in to carbonizing furnace, igniting carbonizing furnace from bottom at 270 degrees C to ensure that organic fines combust automatically to generate anaerobic carbonization as micro air inlet is formed in bottom of carbonizing furnace, and controlling temperature.    USE - Carbonization of household garbage (claimed).    ADVANTAGE - Carbonization process is simple, convenient, effective, environment-friendly, non-toxic, and has high carbon rate.    DETAILED DESCRIPTION - Household garbage is carbonized by performing compression molding on organic fines crushed and selected from household garbage, putting organic fines subjected to compression molding into carbonizing furnace for carbonization in which green bricks of organic fines subjected to compression molding are put into set of iron cages and fed in to carbonizing furnace, igniting carbonizing furnace from bottom at 270 degrees C to ensure that organic fines combust automatically to generate anaerobic carbonization as micro air inlet is formed in bottom of carbonizing furnace, controlling temperature of furnace to 270-380 degrees C through air inlet at bottom for 3-10 hours, closing air inlet, extinguishing fire, and controlling temperature to less than or equal to 80 degrees C.
NOVELTY - The system (20) has a cathode line (c) and an anode line (a) for supplying air and hydrogen to a fuel cell stack (1). A hydrogen supply system (15) and a solenoid valve (12) are connected to the anode line. A fan (13) sends air, and is provided in the cathode line. An anode bypass-line (a') is provided side by side on the anode line. An on-off valve (22) is provided in middle of the anode bypass-line. The fuel cell stack produces electric power by hydrogen, which flows through the anode bypass-line when the on-off valve is opened in a valve closing state of the solenoid valve.    USE - Fuel cell system.    ADVANTAGE - The system is started and can supply electric power to a load even if the system is in a state for which power capacity of a secondary battery is insufficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system. '(Drawing includes non-English language text)'    Anode line (a)    Anode bypass-line (a')    Cathode line (c)    Fuel cell stack (1)    Solenoid valve (12)    Fan (13)    Hydrogen supply system (15)    Fuel cell system (20)    On-off valve (22)
NOVELTY - A source gas as raw material contains natural gas, coal and biomass containing carbon monoxide and hydrogen obtained by thermochemical gasification reaction, is used. The source gas and co-catalyst is reacted, synthesized to obtain ethanol. The obtained ethanol is converted to 1-butanol in presence of catalyst containing calcium, strontium and phosphorus or magnesium oxide, titanium, molybdenum and/or lithium. The co-catalyst is zinc or copper, and catalyst is rhodium, manganese, zirconium, scandium, lanthanum, cerium, vanadium, iron, lithium and/or iridium.    USE - Manufacture of 1-butanol used for biofuel as gasoline in gasoline engine.    ADVANTAGE - The method enables efficient manufacture of 1-butanol having low affinity to water, with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of 1-butanol.    Biomass insertion opening (1)    Heating water vapor insertion opening (2)    Biomass gasifier (3)    Recycle and source gas booster (5)    Membrane separation device (8)
NOVELTY - This utility model claims continuous production equipment is a kind of biological diesel oil, the metering pump comprises a reaction device, a connecting pipeline and a pipeline, a conveying pump and a flow meter, wherein a biological reaction device comprising a mixer (2), a heater I (3), a pipeline reactor I (4), the esterification reaction tower (5), a catalyst separator (10), a methanol storage tank (9), alkali liquid tank (12), a pipeline reactor II (24), a flash evaporation tower (15), separator (16), a distillation tower (17) and a storage tank (19). This utility model device is suitable for the raw material oil quality range, low energy consumption, the conversion rate is high, more environment-friendly, it can effectively improve the product quality and the yield of the bio-diesel.
NOVELTY - This utility model claims a continuous preparation of biodiesel reinforced mixing reaction device, comprising a reactor and pre-mixer, wherein a guide cylinder is a tubular reactor inlet end. This utility model has advantages of a suitable size guiding the guide cylinder, the ordered circulation of the material to make the material generate back mixing, supercritical methanol phase and at a reactor inlet end of solubility increase beneficial effects of a back mixing and the adverse effect brought by, a ratio is reduced, the reaction time is shortened. Reducing the reaction time to alcohol ratio is shortened to avoid coking of biological diesel oil at high temperature, so the energy consumption is reduced, and the yield is improved. Provided with a guide cylinder enhances the reaction process, increasing the production efficiency of the reactor, so as to realize the continuous biodiesel production, low energy consumption and high yield.
NOVELTY - This utility model claims a kind of for biological diesel production device for separating and draining solid liquid continuously, comprising a tank body (1), the tank body (1) is provided with a filler (3) and the heavy phase deposition part (7), a tank body (1) is provided with a light phase outlet (4), a tank body (1) is provided with a heavy phase outlet (6), a heavy-phase deposition part (7) is provided with a feeding port (2), wherein the filler part (3) is provided with hydrophilic filler. This utility model has good separation effect and high separation efficiency, low energy consumption and environmental protection and so on.
NOVELTY - The sewage and sludge regenerated biomass combustion gas absorbs organic substance in the high temperature thermal decomposition. The organic matter gasification evaporation process is performed in the inorganic substance to separate lime-sand and decomposition product from the inorganic substance. The generated gas and biological natural gas are provided to a dust removing device for performing temperature methanation reaction at high temperature for avoiding catalytic thermal cracking.    USE - Combustion biomass gas production line, used in sludge treatment and sewage treatment.    ADVANTAGE - The efficiency of the biomass fuel gas production process can be improved effectively. The water content of the sludge can be reduced reliably. The catalytic thermal cracking can be prevented reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage and sludge regenerated biomass combustion gas production line. (Drawing includes non-English language text)    Quality device (1)    Drying device (2)    Blower (4)    Thermal decomposition reaction device (5)    Exhaust fan (6)
NOVELTY - Slag contained in drainage oil is cleaned, and solid waste such as solid grease and hair are separated. The waste oil is primary filtered and separated. The filtered waste oil is heated and further filtered, oil concentrate is separated, and liquid is obtained. Additive is added to liquid, esterified into glycerol, and distilled or converted into biodiesel product. The solid waste is further separated into inorganic substance and organic substance, and used as fertilizer. The separated waste oil is recycled. Residual wastewater is cleaned, separated, and recycled.    USE - Treatment of drainage oil (claimed).    ADVANTAGE - The drainage oil treatment is easily and economically enabled at high decomposition rate.    DETAILED DESCRIPTION - Slag contained in drainage oil is cleaned, and solid waste such as solid grease and hair are separated from oil using a screening device. The resulting waste oil is primary filtered in a 20-mesh filter bag and separated. The filtered waste oil is heated at 50 degrees C and further filtered with a filter membrane, oil concentrate is separated, and liquid is obtained. Additive is added to the obtained liquid in a stirrer, esterified into glycerol, and distilled or converted into biodiesel product in a distillation column. The solid waste is further separated into inorganic substance and organic substance in a distillation tower, and used as fertilizer. The separated waste oil is recycled. Residual wastewater is cleaned by nano-filtration module, clear water and waste liquid are separated, clean water is recycled, slag oil is cleaned, further filtered and separated.
NOVELTY - Biogas strawberry soilless culture in greenhouses application method involves strawberry soilless culture in greenhouses, construction of biogas digesters, biogas combustion heat release, improve the greenhouse temperature, increasing light, Adding carbon dioxide, Meanwhile, biogas can foliar application, foliar spraying, biogas residue as soilless media materials, to improve physical and chemical properties matrix, and promote the growth of strawberry plants.    USE - As biogas strawberry soilless culture in greenhouses application method (claimed).    ADVANTAGE - The method improves the physical and chemical properties of the substrate, promotes growth of plant of strawberry to realize strawberry soilless facility planting high yield, high quality and high efficiency.
NOVELTY - Refined waste cooking oil and methanol are catalytically reacted at 60-80 degrees C for 5-10 hours in the presence of solid base catalyst, and the solid base catalyst is removed after reaction is finished. The obtained filtrate is distilled in a pressure-reducing state for 2-4 hours under vacuum degree of 0.08-0.11 MPa at 95-110 degrees C, decompressed, distilled, and the obtained supernatant liquid is sequentially decolored and filtered to obtain biodiesel oil. The mass ratio of oil and methanol is 100:16-20. The amount of catalyst with respect to total amount of oil and methanol is 0.1-2.5 %mass.    USE - Manufacture of biodiesel oil (claimed).    ADVANTAGE - Clear and transparent biodiesel oil is economically and easily manufactured with favorable cold filter plugging point, closed-cup flash point, room-temperature kinematic viscosity and acid value.
NOVELTY - Fuel-formation method of combustible waste liquid involves mixing wood-type biomass, and performing combustible waste liquid having a consolidation set as solid fuel absorbed and supported by wood-type biomass.    USE - Fuel-formation method of combustible waste liquid used for forming solid fuel for manufacturing cement.    ADVANTAGE - The method easily and cheaply forms combustible waste liquid with high fuel value and emitted-heat amount, and favorable safety and handleability.
NOVELTY - An animal waste treatment system has mixing system (A) which mixes and supplies manure and fine wooden molder powder, drying system (B) which dries the mixed raw material to obtain composite biomass fuel where self-sustained combustion heating is possible, system (C) which measures moisture content and stores composite biomass fuel, and boiler system (D) having boiler that uses composite biomass fuel as fuel source to generate heat for drying process.    USE - An animal waste treatment system.    ADVANTAGE - Livestock excrement waste is reduced, and quality of biomass fuel is improved and stabilized.    DETAILED DESCRIPTION - An animal waste treatment system has mixing system (A) which mixes and supplies manure and fine wooden molder powder, drying system (B) which dries the mixed raw material to obtain composite biomass fuel where self-sustained combustion heating is possible, system (C) which measures moisture content and stores composite biomass fuel, and boiler system (D) having boiler that uses composite biomass fuel as fuel source to generate heat for drying process. The process involves mixing defiberized fine wooden molder powder with manure which contains livestock excrement, drying to obtain composite biomass fuel where self-sustained combustion heating is possible, and using obtained composite biomass fuel as heat source for drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the animal waste treatment system. (Drawing includes non-English language text).    Mixing system (A)    Drying system (B)    System (C)    Boiler system (D)
NOVELTY - A fuel reformer for reforming low quality fuel oil and non-chlorine-type lubricous waste oil comprises superheated steam generator which uses composite material of ceramic and metal, saturated steam generator, and thermal decomposition unit which uses composite material of ceramic and metal.    USE - A fuel reformer for reforming low quality fuel oil and non-chlorine-type lubricous waste oil and processing radioactive liquid waste, polymeric liquefaction waste material, and small amount of residues (all claimed).    ADVANTAGE - Product oil of grade A heavy oil can be obtained from low quality fuel or waste oil, and environmental load is reduced.
NOVELTY - A Trichoderma microbe having antagonistic property with respect to white root rot disease microbe of Hevea brasiliensis, is new.    USE - The Trichoderma microbe is useful as biological pesticide for controlling white root rot disease microbe, preferably Rigidoporus microporus, and in plant-pathogen protectant and soil conditioner. The Trichoderma microbe is T.spirale or T.erinaceum (all claimed).    ADVANTAGE - The Trichoderma microbe microbe is reliable to use, and causes less toxicity as the microbe is biological pesticide.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) Plant-pathogen protectant comprising cultured microbe, wet biomass or dry biomass of Trichoderma microbe; (2) method for controlling plant pathogens, involves processing soil using the above-mentioned plant-pathogen protectant; (3) soil conditioner comprising cultured microbe, wet biomass or dry biomass of Trichoderma microbe; and (4) method for improving soil, involves processing soil with the soil conditioner.
NOVELTY - The water electrolysis apparatus (1) has a water electrolysis stack (4) that is provided with water electrolysis cell. The oxygen gas-liquid separation unit (2) and pump (5) supply water to anode of water electrolysis cell, and hydrogen gas-liquid separation unit (3) and pump (6) supply water to cathode of water electrolysis cell, and electric power supply unit (7) applies a stop voltage lower than electrolysis generated voltage to water electrolysis cell, when the water electrolysis stack stops the water electrolysis reaction.    USE - Water electrolysis apparatus.    ADVANTAGE - Since the oxygen gas-liquid separation unit and pump supply water to anode of water electrolysis cell, and hydrogen gas-liquid separation unit and pump supply water to cathode of water electrolysis cell, and electric power supply unit applies stop voltage lower than electrolysis generated voltage to water electrolysis cell, when the water electrolysis stack stops the water electrolysis reaction, the deterioration of the electrolytic membrane can be effectively suppressed, and the migration of the impurity ion in the reverse direction accompanying fuel cell reaction can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating water electrolysis apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the water electrolysis apparatus. (Drawing includes non-English language text)    Water electrolysis apparatus (1)    Oxygen gas-liquid separation unit (2)    Hydrogen gas-liquid separation unit (3)    Water electrolysis stack (4)    Pumps (5,6)    Electric power supply unit (7)
NOVELTY - Activation process of hydrogen storage alloy (8) involves evacuating container (3) filled with hydrogen storage alloy at 40-300 degrees C, passing hydrogen gas to container, and cooling container at less than 40 degrees C.    USE - Activation process of hydrogen storage alloy used in fields using hydrogen fuel battery and hydrogen, e.g. heat pump, actuator, and hydrogen purification.    ADVANTAGE - The activation process of hydrogen storage alloy can be efficiently carried out with the container filled with large quantity or small sized hydrogen storage alloy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (1) for activation process of hydrogen storage alloy.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus for activation process of hydrogen storage alloy.    Apparatus for activation process of hydrogen storage alloy (1)    Container (2)    Warming-cooling-medium circulation path (3)    Hydrogen storage alloy (8)    Gas exhaustion pipe (9)
NOVELTY - The system has a measuring section (301) for measuring values of electric signals output from a heating element that is exposed to mixed gas flowing in a pipe (101). An equation creating section (302) creates calorific value equation with independent variables. Dependent variable is created based on known calorific values of the mixed gas and measured values of the signals output from the heating element at heating temperature, where the independent variables are the signals output from the heating element at the temperature and the dependent variable is the calorific values.    USE - System for creating calorific-value-equation to calculate a calorific value of mixed gas i.e. natural gas.    ADVANTAGE - The calorific values of gas are measured in an easy manner. The calorific values of mixed gas such as natural gas, are obtained to appropriately set volume of air necessary to combust the mixed gas, thus reducing an amount of unnecessary carbon dioxide emissions in an easy and accurate manner. The heating element heats atmosphere gas whose temperature fluctuation is reduced, thus calculating heat-radiation coefficient in an accurate manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a calorific value measuring system    (2) a calorific value measuring method    (3) a calorific value equation creating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a calorific value measuring system.    Calorific value measuring system (20)    Pipe (101)    Measuring section (301)    Equation creating section (302)    Electric signal storage device (401)    Equation storage device (402)
NOVELTY - A modification catalyst contains inorganic complex oxide support containing alumina, rare-earth metal oxide and alkaline-earth metal oxide, and cobalt and rhodium are supported on the support.    USE - Modification catalyst is used in hydrogen production apparatus for fuel cell system for producing hydrogen (all claimed) using hydrocarbon as raw material.    ADVANTAGE - The modification catalyst has excellent catalytic activity and durability, and efficiently and economically produces hydrogen by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of modification catalyst, which involves impregnating a solution in which cobalt compound and rhodium compound are contained in inorganic complex oxide support or its precursor;    (2) production method of hydrogen, which involves modifying hydrogen raw material containing hydrocarbon compound by modification catalyst; and    (3) hydrogen production apparatus, which has a supply unit which supplies gas containing oxygen and/or steam, and modification unit having modification catalyst and hydrogen raw material in which hydrocarbon compound is contained. The product containing hydrogen is obtained from hydrogen raw material by partial oxidation reaction, self-thermal reforming reaction and/or steam reforming reaction.
NOVELTY - A modifier (1) comprises catalyst unit (20) which has modification catalyst (2) which modifies hydrogen fuel and generates hydrogen and oxidation catalyst (3) which oxidizes in oxidizing atmosphere and electric heater (10) having electroconductive part. Catalyst unit has carrier which supports catalyst particle of modification catalyst and oxidation catalyst and base material which supports carrier and has electroconductive material. Electric heater is positioned adjacent to catalyst unit or in upstream of catalyst unit.    USE - A modifier for modifying hydrogen fuel (claimed).    ADVANTAGE - Modification time is short, structure of modifier is compact, and pressure loss is low.    DETAILED DESCRIPTION - A modifier (1) comprises catalyst unit (20) which has modification catalyst (2) which modifies hydrogen fuel and generates hydrogen and oxidation catalyst (3) which oxidizes in oxidizing atmosphere and electric heater (10) having electroconductive part. Catalyst unit has carrier which supports catalyst particle of modification catalyst and oxidation catalyst and base material which supports carrier and has electroconductive material. Electric heater is positioned adjacent to catalyst unit or in upstream of catalyst unit. Modifier makes catalyst unit induce electric current by electromagnetic induction brought about by electricity supply of alternating current to electroconductive part and heats catalyst unit by supply of alternating current with electricity to electroconductive part of electric heater.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the modifier.    Modifier (1)    Modification catalyst (2)    Oxidation catalyst (3)    Electric heater (10)    Catalyst unit (20)
NOVELTY - A fuel formation apparatus (1) of municipal solid waste processed material comprises classifying apparatus (11) which classifies municipal solid waste processed material (T) to coarse grain (C) and microparticle (F). Municipal solid waste processed material is obtained by fermenting municipal solid waste (W).    USE - A fuel formation apparatus of municipal solid waste processed material used in cement firing.    ADVANTAGE - Heat arising from combustion of municipal solid waste processed material can be effectively used, therefore suppressing generation of persistent organic pollutants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel formation method of municipal solid waste processed material which involves classifying municipal solid waste processed material to coarse grain and microparticle and separately utilizing coarse grain and microparticle as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel formation apparatus of municipal solid waste processed material.    Fuel formation apparatus (1)    Classifying apparatus (11)    Coarse grain (C)    Microparticle (F)    Municipal solid waste processed material (T)    Municipal solid waste (W)
NOVELTY - This utility model claims a combustion energy-saving furnace with biomass straw as a filtering device, comprising at least more than one air outlet orderly connected with filtering device, the filtering device comprises a leading-in air pipe, a filter tank and the air pipe, an air inlet opening of the air leading-in pipe is provided with the bottom of the filter tank, a gas outlet opening of the gas leading-out pipe is set on the top of the filter box, the filter box is provided with at least more than one air outlet nozzle, the one used for combustion energy-saving furnace with biomass straw as a filtering device, the harmful gas is water-soluble, it can effectively remove harmful gas and low cost through a multi-stage water filter. At the same time the transmission process of the straw burning gas mixture, the air leading-in pipe and tightness of the gas leading-out pipe so as to avoid gas leakage caused by waste or other security to the out of the air pipe and the air pipe are covered with sealing caused by the leading-in air pipe and the air pipe for sealing, ensures the smooth production and improve the safety of the production.
NOVELTY - Producing biogas involves utilization of residual wastes of Pleurotus eryngii bran and mushroom head, as fermentation substrate. The method involves crushing Pleurotus eryngii bran and mushroom head into loose powder state or extruding into slurry, and then mixing uniformly. The fermentation process involves addition of nitrogen fertilizer; and is carried out by wet or dry fermentation. The wet fermentation provides final fermentation product 40-80% of the total volume of biogas.    USE - For producing biogas (claimed).    ADVANTAGE - The method by using bi-component (i.e. Pleurotus eryngii bacteria bran and mushroom head) achieves 20-30% higher production rate than the original single fermentation, which greatly improves the resource utilization rate of the waste. The fermentation period is a day yield that is lower than half of average daily gas production rate of fermentation.    DETAILED DESCRIPTION - Producing biogas involves utilization of residual wastes of Pleurotus eryngii bran and mushroom head, as fermentation substrate. The method involves crushing Pleurotus eryngii bran and mushroom head into loose powder state or extruding into slurry, and then mixing uniformly. The fermentation process involves addition of nitrogen fertilizer; and is carried out by wet or dry fermentation. The wet fermentation provides final fermentation product 40-80% of the total volume of biogas. The step of inoculating involves inoculating 30-50% normal fermentation gas by dry fermentation to obtain biogas residue. The method involves adjusting the final fermentation product dry matter concentration of the wet fermentation upto 3-15% to obtain 15-25% dry yeast. The fermentation temperature is 30-45 degrees C, or 50-60 degrees C.
NOVELTY - Producing fuel butanol involves using adding 1.5% maize straw hydrolysis solution in fermentation culture medium followed by fermenting using Clostridium acetobutylicum. The method involves adding 2% dilute sulfuric acid into the straw hydrolysis liquid, where ratio of acid to liquid is 1:5, at 121 degrees C and performing hydrolysis for 2 hours, followed by neutralizing using Ca(OH)2 to pH value of 4.5, where initial pH is 6.0, and filtering.    USE - For producing fuel butanol (claimed).    ADVANTAGE - The present method is cost-effective, and produces butanol in high yield.
NOVELTY - Constructing bacteria fermentation system for forming ethanol straw rod involves: preparing straw fermentation culture medium; using Trichoderma viride and Trichoderma reesei ferment straw, secretion lignocellulose degrading enzyme, lignin peroxidase, laccase and cellulose; accomplishing in situ enzymatic saccharification of straw rod; and re-using sodium alginate-polyvinyl alcohol-silicon dioxide immobilized Saccharomyces cerevisiae and Candida tropicalis for co-immobilized yeast granule to multi-batch fermentation of straw saccharified liquid.    USE - For constructing a bacteria fermentation system for producing ethanol straw rod (claimed).    ADVANTAGE - The method produces ethanol micro-environment; improves the efficiency of producing ethanol; has low energy consumption, no pollution, short production period; and recycles the yeast.    DETAILED DESCRIPTION - Constructing a bacteria fermentation system for producing ethanol straw rod, involves: (1) preparing straw fermentation culture medium; (2) using Trichoderma viride and Trichoderma reesei ferment straw, a secretion lignocellulose degrading enzyme, a lignin peroxidase, laccase and cellulose; (3) accomplishing an in situ enzymatic saccharification of straw rod through a process, to prepare the straw saccharification liquid; and (4) re-using sodium alginate (SA)-polyvinyl alcohol (PVA)-silicon dioxide (SiO2) immobilized Saccharomyces cerevisiae and the Candida tropicalis for co-immobilized, which is a co-immobilized yeast granule to multi-batch fermentation of straw saccharified liquid.
NOVELTY - A kind of marsh gas pool cleaning device, belonging to the technical field of marsh gas, comprising a base, the base is provided with a vacuum pump, a liquid storage tank, a liquid storage tank is connected with one end of the feeding pipe, the feeding pipe is connected with a spherical slag filter, filter is connected with a soft pipe, the top part of the liquid storage tank liquid storage tank at the bottom of one end of the valve is provided with a discharging pipe connected with the vacuum pump by an air pipe. Using pressure difference principle, reducing the pressure in the liquid storage tank, the liquid in the marsh gas tank is pumped to the liquid storage tank to replace the original manual cleaning, the operation is very convenient and safe, and has simple structure, low manufacturing cost, it is suitable for the user to use.
NOVELTY - The cell (100) has photo-electric layer structure (1) and electrochemical-layer structure (2) for receiving the electrolyte (10) are provided at front and back surface of layered structure (40) respectively. A conductive coupling and corrosion-inhibiting layer (13), photo-electric layer structure and electrochemical-layer structure are electrically contacted with the layered structure. An ion exchange film (61) is arranged between front and back electrodes (21,22) of the electrochemical-layer structure, and is provided to contact with the electrolyte and front and back electrodes.    USE - Photo-electrochemical cell of photo-electrochemical cell system, for light-driven production of hydrogen and oxygen in water or electrolyte based acidic or alkaline aqueous solution e.g. sulfuric acid (all claimed).    ADVANTAGE - The stability and efficiency of the photo-electrochemical cell can be improved. The structure of the photo-electrochemical cell is simplified. The harmful impacts of electrolytes to the photo-electrochemical cell are reduced. The resistance of the cell is reduced. The charger transfer between light absorber and redox system is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of hydrogen and oxygen in water or electrolyte aqueous solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the photo-electrochemical cell.    Photo-electric layer structure (1)    Electrochemical-layer structure (2)    Electrolyte (10)    Conductive coupling and corrosion-inhibiting layer (13)    Front electrode (21)    Back electrodes (22)    Layered structure (40)    Ion exchange film (61)    Photo-electrochemical cell (100)
NOVELTY - Method for producing methane, involves co-cultivating purple non-sulfur bacteria and hydrogen utilization methane producing bacteria in a culture medium in the presence of carbon dioxide, where the culture medium does not contain ammonium salt but contain L-cysteine hydrochloride as a reducing agent.    USE - The method is useful for producing methane (claimed) which is used as energy source.    ADVANTAGE - The method simple and cost-effective, and causes no environmental pollution.
NOVELTY - A biological oil preparing method involves putting mixed liquefier and liquefying catalyst in a container, heating at 120-180 degrees C, adding biomass or biomass waste, liquefying for 30-120 minutes, cooling to room temperature, dissolving the liquefied mixture in a solvent till the liquid product is sufficiently dissolved, carrying out vacuum filtration to implement solid-liquid separation, carrying out rotary evaporation, and concentrating the liquid product to obtain finished product.    USE - Method for preparing biological oil.    ADVANTAGE - The method enables preparing biological oil in a simple and inexpensive manner with high thermal efficiency, yield and liquid rate.
NOVELTY - Matrix is prepared by collecting waste rods after producing edible fungus, crushing and fermenting at 60 degrees C or less, mixing the fermented waste, furnace ash and dry chicken manure in ratio of 6:3:1, in a plastic greenhouse, where the ash has pH value of 7 after half month, laying a layer of brick at the peripheral region of vegetable planting, laying a plastic film, then laying two layers of bricks on the first layer of the brick, and then laying a nutrition bed of the vegetables.    USE - As matrix for soilless culture of vegetable.
NOVELTY - This utility model claims a coke-oven gas LURGI furnace or /BGL furnace coal gasification co-production technique of alcohol-ammonia device, comprising: a first heat exchanger, a second heat exchanger, a third heat exchanger and a nitrogen washing tower, wherein it further comprises a methane rectifying tower, methane rectifying tower top condenser, methane rectifying tower bottom reboiler and the raw material gas flash tank, C0 liquid tank, liquid methane pump, and they are connected by pipeline. This utility model through increasing the methane rectifying tower in the conventional liquid nitrogen washing device, a liquid methane pump and through the reasonable circuit design, the methane-rich fraction can be reheated as city gas. methane-rich fraction is also capable of producing LNG product by Claude cycle. SNG at the same time and the LNG product can be adjusted according to different load.
NOVELTY - Method for producing bio-oil using nanoclay, involves (a) taking five days culture medium comprising oil-producing microorganism, (b) adding nanoclay to the culture comprising oil, (c) performing nanoclay flocculation by separating microorganism from the culture medium, (d) separating oil from the culture medium and crushing the microorganism, and (e) discharging the oil separated from the microorganism debris.    USE - The method is useful for producing bio-oil which is useful for preparing biofuel (all claimed).    ADVANTAGE - The method cost-effectively prepares environmentally-friendly biofuel, and provides high yield of biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biofuel, which involves performing the above-mentioned step (a)-(e), and (f) reacting the oil with acid or base catalyst and alcohol.
NOVELTY - Preparing an amorphous tolvaptan comprises: either (a) dissolving tolvaptan in an organic solvent, (b) removing the solvent, and (c) isolating pure amorphous tolvaptan; or (a1) the steps (a) and (b) as above per se, (b1) adding a second solvent, (c1) optionally drying the wet mass, and (d1) isolating amorphous tolvaptan.    USE - The method is useful for preparing an amorphous tolvaptan (claimed), which is useful for treating hyponatremia associated with congestive heart failure, cirrhosis and a syndrome of inappropriate antidiuretic hormone. No biological data given.    ADVANTAGE - The method provides the amorphous tolvaptan with high purity in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for packing the amorphous tolvaptan comprising (1) placing amorphous tolvaptan in high molecular weight low-density polyethylene (HMLDPE) bag under inert atmosphere at 55 plus minus 5% relative humidity, (2) placing HMLDPE bag in a triple laminated aluminum bag under inert atmosphere with two silica gel sachets and one molecular sieve sachet, (3) placing the contents of step (2) in the triple laminated aluminum bag under inert atmosphere with two silica gel sachets and one molecular sieve sachet, and (4) packing the contents of step (3) in a closed high density polyethylene container.
NOVELTY - The invention relates to a process for preparing a Diesel bio-fuel. According to the invention, the process consists in extracting oil with hexane from algae as powder, at a temperature of 70...75 degrees C, for 6...8 h, after which methanol containing 5...10% sulphuric acid is admixed to the algae oil dissolved in hexane and the resulting mixture is thermostated at 50...55 degrees C for 1...2 h and further treated with a solution of sodium methoxide in methanol, in a concentration of 20...25%, at a pH value of 10...13, then it is thermostated at 50...55 degrees C for 1...2 h, the phases are separated and the upper layer containing the methyl esters of fatty acids of algae is purified by distillation-washing-drying to result in a fuel having a minimal methyl ester content of 97%.
NOVELTY - Chlamydomonas moewusii KNUA013 strain having a preservation number of KCTC12065BP, is new.    USE - The Chlamydomonas moewusii KNUA013 strain is useful for producing heptadecane, hexadecenol and 16-18C fatty acid such as 0-16C palmitic acid, 16-4C hexamethylene deca tetracarboxylic acid and 18-1C oleic acid and in the production of biodiesel (all claimed).    ADVANTAGE - The Chlamydomonas moewusii KNUA013 strain can directly produce biodiesel without the process of conversion of liquid hydrocarbon.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) producing heptadecane, hexadecenol and 16-18C fatty acid comprising cultivating the Chlamydomonas moewusii KNUA013 strain and extracting heptadecane, hexadecenol and 16-18C fatty acid from the culture medium; and (2) producing biodiesel comprising performing transesterification of 16-18C fatty acid produced by the strain to obtain fatty acid ester.
NOVELTY - The controlled inner combustion cylinder is integrated in different technological development levels by diverse devices, and has a cylinder and five components.    USE - Controlled inner combustion cylinder for the gasification and generation of hydrogen.    ADVANTAGE - The controlled inner combustion cylinder is integrated in different technological development levels by diverse devices, and has a cylinder and five components, and hence ensures ecological and economical combustion cylinder.
NOVELTY - The lignocellulosic materials delignification involves separating major components of lignocellulosic materials, cellulose, lignin and hemicelluloses at atmospheric pressure and low temperatures.    USE - Method for delignification of lignocellulosic materials for use as fertilizer.    ADVANTAGE - The method increases performance, and allow more economical equipment in an environmentally friendly manner.
NOVELTY - An alkali metal additive composition comprises feed stock obtained by mixing alkali metal compound with water.    USE - Alkali metal additive composition is used for liquefaction and gasification of solid material (claimed) e.g. biomass and coal.    ADVANTAGE - The alkali metal additive composition optimizes efficiency of gasifier and liquefier, and prevents corrosion of instrument for fuel recycling. The liquefaction and gasification of solid material is efficiently carried out using the alkali metal additive composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for usage of alkali metal additive composition for liquefaction and gasification of solid material.
NOVELTY - This utility model claims a biomass fuel gas purifying absorption tower, the bottom of the tower body is liquid collecting tank, liquid collecting groove above the tower body along the radial direction is provided with a filling layer, the filling layer is set above the liquid, the upper part of the tower body above the liquid is provided with a liquid inlet, the liquid inlet is equipped with liquid distributing tube, a liquid distribution pipe is equipped with liquid distributor, a tower body of the liquid inlet above the foam destroyer, the top end of the tower body is provided with a gas outlet, the bottom of the collecting tank is provided with a liquid outlet, the liquid outlet of the liquid distribution pipe through pipeline, the bottom of the tank is provided with a gas inlet, a liquid collecting groove is equipped with a spiral gas pipe, the spiral air tube is distributed with a gas distributor with gas inlet of the spiral air pipe. This utility model can effectively adjust the air flow distribution, extend through time, reduces air flow resistance to air flow orderly stable flow, increasing gas-liquid contact mass transfer and eliminate air bunch phenomenon and improves the absorption efficiency.
NOVELTY - The apparatus (100) has an auto thermal reforming reactor (10) to which the reactant is supplied through a reactant supply path within an internal heat exchanger (20). The reactant after supplying to the auto thermal reforming reactor is supplied to an aqueous reactor (30) in which aqueous reaction is occurred. The auto thermal reforming reactor and the aqueous reactor are arranged by facing each other. The internal heat exchanger is positioned between the auto thermal reforming reactor in which the autothermal reforming reaction is occurred, and the aqueous reactor.    USE - Fuel processing apparatus of fuel processing system, for processing fuel such as liquid fuel, petrol and hydrocarbon fuel used for fuel cell.    ADVANTAGE - The high hydrogen yield and the low carbon monoxide yield can be maintained at sufficient temperature. The weight reduction of the apparatus can be reduced. The product passing through the aqueous reactor can be ejected reliably through the vent. The high fuel energy storage density can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for processing fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for processing fuel. (Drawing includes non-English language text)    Auto thermal reforming reactor (10)    Auxiliary heating device (15)    Internal heat exchanger (20)    Aqueous reactor (30)    Apparatus for processing fuel (100)
NOVELTY - Pharmaceutical preparation, comprises washing radix sophorae tonkinensis, slicing the washed sophorae tonkinensis using slicing machine, extracting sliced material with matrine, matrine oxide and organic acid, concentrating, purifying and drying the material, and pelleting the dried material with auxiliary material.    USE - The pharmaceutical preparation is useful for treating acute and chronic hepatitis.    ADVANTAGE - The method provides tablet in a simple, cost-effective and an environment-friendly manner.
NOVELTY - Dimethylsulfate and dimethylsulfide are added to acetone in the mol ratio of 1:1-3, and heat-stirred, to obtain onium salt. 1-Phenethyl-4-piperidine ketone is cyclized to obtain 1-phenethyl-4-piperidine oxirane. The oxirane is reacted with the onium salt in the presence of non-polar solvent, carbamate and a base to obtain fenspiride.    USE - Manufacture of fenspiride (claimed).    ADVANTAGE - The fenspiride is manufactured by a simple process under controlled reaction conditions, with an organic solution at normal pressure without an enclosed space, without using a complicated equipment and with reduced energy consumption and high efficiency. The manufacturing process is safe and short without using activated catalyst. The raw materials and intermediate products do not produce toxic substances, and pollution of the environment during the manufacturing process is suppressed.
NOVELTY - This utility model claims a kind of straw microwave carbonization device, belonging to the technical field of machinery. It solves the problem that the traditional agricultural biological carbon a carbon high temperature, long time consumption, low utilization rate and so on; The straw microwave carbonization device, comprising a containing chamber, the upper part is provided with a feeding port, the bottom is provided with discharging port of carbonization furnace, the side of the carbide furnace is installed with at least one capable of continuously generating the microwave generator, the microwave generator is connected with the chamber of the microwave guide tube with silicon carbide furnace, the feeding port is mounted on the upper part of the feeding machine, the discharging port of the lower part is set with a discharging machine. This utility model is generated by microwave generator of the microwave direct the straw and so on agricultural waste carbon energy-saving, green and environment-friendly and so on.
NOVELTY - This utility model claims a kind of continuous biomass carbonization device agitator, wherein the technical solution comprises a disturbance shaft, agitator blade seat is fixed on the disturbance shaft belt transmission system, agitator blade is arc-shaped, the inner arc is a feeding spiral blade is the same as the lower to the upper part of the extending angle alpha with the carbonization hearth tilt angle gap of the agitator blade edge with the carbonization furnace is 300 mm, the agitator blade and the agitator blade seat by a bolt mode. The utility model can block the heat transfer and reduce the material interlayer carbonization process of the biomass raw material fully, the carbonization effect, and capable of crushing fixed block of the bio-char so that it can smoothly output is suitable for thermal cracking carbonization of the biomass straw, saw dust, peanut shell and so on solid moulded fuel, which is good for producing high-quality of the bio-char.
NOVELTY - This utility model claims a biomass carbonizing device driving compactor, belonging to the technical field of renewable energy sources, wherein the technical solution comprises a spring device, a spiral conveying shaft, a spiral conveying blade, stirring, the stirring gear, a stirring shaft, a long guide rail, a spring locating device is welded on the spiral conveying shaft on the stirring shaft along the axial direction, a spiral conveying blade stirring, expansion spring is clamped on the upper end of the top cover, the lower end of the upper shaft end of the spiral conveying shaft, the top cover and the locating screw shaft and flexible moving, a spiral conveying shaft is sleeved on the stirring shaft, the stirring shaft can move along the axial direction, a stirring gear is spring teeth are distributed on the stirring. This utility model is used for driving the raw material stirring, filling and compacting, and it can realize the continuous, real time controlling feeding quantity, which is suitable for straw, saw dust, peanut shell and so on all kinds of biomass solid forming fuel, for preparing bio-char provides guarantee in the carbonization raw material enter into carbonization furnace.
NOVELTY - This utility model claims a kind of rice hull gasification and liquid impurity removing tar device, comprising a filter tank, the filter tank, the middle part is provided with multiple layers of filter screen, the filter tank of the filter screen are respectively connected with a feeding pipe and a discharging pipe, the discharging pipe is provided with a anti-overflow receiving groove, filtering pool is provided with a pool cover, wherein the bottom of the filter tank is connected with a liquid outlet pipe. This utility model has simple structure, simple manufacturing, can separate the vinegar liquid continuously used, reduce waste and is provided with anti-overflow receiving tank to prevent tar overflowing from the discharging pipe at the same time so as to fall on the ground;
NOVELTY - This utility model claims a small biomass fuel gas generator, comprising a reduction reaction area and pyrolysis area is located on the lower part of the regenerator through inlet connected with a fan, the periphery of the reduction reaction area is provided with a water tank, the right upper end is connected with a waste gas pipe, a left upper end is connected with water-gas tar separator, the left side of the oil-gas separator is connected with the filter, the left side of the filter is provided with a fuel gas pipe, a filter, a water-gas separator is connected with a tar reduction reaction section, the lower end of the water-gas separator is connected with a tar filter is provided with tar discharge port. After filling biomass raw material in reduction reaction area through the fan oxygen supply pyrolysis area fast pyrolysis to generate carbon monoxide and carbon dioxide gas, and reduction reaction to generate methane, hydrogen and carbon monoxide and waste gas, a cooling water tank, a cover to the coke oil gas separator for separating the gas and tar, and then the filter further decoking dust gas, the working process of cracking, high resource utilization rate, no discharge and environment-friendly.
NOVELTY - This utility model claims a kind of rice hull gasification extracting device, comprising a gasification furnace is on the gasification furnace is provided with rice hull feeding port, the gasification furnace through the pipeline is connected with a cooling tower, the cooling tower is connected with a static decoking device, for static coke catching device is connected with catching focus to the tar collecting tank, the air outlet is connected with a static electricity spray tower through the pipeline, the upper part of the spray tower is connected to the air storage tank through the air pipe, a spray tower is connected to the sewage tank by the drain pipe, the cooling tower is provided with two, and are connected with each other. This utility model has simple structure, uses gasification furnace gasification and cooling in order to remove the tar oil, finally collecting the gas, and the operation is simple.
NOVELTY - A non-solvent under the condition of plant sterol green method of preparing alkyl alcohol ester, involves plant stanol and catalyst in the absence of solvent, in the reaction test tube with the mouths 25 mL of adding a certain mol ratio of the constant temperature oil bath with magnetic force stirring, then under the protection of nitrogen atmosphere agitating and reacting for a certain time at a certain temperature, the reaction is finished to obtain stanol product. The adding amount of the catalyst is 0.5-5 mol% (relative to plant stanol mol), where the reaction temperature is 90-170 degrees C, the reaction time is 2-7 hours, at the same time, sampling at regular time, detecting the reaction process, and separating and purifying the obtained plant by column chromatography left alkyl alcohol ester product, using infrared, mass spectroscopy and spectroscopy analysis frame.    USE - For preparing plant stanol ester under solvent-free condition, used in food, medicine, or chemical industry (claimed).    ADVANTAGE - The method has simple technique and high production efficiency; it is convenient for mass production.
NOVELTY - This utility model claims a biomass fuel gas cyclone coke collecting device, comprising an air inlet pipe (1), a bottom plate (2), a drain pipe (3), a cylinder (4), a cover plate (7), an air outlet pipe (8), filter (11), pipe (12), wherein the cylinder body (4) under the welding bottom plate (2), a cylinder body (4) on the welding cylinder flange (6), a cover plate (7) of the air outlet pipe is welded (8), an air outlet pipe (8) extends into the lower opening of the cylinder body (4) at the lower part, and the lower welding filter pipe (11), a filter hole (11) are uniformly distributed on the surface of the small hole, the cylinder body (4) one side of the lower part is welded and cleaning pipe (12) and the other side of the cylinder body (4), the lower part is welded drain pipe joint (3), a cylinder body (4), the front left side of the upper part welding air inlet pipe (1). This utility model has advantages as follows: the biomass fuel gas cyclone coke collecting device has reasonable design, simple structure, and focus with the focus effect better and more complete.
NOVELTY - This utility model is a water fog filter and a hydrogen-oxygen hydrogen and oxygen producing machine is an automatic water replenishing device, the hydrogen and oxygen producing machine end is provided with an air outlet, the air outlet of air outlet pipe is connected with an automatic water replenishing device is set the bottom of the water tank and the hydrogen and oxygen producing machine is connected to an automatic water replenishing device is set, and the upper part of the hydrogen and oxygen producing machine, wherein the hydrogen and oxygen producing machine produced by electrolysis in the electrolytic groove water mist of gas by air outlet pipe flow upwards to the automatic water supplementing device for the bottom of the flume, the water, the water mist of gas water mist, and effectively filtering impurities of hydrogen gas, the hydrogen gas specific gravity and the purity of the pure oxygen gas and upwards to flow to cooling device on the upper end of the automatic water replenishing device, the plurality of filter tube body is step-shaped and the back gap flow path according to the effective to reduce the temperature of the pure oxygen gas, a flow to the engine of a motor vehicle, as alternative energy sources, the hydrogen and oxygen producing machine using the safety and practicability of the motor vehicle.
NOVELTY - A kind of sugar alcohol production neutralizing decolouring system, the neutralizing decolouring system device is connected with the buffer tank, a dispenser and the buffer tank is set with spraying nozzle, buffer tank, the top end is set with spraying nozzle, buffer tank is set with open barrel, a buffer tank is connected with the neutralizing decolouring kettle, at the same time, a buffer tank and the bottom of the opening, and the bottom of the buffer tank dispenser of the pipe is set with valve. This utility model is the system in two different positions is provided with two adjustable nozzle, a part of the device in the powder to wet or dissolved, and powder during this period can not enter into the outside air by the two nozzles, when the powder fully wet or dissolved, along with the water flow to the storage tank. The system has simple structure, the operation is very convenient, by neutralizing decolouring device, which avoids the problem of flying powder, reduces the pollution and disease, occupational health.
NOVELTY - This utility model claims a kind of solid organic waste plasma gasification process, wherein, comprising a feeding part, a drying device, a gasification furnace, a synthesis gas purifying device, the feeding part comprises a feeding device (1), a feeding channel (2), drying device comprises a drying hot air pipe (4), a wet steam outlet (10), gasification furnace comprising a gasification plasma spray gun (7), an adjusting pipe (6), a gasification chamber (8), a slag-drip opening (9), and a purified synthesis gas outlet (11), the synthesis gas purifying device comprises a secondary heating plasma spray gun (12), gas heating area (13), fly ash depositing area (14), fly ash settling tank (15), a dust outlet (16), and a purified synthesis gas outlet (17). This utility model high gasification efficiency, stable operation, without pollution.
NOVELTY - A kind of integrated micro-negative pressure marsh gas purifying device, comprising an air inlet, an air outlet and a box body, the air inlet and the air outlet are respectively welded on the head and tail two ends of the box body, a box body from the air inlet to the air outlet is orderly arranged with gas distribution chamber, a desulphurization/decarburization, a alkali, ammonia chamber, a chamber and a dehydrating chamber. The internal chamber is provided with a desulphurization/decarburization desulphurization/decarburization filler, removing ammonia in the ammonia chamber is provided with filler, dehydration chamber is a funnel is connected with a condensed water collecting groove. The drain opening is connected with a drain pipe and an automatic drain valve, which are distributed with a condenser pipe. This utility model is waste water, waste liquid, garbage, excrement, sludge and so on high thickness organic waste harmless and recycling treatment engineering provide a practical marsh gas purifying device, realizing the anaerobic digestion marsh gas desulfurization, decarburization and ammonia, purifying processing device of container for configuration, obviously improves the marsh gas purifying efficiency and reduces the marsh gas purifying and processing energy consumption and cost.
NOVELTY - This utility model claims one kind of biomass fuel production equipment. The biomass fuel producing device comprising: a cutting device, device is located on the side of the first cutting device and the second cutting rolling device side of the device, wherein the first cutter device the first distance between the saw tooth is greater than the rolling device and rolling press roller and the base of the third space and the second cutting device of a saw tooth is the second distance. The first cutting device, device and the second cutting device are respectively provided with an adjusting device to make the first distance between the first saw cutting device, the distance between the third rolling press roller and the base of rolling device and the second cutting device is a saw tooth is the second distance between the relative size can be adjusted, so as to satisfy different demands. In addition, this utility model has simple structure, convenient operation, low energy consumption, high production efficiency and low production cost.
NOVELTY - A kind of main frame, relating to a water electrolysis hydrogen production field of electrolytic technique. The utility model comprises frame main body, the frame main body is provided with a central hole, is provided with an annular groove on the back surface of the main frame body, an annular groove connected with the central hole. This utility model is the electrolytic groove whole length is shortened, a weight ratio of light and reduces the assembling difficulty and saves material and reduces cost.
NOVELTY - The electrolytic groove process of wrapping membrane gasket, referring to the water electrolysis hydrogen production field, especially a kind of wrapping membrane. This utility model comprises a diaphragm gasket main body is provided with four fluorine rubber fabric side at the periphery of the diaphragm gasket main body. The utility model on the original base, the thickness is increased, so as to achieve a better sealing effect, and the diaphragm pad itself is elastic, to avoid the loss of the respective gas.
NOVELTY - Environment-friendly comprehensive treatment method of household garbage and waste oil and fat involves sorting the household garbage, breaking the household garbage into garbage particles through breaking machine, drying and dry distillation on the garbage particles, obtaining charcoal through sealed spiral conveying machine, separating portion of waste oil and fat into two portions through oil and water separating system, treating other portion of wastewater through biochemical wastewater treatment system, and discharging processed wastewater reaching the standard.    USE - Environment-friendly comprehensive treatment method of household garbage and waste oil and fat (claimed).    ADVANTAGE - The method economically enables environment-friendly comprehensive treatment method of household garbage and waste oil and fat with excellent practicability, and high operability.    DETAILED DESCRIPTION - Environment-friendly comprehensive treatment method of household garbage and waste oil and fat involves sorting the household garbage, breaking the household garbage into garbage particles through a breaking machine, and conveying the garbage particles to a feeding hopper through a spiral transmitting machine, carrying out the procedures of pre-heating, drying and dry distillation on the garbage particles, obtaining charcoal through a sealed spiral conveying machine, separating portion of waste oil and fat into two portions through an oil and water separating system, and burning one portion of waste oil and fat as fuel through a hot blast stove to perform drying and dry distillation on the garbage and convert the garbage into charcoal, treating the other portion of wastewater through a biochemical wastewater treatment system, and discharging the processed wastewater reaching the standard.
NOVELTY - The system has a quick fluidized bed oxidizing furnace (1) arranged with an upper part of a primary cyclone separator (2). The primary cyclone separator is provided with a flue gas pipe (3). A bottom outlet is connected with a primary material returning valve (4) and a bubbling fluidized bed calcining furnace (5). A secondary material returning valve (6) is connected with the quick fluidized bed oxidizing furnace. A secondary cyclone separator (7) is connected with a carbon dioxide pipe (8). A heat packing auger (13) is connected with a lower part of the bubbling fluidized bed furnace.    USE - Three-phase reactor biomass pyrolysis system.    ADVANTAGE - The system reduces heat loss, ensures better biomass energy-saving effect and avoids environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a three-phase reactor biomass pyrolysis system working method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a three-phase reactor biomass pyrolysis system.'(Drawing includes non-English language text)'    Quick fluidized bed oxidizing furnace (1)    Primary cyclone separator (2)    Flue gas pipe (3)    Primary material returning valve (4)    Bubbling fluidized bed calcining furnace (5)    Secondary material returning valve (6)    Secondary cyclone separator (7)    Carbon dioxide pipe (8)    Heat packing auger (13)
NOVELTY - The device has a main body provided with a material lifting motor (1), a rotating motor (2), a distributor triangular bracket (3), an upper and lower sliding component (4), a distributor lifting track (5), a scraping and pressing material plate (6), a scattering material (7), a camera (8), a distributing console (9) and a control switch (10). The distributor triangular bracket is connected with the rotating motor and a support frame. The pressing and lifting operation lifting motor is connected with an oil wire rope through a distributing device.    USE - Material distribution monitoring device for a straw generator.    ADVANTAGE - The device avoids manual shifting operation and effectively monitors material surface layer combustion condition, material stack spreading and controlling operations so to avoid generation of flue gas and harmful gas and high-temperature explosion conditions, so that labor intensity can be effectively reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a material distribution monitoring device.'(Drawing includes non-English language text)'    Material lifting motor (1)    Rotating motor (2)    Distributor triangular bracket (3)    Upper and lower sliding component (4)    Distributor lifting track (5)    Scraping and pressing material plate (6)    Scattering material (7)    Camera (8)    Console (9)    Control switch (10)
NOVELTY - The system has a main control system (100) connected with a storage unit (200) by a control cable. A wind power unit (300) is provided with a wind turbine device (302) and an electric control module (301). The wind turbine device is connected with a water treatment sub-control module (401). A water treatment device (402) is fixed with a hydrogen sub-control module (501). An electrolytic hydrogen producing device (502) is installed with the wind turbine device by an electric power transmission line. An automatic intelligent conversion program is executed by the main control system.    USE - Hydrogen generation system.    ADVANTAGE - The system adopts the wind turbine device so as to provide electricity supply to an electrolytic hydrogen plant. The system ensure automatic control and saves energy. The system is environmental-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an hydrogen generation system.'(Drawing includes non-English language text)'    Main control system (100)    Storage unit (200)    Wind power unit (300)    Electric control module (301)    Wind turbine device (302)    Water treatment sub-control module (401)    Water treatment device (402)    Hydrogen sub-control module (501)    Electrolytic hydrogen producing device (502)
NOVELTY - The device has a plasma shell formed with an inlet and an outlet. A plasma generator (4) comprises a rectangular frame base (5) that is made of insulating material. Front and rear parts of the base are connected with an air flow uniformly distributing grid (18) that is uniformly formed with grid holes. An electrode leading-out wire passes through the base that is connected with a high-voltage alternating current (AC) power supply and a high-pressure end of a controller. The base and the plasma shell are linked together through a C-shaped channel steel part (15) and a fixing bolt (16).    USE - Large wind volume low-concentration plasma waste gas treating device.    ADVANTAGE - The device obtains high processing gas flow rate, realizes high-density large area plasma discharging process in steady-state and improves waste gas processing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a large wind volume low-concentration plasma waste gas treating device.    Plasma generator (4)    Rectangular frame base (5)    C-shaped channel steel part (15)    Fixing bolt (16)    Air flow uniformly distributing grid (18)
NOVELTY - This utility model claims a kind of stove, is a kind of double-control straw gasification furnace. A furnace body (1), a gasification chamber (3), a combustion chamber (6) and a double-layer water jacket (2). The characteristic is: the said gasification chamber (3) is provided with a fuel gas pipe (10), a fuel gas pipe (10) is connected into the combustion chamber (6), a gasification chamber (3) is provided with a wind cover (18), a furnace body (1) is provided with a blast pipe (13), a blast pipe (13) connecting the fan (14), a blast pipe (13) is set with a control valve (12), the lower section is equipped with a control valve (15), a blast pipe (13) is set with upper (11) folded gasification chamber (3) is connected fuel gas pipe (10), a blast pipe (13) at the lower end of the governing (16) is connected with the gasification chamber (3) under the wind cover (18). The beneficial effects are as follows: burning the biomass fuel for the same oxygen source respectively to upper and lower oxygen supply, oxygen supply amount can be determined according to the combustion condition is stable, the combustion is full, no air flow loss, and is featured with simple structure, low cost, convenient to operate, safe and reliable and so on, it is especially suitable for straw and so on, and the market prospect is considerable.
NOVELTY - The utility model claims a system for preparing sludge synthetic fuel, comprising a sludge feeding hopper, a sludge conveying device, a biochemical treatment mixing device, a biochemical processing mixing conveying device, curing process mixing device, a solidifying process mixing conveying device, a storage bin, a material conveying device, a mixing device, fuel synthesis fuel synthesis mixing conveying device, a crushing device, crushing material conveying device and a fuel forming machine, wherein the biochemical treatment device is connected with the mixing auxiliary material bin biochemical treatment through biochemical treatment auxiliary material conveying device, the curing process mixing device is connected with solidifying auxiliary material bin by curing treatment auxiliary material conveying device, biochemical process mixing device and curing process mixing device is respectively connected with the absorption tower, a fuel mixing device for synthesizing composite auxiliary material conveying device connected with the fuel through the fuel composite auxiliary material bin. This utility model can improve the sludge utilization rate, low energy consumption, small pollution, low cost, high safety, is suitable for all kinds of city sludge treatment.
NOVELTY - The electrolysis hydrogen furnace has an anode that is provided for generating oxygen (2) that is guided out by the oxygen conduit. The cathode is provided for generating hydrogen and is pressurized by the micro pressure pump. The generated hydrogen is stored in a hydrogen pressure storage tank (6), when the pressure is reduced by a pressure reducing valve (8) and supplied to the hydrogen burning stove.    USE - Electrolysis hydrogen furnace.    ADVANTAGE - The great amount of energy can be buffered, high-power release is performed in short time, and the fluctuation in the current can be avoided. The utilization rate of renewable energy is improved, and the pollution to environment is remarkably reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis hydrogen furnace.    Hydrogen burning furnace (1)    Oxygen (2)    Three-way valve (3)    Hydrogen pressure storage tank (6)    Pressure reducing valve (8)
NOVELTY - This utility model claims a kind of solid alkali catalyst device for continuously preparing biodiesel, comprising a raw material mixer, a metering pump, a heater, a reaction tower and distillation tower, this utility model make the material after stirring continuously to react in the reaction layer, and the glycerine separating disc is non-effective to recycle crude glycerine layer, product is easy to be separated and reduces the production cost of the energy at the same time, the production method is greatly simplified, there is no pollution and the economic benefit is improved.
NOVELTY - The method involves passing mixture of raw material oil and hydrogen gas by high and low temperature operation reactor. The hydrogen-rich gas separated from stream generated from hydrogenation is recycled. The sub-hydrogen gas separated from stream generated from hydrocracking is recycled. The separated liquid product is subjected to fractionation to obtain naphtha and low freezing point diesel oil. The active components of hydrogenation catalysts are used at two stages under reaction states. The sulfur containing light oil product is included for hydrogenation process.    USE - Two-stage hydrogenation method for producing high-quality low freezing point motor fuel from biological oil e.g. vegetable oil such as soybean oil, peanut oil, castor oil, rapeseed oil, corn oil, olive oil, palm oil, coconut oil, tung oil, linseed oil, sesame oil, cotton seed oil, sunflower seed oil and rice bran oil and animal oil (all claimed) such as butter, lard, mutton fat and fish oil.    ADVANTAGE - The activity stability of the catalyst can be ensured. The stable and long period hydrogenation operation can be ensured effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the production of high-quality low freezing point motor fuel from biological oil. (Drawing includes non-English language text)
NOVELTY - This utility model claims a kind of used for marsh gas purifying cooling water tank, comprising a barrel body and a sealing head is connected to the left and right ends of the cylinder body, the left end is provided with normal temperature water and low temperature water pipe, right end is provided with a water outlet pipe, a middle baffle plate is vertically provided with more than two baffle plates according to according to the order from the left to the right adjacent baffle plate is 20% to 40%, the total length of said baffle plate comprises a first baffle plate and a second baffle plate, the first baffle plate is a baffle plate of the left side of the baffle plate, the first baffle plate is located at the cooling water tank, the first baffle plate is 1/2% of the diameter of 2/3, the bottom baffle plate is located at the bottom of the cylinder is provided with a hole, and the second baffle plate is located at the middle part of the cylinder body, a baffle plate is 1/3% of the diameter of 1/2. This utility model is a cold water tank pump normal temperature technology water outlet pipe and low temperature technology water, the temperature of the water in the cold water tank, reducing the temperature to a predetermined temperature. So it greatly reduces the load of the cooling-water machine unit so as to reduce the operation cost.
NOVELTY - A kind of marsh gas purification and power generation control device, comprises in turn through a pipeline connected with the air storage tank, a desulfurizing tower, a carbon removing tower, dehydrating and drying tower, a compression air storage tank and air mixing chamber, air mixing chamber is connected with a generator set through a gas pipeline. This utility model, the electronic flow meter, a hydrogen sulphide gas detector, an electric air valve, an electric water valve and assorted software program comprising a control system, a marsh gas power generation before pre-processing system and a biogas power generation system integrated combination, an electronic programmed control to realize the marsh gas desulfurization, decarburization, drying, pressing, mixing, generating a integrated mounting bracket of SCR system operation according to the change of the intake air amount, air pressure, a ratio, and the compression ratio of the marsh gas and so on automatically adjusting operation condition in real time monitoring device, which can improve a device integration level to realize the automatic operation, continuous and stable system operation, easy to produce on scale, it can greatly reduce the production cost and improves the production efficiency.
NOVELTY - Copper (Cu)-containing hydrotalcite-based catalyst contains layered structure of hydrotalcite catalyst precursor obtained after calcination in which catalyst precursor consists of alkali metal ion solution obtained by co-precipitation which is a mixed solution of hydroxide and carbonate of sodium (Na) or potassium (K).    USE - Copper-containing hydrotalcite-based catalyst for synthesizing natural gas to produce mixed alcohol (claimed).    ADVANTAGE - Copper-containing hydrotalcite-based catalyst has large specific area, uniform particle size for dispersion, stable structure, long service life, and high selectivity, reaction activity is high, and reaction condition is mild and stable.    DETAILED DESCRIPTION - Copper (Cu)-containing hydrotalcite-based catalyst contains layered structure of hydrotalcite catalyst precursor obtained after calcination in which catalyst precursor consists compound of formula CuM (I) and alkali metal ion solution obtained by co-precipitation in which molar ratio of Cu/M1 is 1/0.05-1/10, C/M2 is 1/0.05-1/10, and Cu/M3 is 1/0.05-1/10, and alkali metal ion solution is mixed solution of hydroxide and carbonate of sodium (Na) or potassium (K).    M=M1, M2, and/or M3;    M1=Fe3+, Fe2+, Co2+, and/or Ni2+;    M2=Cu2+, Fe2+, Co2+, and/or Ni2+; and    M3=Fe3+.    An INDEPENDENT CLAIM is included for preparation of Cu-containing hydrotalcite-based catalyst which involves performing co-precipitation reaction to metal salt solution and alkali CuM at 10-80 degrees C at pH value of 3-13, aging at 0-90 degrees C for 2-5 hours, washing until filtrate is less than or equal to 8 to obtain precipitate cake, drying precipitate cake by air, and calcining at 250-700 degrees C for 1-5 hours.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the X-ray diffraction pattern of a catalyst precursor. (Drawing includes non-English language text).
NOVELTY - The method involves establishing an organic ecological type soil less culture system outside a snakehead pond and planting strawberry on underground water circulating pipeline. The snakehead pond is connected with purifying effect of soil less culture matrix and continuous purification is obtained. A culture medium is provided to obtain a purified aquaculture.    USE - Strawberry soil less culture method for purifying aquaculture water.    ADVANTAGE - The method enables providing water resource recycling, energy-saving, environment-friendly effects and obtaining sustainable development of target.
NOVELTY - A palm husk is baked at 170-410 degrees C under oxygen having concentration of 10% or less, to obtain solid fuel with yield of 70% or more.    USE - Manufacture of solid fuel used for powdered-coal boiler, power generation equipment, and incineration system (claimed).    ADVANTAGE - The method provides solid fuel having high calorie with high yield.
NOVELTY - Co-processing a biocomponent feedstock, comprises exposing the feedstock containing a mineral fraction and a biocomponent fraction to a supported group VI metal catalyst in the presence of hydrogen under effective deoxygenation conditions for forming a deoxygenated effluent, and exposing at least a portion of the deoxygenated feed to a hydroprocessing catalyst under effective hydroprocessing conditions to produce an effluent having a sulfur content of less than 100 weight parts per million (wppm).    USE - The method is useful for co-processing a biocomponent feedstock (claimed) on biological sources, such as feeds containing vegetable, animal, or algae oils or fats.    DETAILED DESCRIPTION - Coprocessing a biocomponent feedstock, comprises exposing the feedstock containing a mineral fraction and a biocomponent fraction to a supported group VI metal catalyst in the presence of hydrogen under effective deoxygenation conditions for forming a deoxygenated effluent, where the group VI metal catalyst comprises tungsten, physically promoted tungsten, or physically promoted molybdenum on a support, and the feedstock comprises less than 25 wt.% of the biocomponent fraction, and exposing at least a portion of the deoxygenated feed to a hydroprocessing catalyst under effective hydroprocessing conditions to produce an effluent having a sulfur content of less than 100 weight parts per million (wppm).
NOVELTY - The power generator (100) has air conduits (108,110) which are disposed near a fuel cartridge (112) in a housing (102). The air conduit is provided with a fuel cell section (118) and a selectively permeable membrane section (120). The air conduit directs oxygen from the air intake to the fuel cell section. The air conduit carries water vapor generated by the fuel cell section past the selectively permeable membrane section so that water vapor passes through the selectively permeable membrane section and causes release of hydrogen from the fuel cartridge.    USE - Power generator for powering portable electronic devices.    ADVANTAGE - Improves power density by heating the fuel in the removable fuel cartridge to produce hydrogen via thermolysis. Improves energy density by providing water to the fuel in the removable fuel cartridge to produce hydrogen via hydrolysis. Minimizes the consequences of the thermal runaway by dividing the fuel cartridge into a predetermined number of cells. Prevents thermal runaway when the power generator includes an exothermic fuel cell by dividing the exothermic fuel among the predetermined number of cells.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for generating power.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the power generator.    Power generator (100)    Housing (102)    Air conduits (108,110)    Fuel cartridge (112)    Fuel cell section (118)    Selectively permeable membrane section (120)
NOVELTY - A fuel composition (C1) comprises diesel fuel, a fusel oil distillate and ethanol.    USE - As fuel composition e.g. non-emulsified fuel composition (claimed) useful as fuel in engine e.g. internal combustion engine.    ADVANTAGE - The compositions are blends of ethanol and diesel fuel which are homogeneous. Such blends can be used directly as a fuel for any diesel powered vehicle, device or equipment, in place of conventional diesel fuel. The preparation of the blend can be done either at the distribution site where fueling of the vehicle, device or equipment takes place, or at a location where bulk quantities of fuel are prepared, such as a refinery or fuel depot. The composition is monophasic from -16 to 50 degrees C. The preparation of the compositions can be accomplished by splash blending, that is, by simple mixing of the diesel fuel, ethanol and fusel oil distillate prior to use. The miscibility of the components of the blend does not require any special equipment to form the blend. The fusel oil distillate is substantially free of water. The diesel fuel blending agent provides enhanced properties (e.g. improved homogeneity, viscosity index improvers, lowering of the cloud point, greater fuel efficiency) to the resulting blend.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of fuel composition involving splash blending of a fusel oil distillate with a mixture of diesel fuel and ethanol; and    (2) a method of using a product as a diesel fuel blending agent, where the product obtained by distillation of fusel oil and collection of portion boiling from 105-125 degrees C (preferably 117-125 degrees C).
NOVELTY - Preparing iloperidone comprises: (a) alkylation of acetovanillone with 1-bromo-3-chloropropane to obtain 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone intermediate in the presence of an inorganic base; (b) alkylation of 6-fluoro-3-(4-piperidinyl)-1,2-benzisoxazole hydrochloride by the 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone intermediate in the presence of an inorganic base, to obtain a reaction mixture containing iloperidone; and (c) isolation of iloperidone from the obtained reaction mixture.    USE - The process is useful for preparing iloperidone (claimed), which is useful for treating schizophrenia, bipolar disorder and other psychiatric conditions. No biological data given.    ADVANTAGE - The process: is a one-pot process; is performed without any intermediate isolation; provides the iloperidone with high purity (99%) and yield; does not need any work-up, isolation or purification steps; is environmentally friendly; and is efficient in increasing the conversion of acetovanillone to 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone, as compared to conventional processes.    DETAILED DESCRIPTION - Preparing iloperidone comprises: (a) alkylation of acetovanillone with 1-bromo-3-chloropropane to obtain 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone intermediate in the presence of an inorganic base; (b) alkylation of 6-fluoro-3-(4-piperidinyl)-1,2-benzisoxazole hydrochloride by the 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone intermediate in the presence of an inorganic base, to obtain a reaction mixture containing iloperidone; and (c) isolation of iloperidone from the obtained reaction mixture, where in the step (a), 0.9-1.2 molar equivalents, preferably 1 equivalent of 1-bromo-3-chloropropane with respect to acetovanillone are used, and the 1-(4-(3-chloropropoxy)-3-methoxyphenyl)ethanone intermediate is not isolated.
NOVELTY - An electrochemical apparatus (1) consists of solid oxide form electrolysis cell (10), hydrogen storage material (20) and heat-transport unit. The solid oxide form electrolysis cell electrolyzes water to produce hydrogen. The hydrogen storage material occludes hydrogen produced from electrolysis cell. The heat-transport unit conveys heat to solid oxide form electrolysis cell from hydrogen storage material.    USE - Electrochemical apparatus is used for electrical storage system (claimed) such as fuel cell, hydrogen production system and electric power generation.    ADVANTAGE - The electrochemical apparatus provides electrical storage system having excellent energy efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrical storage system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrochemical apparatus. (Drawing includes non-English language text)    Electrochemical apparatus (1)    Solid oxide form electrolysis cell (10)    Hydrogen storage material (20)
NOVELTY - The device has a liquid storage container (10) connected to hydrogen-generating unit (22) to store methanol and water. The solid hydrogen storage container (40) has gasification and solidifying module to produce hydrogen by gasifying solid hydrogen into gaseous hydrogen. A sub-device (21) is arranged to obtain hydrogen by residual combustion. The methanol steam is sent to reforming chamber which is at specific temperature after gasification. A pre-heating temperature control mechanism is used for heating output gas of reforming chamber and separation chamber.    USE - Movable-type device for producing hydrogen used as fuel in vehicle such as car and airplane and for air conditioner, from methanol and water. Can also be used in rocket, missile, submarine vehicle and in hydrogen cutting or welding of steel material.    ADVANTAGE - The space for arranging solid hydrogen storage container is reduced and hence the portability of the device is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrogen from methanol and water.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of movable-type device for producing hydrogen. (Drawing includes non-English language text)    Liquid storage container (10)    Sub-device (21)    Hydrogen-generating device (22)    Solid hydrogen storage container (40)
NOVELTY - The device has pyrolysis furnace (1), inner container that is provided on an outer tube, fire grate, discharge hole and air outlet pipe. Bottom of the inner container is connected with the discharge hole, and fire grate is arranged on the inner cylinder and the discharge hole. The inner container is uniformly distributed with multiple air outlet holes, outer cylinder and inner container to form annular air cylinder of air outlet pipe installed on the outer cylinder, and connected with tri-state purification separation device (2), air outlet pipe and air outlet hole gas channel.    USE - Biomass comprehensive transformation device for transforming biomass into biomass fuel gas, biomass vinegar original liquid, biomass tar and biomass carbon.    ADVANTAGE - Biomass comprehensive transformation device can efficiently transform the biomass into biomass fuel gas, biomass vinegar original liquid, biomass tar and biomass carbon, and does not produce secondary pollution to the environment. A biomass conversion rate is 0.5t/h-1.5t/h, and device is featured with simple structure and easy operation to simplify the pyrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass comprehensive transformation device.    Pyrolysis furnace (1)    Tri-state purification separation device (2)    Standing and separating device (3)    Solid separator (21)    Condenser (22)
NOVELTY - A bioalcohol from waste oil comprises 50 pts. wt. methanol, 10 pts. wt. ethanol, 13 pts. wt. acetone, 6 pts. wt. isobutanol, 3 pts. wt. hydrogen peroxide, 3 pts. wt. potassium permanganate, 2 pts. wt. camphor, 8 pts. wt. water, 8 pts. wt. stabilizing agent, 5 pts. wt. stabilizing agent from waste oil and 3 pts. wt. tung oil.    USE - Bioalcohol from waste oil.    ADVANTAGE - The bioalcohol is a renewable source of energy, high quality alternative to petroleum diesel with low cost and high heating value.    DETAILED DESCRIPTION - A bioalcohol from waste oil comprises 50 pts. wt. methanol, 10 pts. wt. ethanol, 13 pts. wt. acetone, 6 pts. wt. isobutanol, 3 pts. wt. hydrogen peroxide, 3 pts. wt. potassium permanganate, 2 pts. wt. camphor, 8 pts. wt. water, 8 pts. wt. stabilizing agent, 5 pts. wt. stabilizing agent from waste oil and 3 pts. wt. tung oil. The bioalcohol is prepared by taking cooking oil, glycerin and tung oil, heating at 280 degrees C, mixing uniformly, standing, adding methanol, ethanol and potassium permanganate, stirring and mixing, adding acetone and isobutyl alcohol, stirring and mixing, adding camphor, water and hydrogen peroxide, stirring, mixing and adding stabilizing agent.
NOVELTY - A solid fuel is prepared by adding dry sludge with 1-5 wt.% additive, dehydrating and drying until moisture content is 10-25%, pulverizing, sieving, and drying to obtain sludge raw material; dehydrating biomass, drying until moisture content is 10-25%, pulverizing, sieving, and drying to obtain biomass feedstock; and mixing sludge raw material and biomass feedstock, stirring to obtain raw material mixture comprising 30-70% raw sludge and 30-70% biomass feedstock, and extrusion molding at 90-130 degrees C and 50-80 MPa.    USE - Method for preparation of solid fuel (claimed).    ADVANTAGE - The method is low in cost, utilizes solid waste and biomass, saves energy, can be an effective solution to the treatment and disposal of solid waste and biomass, and has environment protection.
NOVELTY - The micro compression equipment comprises a storing device and a micro-generating device, where the storing device is used for marsh gas; and the micro-generating device is used for supplying fuel gas and the generated electric potential energy.    USE - The micro compression equipment is useful for purifying and collecting methane, which is useful in an electric energy of storage battery, electric vehicles including car and electric house hold appliances including light (claimed).
NOVELTY - Preparing biological oil comprises collecting the rice straw and then crushing to obtain rice straw powder having size of less than 1 mm, mixing the powder with water and kaolin to obtain slurry with solid-to-liquid ratio of 1:100-50:100, stirring the rice straw slurry into a high pressure reaction kettle at 200-350 degrees C for 5-180 minutes and then cooling to room temperature, collecting the reaction mixture and then extracting solid and liquid phases by solid-liquid separation using organic solvent, filtering the organic phase by removing the organic solvent to obtain the bio-oil.    USE - The method is useful for preparing biological oil containing fatty acid, dicyclopentadiene phenolic compound and ketone compound (all claimed).    ADVANTAGE - The method simply and economically prepares the biological oil with phenol compound content of more than 60% and less raw material source consumption, and without pollution.
NOVELTY - A kind of urban garden green waste biological treatment system, belonging to the field of chemical and environmental protection material biological treatment technology field. The sleeve system comprises a mixing system, distributing system, turning system, an oxygen supply system, a screening system, deodorization system and each system is connected to the production line, reasonable arrangement and adjusting technique device and overall operation sequence of the process improving the processing efficiency and the quality of the product. Comprises the following step: quantitative mixing, conveying, distributing, turning, sieving, for oxygen, and a monitor. This utility new type biological treatment function equipment, biological treatment rate is high, high screening efficiency, system integration, small floor space, low energy consumption. This utility model system for garden green waste biological treatment and biological treatment to other organic mixed material.
NOVELTY - A kind of water-saving biomass solid waste solid aerobic fermentation reaction device, comprising a fermentation reactor, a stirring device, a heating device, a collecting device and a temperature and humidity control device, the fermentation reactor is provided with inlet and outlet, the liquid feeding pipe inlet, a hot water inlet and outlet pipes and the exhaust fan, the stirring device comprises a motor and a spiral stirrer, heating device is a solar heating plate, heat exchanger in the fermentation reactor is set on the front wall and the back wall of water collecting device comprises a condensing cover, an overflow groove, a probe temperature-measuring sensor, and a humidity sensor of the collecting bottle and the water, the fermentation in the reactor and is connected with the temperature measuring instrument and measuring moisture meter of the control chamber. This utility model has advantages of low energy consumption, the device water rate is high, it is easy to operate, the cost is low, the first time adding water that is capable of the need for water in the microorganism ferment process water circulation in reactor and improving the growth metabolizing speed and efficiency, and it can be widely used for biomass solid aerobic fermentation system.
NOVELTY - The tank has a feed pipe and a discharge pipe (3), which are arranged on both corresponding bottom sides of the tank body (1). The tank body is connected with a storage pool through the feed pipe and connected with a biogas residue treatment plant through the discharge pipe. An air outlet pipe (9) is arranged at the top of the tank body and communicates the tank body and a biogas purification plant. The tank body is provided with a heating pipe, which connects the tank body and a heating boiler. A thermometer is arranged inside the tank for monitoring the internal temperature of the tank.    USE - Fermentation tank used in biogas engineering.    ADVANTAGE - Ensures biogas production in cold season by including a thermometer to monitor the temperature of the tank and a heating pipe that connects the tank to a heating boiler. Provides a tank that is set with simple structure, convenient and practical and has wide application and high gas production efficiency. Ensures the volume of container and stability of gas production since residue is thoroughly cleaned up.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structural view of the fermentation tank.    Tank body (1)    Discharge pipe (3)    Outlet valve (4)    Air outlet pipe (9)    Valve (10)
NOVELTY - The electrolysis bath has a blower (9) which is connected to the upper end of W-shaped fin tube type condenser (11). The left W-shaped fin pipe type condenser is connected with an oxygen-liquid separator (14), and a right W-shaped fin pipe type condenser is connected with gas-liquid separator (13). An electrolytic tank main portion is provided with a hydrogen side Y-type liquid collecting pipe (15), an oxygen side Y-type liquid collecting pipe, hydrogen side liquid transport tube (17) and the oxygen side liquid transport tube.    USE - Inner and outer combined air cooling type water electrolysis hydrogen preparing electrolysis bath.    ADVANTAGE - The hydrogen preparing electrolysis bath with good cooling effect, low manufacturing cost, small occupied area and small space can be achieved. The electro-hydraulic tube is provided for regular periodic cycle of filter pump, so that the service life and work reliability of filter pump can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cooling type water electrolysis hydrogen preparing electrolysis bath.    Blower (9)    W-shaped fin tube type condenser (11)    Gas-liquid separator (13)    Oxygen-liquid separator (14)    Hydrogen side Y-type liquid collecting pipe (15)    Hydrogen side liquid transport tube (17)
NOVELTY - Degrading straw cellulose to reducing sugar involves: adding buffer liquid to the straw cellulose; adding 1-7 ml of hydrochloric acid solution having concentration of 0.005-0.10 mol/l, to per 50 ml of buffer solution; pre-processing for 5-180 minutes to obtain the reaction solution; then adding cellulase to the reaction solution.    USE - For degrading straw cellulose to reducing sugar (claimed) used for producing ethanol fuel and other products.    ADVANTAGE - The present method simplifies the operation process technique; reduces the production cost; provides high saccharification rate than the existing technology; can be directly used for ethanol fermentation production; does not need the pre-process for the subsequent process; is simple and more environment-friendly; effectively reduces energy consumption; and saves the energy and time.
NOVELTY - This utility model claims a kind of fatty acid esterification, wherein said esterification device comprises a kettle body (2), the top of the kettle body (2) is provided with a condenser (5), kettle body (2) is provided with a valve (4) and the condenser (5), kettle body (2) close to the condenser (5) is set with a feeding port (3, 6, 7) end is provided with a discharging port (8), kettle body (2) is covered with a heating jacket (1). The utility model not only effectively solves the problem that the existing pre-processing waste animal oil and vegetable oil acid value by high vacuum evaporation method, equipment investment is large, the energy consumption is large, and has big energy consumption, production cost, and effectively solves the problem that the acid catalysis esterification reaction of fatty acid and methanol, fatty acid conversion rate is low, the methanol leakage, the value is reduced to the effective value of the problem.
NOVELTY - This utility model claims a kind of method of preparing biodiesel by ester exchange, wherein the device comprises a glycerol separating tank (2), a reverse reaction tower (3), counter-current reaction tower (3) is provided with glycerin separating tank (2) and are connected with each other, the upper part of the tower body counter-current reaction tower (3) is provided with a material inlet (5, 7, 8), a material outlet A (6), a tower body is provided with a porous sieve plate (4), glycerin separating tank (2) is provided with a material outlet B (1, 10), the box body is set with a baffle plate (9, 11, 12). The utility model not only effectively solves the problem that the existing homogeneous alkali catalysis method to prepare biological diesel oil, it not only device investment, complex process, for producing biodiesel with high cost, and effectively solves the problem that the existing homogeneous alkali catalysis method to prepare biological diesel oil to multi-stage catalytic reaction and separation steps to prepare the qualified biodiesel.
NOVELTY - The water electrolyzer has electrode (1) whose base material is made of lightweight graphite slab (11). The anode surface is provided with the graphene layer, and oxygen and hydrogen storage metal layer with low hydrogen overvoltage. An alloy layer is formed in the surface of cathode of electrode. An electric heat mechanism made of corrosion-resistant electric heat material or water-proof electric heat material is formed for providing heat in electrolytic cell.    USE - Water electrolyzer used in production experiment of hydrogen and oxygen gas and fuel-consumption experiment of diesel truck engine.    ADVANTAGE - The production efficiency of hydrogen and oxygen gas is improved, by forming graphene layer and hydrogen storage metal layer with low hydrogen overvoltage as anode layer. The power efficiency of the electrode for electrolysis can be improved. Since lightweight graphite slab is used as a base material for electrodes, the size and weight reduction of the water electrolyzer can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrode of water electrolyzer.    Electrode (1)    Graphite slab (11)    Vapor-deposited graphene layers (12,13)    Terminal hole (14)
NOVELTY - A fuel formation method involves mixing toner waste, and waste oil. The mixture is mixed with wood-based biomass to obtain solid fuel.    USE - Method for formation of fuel.    ADVANTAGE - The method enables forming fuel without the danger of a dust explosion, freezing inside of a tank, and occlusion of piping, in simple, easy and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid fuel obtained by a method.
NOVELTY - Flocculant production system is capable of chemically modifying cell wall of yeast, preferably deacetylating chitin included in the cell wall of yeast for producing chitosan flocculant. The flocculant is tinged with a negative charge, and is obtained by chemically sulfating or phosphorylating cell wall component of yeast.    USE - The system is useful for producing chitosan flocculant which is useful for aggregating sludge (claimed).    ADVANTAGE - The flocculant is cost-effective and biodegradable.
NOVELTY - Producing L-lactic acid, comprises hydrolyzing a woody biomass to give a sugar-containing substrate; and subjecting the substrate to lactic acid fermentation with the use of microorganism belonging to the genus Bacillus having 16S ribosomal DNA base of SEQ ID No.1 (Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication) or Bacillus SANK 70182 strain, where the substrate is not sterilized by heating and the fermentation temperature is controlled to 45-60 degrees C.    USE - The process is useful for producing L-lactic acid.    ADVANTAGE - The process provides highly pure L-lactic acid in low cost by reducing production costs including raw material, medium and equipment.
NOVELTY - The system (1) has a hydrogen storage unit (92) that stores the water accompanying the hydrogen which is generated in a reversible cell (10) at the time of a water electrolysis operation. A piping (83) directly connects an air layer unit of a tank (41) and a bottom unit of a tank (82). The flow paths supplies raw air taken in from in-air to the oxygen side of the reversible cell at the time of fuel cell operation. The flow path supplies hydrogen from the hydrogen storage unit to the hydrogen side of the reversible cell at the time of the fuel cell operation.    USE - Charging/discharging system for use as electric power storage system.    ADVANTAGE - The charging/discharging system can be operated efficiently without providing auxiliary machines such as gas-liquid separation tank of hydrogen and makeup tanks. Since the contact with the electrical power collector is made uniform, the conductor resistance is reduced and hydrogen production efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of charging/discharging system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the charging/discharging system.    Charging/discharging system (1)    Reversible cell (10)    Tanks (41,82)    Piping (83)    Hydrogen storage unit (92)
NOVELTY - Methanol gasoline additive comprises 90-99% methanol, 0.1-0.3% n-butanol, 0.1-0.5% isopropyl alcohol, 0.5-1% oil acid, 0.2-1% liquid paraffin, 5-10% oil, and 0.0005-0.001% octane. The gasoline is prepared by adding components through pump circulation or aeration, stirring uniformly, or cycling uniformly to finish whole operation flow to form product.    USE - Methanol gasoline additive, and its preparation (claimed).
NOVELTY - Methanol diesel comprises 100-300 pts. wt. methanol, 400-700 pts. wt. diesel oil, 50-200 pts. wt. fatty acid, 20-150 pts. wt. oil acid, 1-15 pts. wt. cosolvent, 20-100 pts. wt. aviation kerosene, 0.1-5 pts. wt. cetane number improver, and 1-10 pts. wt. zinc peroxide.    USE - Methanol diesel.    ADVANTAGE - The methanol diesel has large methanol usage, better fossil diesel fuel miscibility, improved performance, and can be used as No. - 20 diesel. It is safe, environment friendly, and has low raw material cost. It has simple preparation and mild reaction condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol diesel by uniformly mixing methanol, fatty acid and oil acid to form mixture A; uniformly mixing diesel oil, cetane number improver, and zinc peroxide to form mixture B; mixing mixtures A and B, and aviation kerosene; adding cosolvent; and uniformly stirring to obtain methanol diesel.
NOVELTY - Gas desulfurization comprises, carrying out anaerobic biochemical treatment, passing through fan booster into washing tower, cooling, entering into the wet desulfurization tower, countercurrent contacting with sodium carbonate and catalyst, removing moisture, further removal of hydrogen sulfide with amorphous iron oxyhydroxide desulfurizer, entering hydrogen sulfide-rich liquid into regeneration tank for absorption, oxidizing hydrogen sulfide ion to elemental sulfur, separating sulfur in the form of foam, recycling desulfurization solution, steam heating sulfur foam for recycling.    USE - Method for gas desulfurization used for biogas (claimed).    ADVANTAGE - The method has a large processing capacity and long service life, is stable, recovers sulfur, easily regenerates desulfurizer, ensures to meet hydrogen sulfide standard requirement, extends service life of gas pipes, and prevents secondary pollution.    DETAILED DESCRIPTION - Gas desulfurization comprises, carrying out anaerobic biochemical treatment, subjecting to fan booster at 8-10.0 MPa into washing tower, cooling to 25-30 degrees C, entering filler into the wet desulfurization tower, countercurrent contacting with 2-3 g/L sodium carbonate and 4 ppm catalyst to remove hydrogen sulfide impurities, removing moisture by dehydration tower, further removal of hydrogen sulfide with amorphous iron oxyhydroxide desulfurizer to 15 mg/ Nm3, entering hydrogen sulfide-rich liquid into regeneration vessel for absorption, oxidizing hydrogen sulfide to elemental sulfur with desulfurization solution in the presence of oxygen, separating sulfur in the form of foam from the regeneration vessel, recycling desulfurization solution, steam heating sulfur foam for recycling.
NOVELTY - Culturing microorganism for producing oil, involves adding 20-90 wt.% xylose and 5-75 wt.% cellobiose as carbon source in a microbial culture medium, at a pH 4-8.    USE - In culturing microorganism for producing oil (claimed), microbial grease and biodiesel.    ADVANTAGE - The method shortens the culturing period; improves the production efficiency and utilization rate of raw material; reduces cost; and improves the economical efficiency of microbial oil.
NOVELTY - Producing 2,3-butanediol involves fermenting Bacillus subtilis (CTCCM2009200) strain in culture medium containing crude glycerine from biodiesel. The method is performed in seed culture and fermentation culture by inoculating the seed solution to fermentation culture medium at 37 degrees C, and stirring speed of 350 revolution per minute (r/min); carrying out fermentation culture; adding the crude glycerine so that the concentration of the glycerol in the culture solution is maintained at 0-20 g/l, then stopping fermentation.    USE - For producing 2,3-butanediol (claimed), which is used in biological engineering fermentation technology.    ADVANTAGE - The process has high yield i.e. 70 g/l; and reduces the production cost.
NOVELTY - Wood biomass fuel combustion mechanism comprises chassis support (1), hearth (21) provided with grate (211) at lower part, incinerator (2) fixed at one end of chassis frame and provided with jacket (22), feeding port (23) connected with combustion-supporting air introducing mechanism (3), furnace cover (24), flame ejection mechanism (4) connected to incinerator, feeding mechanism (5) set on other end of chassis frame, biomass fuel supply tank (6), power transmission mechanism (7) and oxygen supply mechanism (8). The grate is provided with high alumina particle bedding (2111).    USE - A wood biomass fuel combustion mechanism.    ADVANTAGE - The mechanism has simple structure, high combustion efficiency and good environment protection capability. It saves raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wood biomass fuel combustion mechanism.    Chassis support (1)    Incinerator (2)    Air introducing mechanism (3)    Flame ejection mechanism (4)    Feeding mechanism (5)    Supply tank (6)    Power transmission mechanism (7)    Oxygen supply mechanism (8)    Hearth (21)    Jacket (22)    Feeding port (23)    Furnace cover (24)    Grate (211)    Alumina particle bedding (2111)
NOVELTY - Biological organic-inorganic mixed fertilizer comprises inorganic nutrient nitrogen, phosphorus and potassium, dry-mixed granular fertilizer, particle fertilizer, phosphate fertilizer particle such as diammonium phosphate, Urea and granular potash fertilizer.    USE - Biological organic-inorganic mixed fertilizer used for improving soil and crop quality.
NOVELTY - Producing ethanol by using fermenting gas phase substrate involves fermenting synthetic gas containing carbon monoxide (CO) and/or hydrogen (H2) in microbe culture bioreactor to obtain fermentation liquor and fermented tail gas; processing fermentation tail gas; mixing the post-processing fermented tail gas and fresh synthesis gas mixture into the reactor; separating the bacteria by centrifugation/filter membrane assembly/ultra-filtration, and returning separated bacteria to bioreactor; separating organic matter solution of bacteria to carry out rectifying to obtain ethanol.    USE - For producing ethanol (claimed), which is useful as fuel.    ADVANTAGE - The product produces ethanol having high yield, and little byproduct; reduces gas purification cost; reduces discharge of pollutant; and improves conversion rate of carbon monoxide (CO) and hydrogen (H2).    DETAILED DESCRIPTION - Producing ethanol by using fermenting gas phase substrate involves fermenting synthetic gas containing carbon monoxide (CO) and/or hydrogen (H2) in microbe culture bioreactor to obtain fermentation liquor and fermented tail gas; processing fermentation tail gas by separating carbon dioxide from the fermented tail gas with enriched fermentation of CO and/or H2 in the tail gas; mixing the post-processing fermented tail gas and fresh synthesis gas mixture into the reactor; separating the bacteria by centrifugation, filter membrane assembly made of hollow fiber, or ultra-filtration, and returning the separated bacteria to the bioreactor; separating the organic matter solution of bacteria to carry out rectifying to obtain the ethanol, and the remaining residual liquid return to the bioreactor.
NOVELTY - Producing ethanol using wood fiber raw material involves mixing wood fiber raw material with dilute acid; then dehydrating the material, to obtain dehydrated material; adding dehydrated material into water, to obtain dry matter concentration; hydrolyzing cellulase at pH of 1-7, to obtain pentose, hexose and lignin enzymolysis liquid; fermenting enzymolysis liquid to remove lignin to obtain a solution of pentose and hexose; concentrating solution at anaerobic condition having pH value of 3-8, to obtain fermented mash of ethanol; followed by fermenting and concentrating.    USE - For producing ethanol using wood fiber raw material selected from corn straw, rice straw, wheat straw, straw or beanstalk (claimed), where ethanol is used as a fuel in combustion industry.    ADVANTAGE - The process produces ethanol having high yield, and high purity i.e. 95%; is environment-friendly process; and reduces energy consumption of the subsequent ethanol concentration.    DETAILED DESCRIPTION - Producing ethanol using wood fiber raw material involves mixing wood fiber raw material with dilute acid by continuous impregnation at 20-80 degrees C for 1-15 minutes; then dehydrating the material at 80-200 degrees C and at a pressure of 0.4-10 MPa for 1-35 minutes, to obtain dehydrated material; adding the dehydrated material into water at 30-70 degrees C, to obtain dry matter concentration; hydrolyzing cellulase at a pH of 1-7 for 8-120 hours to obtain pentose, hexose and lignin enzymolysis liquid; fermenting the enzymolysis liquid to remove lignin to obtain a solution containing pentose and hexose; concentrating the solution with bacteria at 20-45 degrees C and at anaerobic condition having pH value of 3-8 for 8-120 hours to obtain fermented mash of ethanol; and fermenting and concentrating the fermented mash of ethanol, to obtain 95% ethanol.
NOVELTY - A reaction system comprises a chitosan, grease, Cystofilobasidium and carbohydrate.    USE - For producing oil including medium-chain fatty acid and unsaturated fatty acid and grease, used as bio-diesel (claimed).
NOVELTY - This utility model claims a preparation system of biomass moulded fuel and efficient use, aiming at providing a method for improving slurry stability of the device. A device for containing a slurry of the storage tank or stirring tank, bubble generating device is provided with storage tank or at the bottom of the stirring tank, a bubble generating device comprises a plurality of groups of row pipe or tube at the bottom of the tank, and outlet tube or pipe is connected by a connecting pipe, the air inlet of the outlet pipe or tube is connected to the compressor, 0.1 power supply is provided by a compressor to compress air at 0.4MPa. This utility model uses the air bubble device is simple and easy, which can greatly improve the stability of the slurry, at the same time, is provided with stirring to slurry, and wide application range. Adopted foaming agent low price, easy. In addition, has large amount of bubbles is more helpful for slurry pipeline conveying and atomization burning.
NOVELTY - This utility model claims a kind of synthesis gas methanation flow transformation period operation reaction device, belonging to the field of coal chemical industry. The reaction device comprises a reactor unit and a heat exchange device, wherein the reactor unit is divided into three layers of a packed bed catalytic reactor, the two two-position three-way valve, two through a disconnecting valve with a connecting pipe, the heat exchange device comprises a raw material pre-heating heat exchanger and a heat recovery heat exchanger, the said heat recovery heat exchanger is connected with a raw material pre-heating heat exchanger by the pipeline so as to product gas with waste heat to the raw material gas preheating, in practice according to the need, also can be the three reactor units connected to a combination so as to improve the content of methane in the product gas and improve the stability of the whole process. This utility model of device performance is stable, the equipment investment and operation cost is low, and it can prolong the service life of the catalyst.
NOVELTY - This utility model claims a low energy consumption and low cost of the multi-frequency ultrasonic radiation overflow groove continuous producing device of the biodiesel, comprising a raw material tank, methanol-catalyst jar, glycerol separation tank, tank, washing tank, a hot water tank, methyl tank, a waste water tank and fractionation device, a pre-esterification reaction kettle and gradually overflow multi-frequency ultrasonic reactor. Capable of efficient, energy-saving, low consumption production of bio-diesel. This utility model is added with multi-frequency reverberant ultrasonic field on the basis of the continuous producing device of the biodiesel, it enhances the mass transfer and heat transfer of the ester exchange reaction, it is a kind of fast speed, high efficiency and continuous producing device of the biodiesel.
NOVELTY - A kind of alcohol-based fuel deodorization device, comprising a smell-removing tank, a feed pipe, a spray head and a discharge pipe, the delivery pump is set with control of the control panel to the surface, the smell-removing cavity is provided with a fuel smell-removing layer, the fuel odour smell-removing layer is set on the inner cavity middle part cross section, and a smell-removing tank is fixedly connected with the inner wall of the bottom of the smell-removing tank is provided with a discharging port, the discharging port is fixedly connected with the discharge pipe. When the utility model is beneficial at: using this utility model, the peculiar smell and can eliminate alcohol group fuel emitted by the 80%, and can effectively eliminate alcohol volatile gas from the, it can effectively protect the using alcohol-based fuel people;
NOVELTY - Preparing solid dispersion of nimodipine comprises taking nimodipine as active component and hydrophilic carrier material according to mass ratio of 1:2-1:15, uniformly mixing in a high pressure kettle, filling supercritical carbon dioxide fluid at a temperature of 30-80 degrees C for 2-24 hours and a pressure of 10-40 MPa, and decompressing collected product in the kettle.    USE - The method is useful for preparing solid dispersion of drug nimodipine (claimed).    ADVANTAGE - The method: allows simple preparation of the solid dispersion of nimodipine with promoting absorbing effect in an environmentally-friendly manner; and is suitable for industrial production.
NOVELTY - Optimizing mixed anaerobic fermentation using microalgae, comprises inoculating microalgae into an anaerobic fermentation tank, setting an artificial light source in the anaerobic fermentation tank or using natural light source via the transparent top part of the anaerobic fermentation tank, adding solid oxygen adsorbent into the anaerobic fermentation tank and performing anaerobic fermentation.    USE - The method is useful for optimizing mixed anaerobic fermentation using microalgae (claimed).    ADVANTAGE - The method: is economical and simple and easy to operate; ensures absorption of carbon dioxide in biogas by photosynthesis during the growth of microalgae and absorption of carbon, nitrogen, phosphorus and other nutrients by the fermentation culture medium and hence improves the relative proportion of methane in biogas, upgrades biogas quality and reduces pollution load of discharged biogas; and utilizes solid oxygen adsorbent, which absorbs the oxygen produced during microalgae photosynthesis process and hence maintains anaerobic environment within the fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic fermentation device (Drawing includes non-English language text).
NOVELTY - A heterogeneous catalyst contains zeolite particles having particle size of 0.25-0.50 mm, and zeolite particles exchange ions, with metal alkoxide (1M-5M). During ion exchange, the ratio of zeolite and metal alkoxide mixture is 1:2, and the mixture is agitated for 1 hour at 50-60 degrees C. The agitation is repeated for at least 3 times and the zeolite particles are dried for 2 hours at 110-150 degrees C.    USE - Heterogeneous catalyst is used for manufacturing fatty acid methyl ester, and for producing biodiesel (claimed).    ADVANTAGE - The heterogeneous catalyst is economical and efficient, and has excellent reusability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fatty acid methyl ester.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the manufacture method of zeolite catalyst. (Drawing includes non-English language text)
NOVELTY - The biofuel cell (1) has an external circuit (30) that is connected with positive and negative electrodes (23,11). The electrodes are arranged in the positive and negative electrode regions (7,5). A proton-permeable membrane (9) is arranged between positive and negative electrode regions. A biological catalyst with crushed matter is accommodated in the negative electrode region. The negative electrode region is separated into an electrode region (15) and a crushed matter region (17). The crushed matter is accommodated in the crushed matter region.    USE - Biofuel cell e.g. hydrogen fuel cell.    ADVANTAGE - The electric power generation efficiency of biofuel cell can be improved effectively when disposable material is utilized as the fuel, since negative electrode region is separated into electrode region and crushed matter region. The arrival of electron at surface of negative electrode can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biofuel cell.    Biofuel cell (1)    Negative and positive electrode region (5,7)    Proton-permeable membrane (9)    Negative and positive electrode (11,23)    Electrode region (15)    Crushed matter region (17)    External circuit (30)
NOVELTY - Silica and metal alkoxide are subjected to sol-gel process, to obtain support (51a). Silane coupling agent having thiol group is reacted with support, and thiol group is added to the surface of support or mixture of silica from silane coupling agent having thiol group, metal alkoxide and thiol group are added to the surface, to obtain support (51b). The thiol group is oxidized by oxidizing agent and sulfo group (52) is generated on surface of support, to obtain solid catalyst.    USE - Manufacture of solid catalyst used for producing polysaccharide (claimed) for biofuel and bioplastics.    ADVANTAGE - The method provides solid catalyst having high catalyst life. The polysaccharide having reduced energy consumption is economically and efficiently manufactured with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of saccharide, which involves saccharifying polysaccharide at predetermined temperature in presence of solid catalyst; and    (2) continuous saccharification apparatus, which has reaction container accommodating solid catalyst and reaction solvent in which reaction solvent containing monosaccharide is decomposed within the container, solid-liquid separator for separating solid catalyst, and return path which returns separated solid catalyst to reaction container.    DESCRIPTION OF DRAWING(S) - The drawing shows a typical view of solid catalyst.    Supports (51a,51b)    Sulfo group (52)    Support metal (53)
NOVELTY - The installation has steam generation unit which collects potential heats of dry waste gas emitted with indirect heating type drying machine, and to generate vapor. Steam generation unit generates vapor to make heat source of combustible gas. Pressure rise unit pressure-rises vapor by making into drive source. Machine compression unit compresses vapor pressure-risen by rise unit. Machine compressed vapor supply unit supplies compressed vapor as heat source that dries to-be-processed object with indirect heating type drying machine.    USE - Heat-processing installation in heating drying machine used for drying of woody biomass including drying of resin, foodstuff, organic substance, organic waste, etc.    ADVANTAGE - The vapor generated to perform the pressure rise reliably with an ejector. The heat amount of the dry waste gas emitted with indirect heating drying machine can be recovered economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of utilizing heat source of drying machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the heat-processing installation. (Drawing includes non-English language text)    Sludge feed pump (1)    Mixer (2)
NOVELTY - Preparing crystalline form C of prasugrel hydrobromide, comprises: either (a) dissolving prasugrel in a solvent comprising ketones, preferably methylethylketone or methylisobutylketone and/or esters such as ethyl acetate, (b) adding a source of hydrobromic acid to the solution obtained in step (a), and (c) isolating crystalline Form C of prasugrel hydrobromide; or (a1) dissolving or suspending prasugrel hydrobromide in a solvent, and (b1) isolating prasugrel hydrobromide Form C by cooling the solution or suspension obtained in step (a1).    USE - The process is useful for preparing crystalline form C and amorphous form of prasugrel hydrobromide (all claimed), which is used for the treatment or prophylaxis of acute coronary syndrome and thrombosis or embolisms. No biological data given.    ADVANTAGE - The process allows simple and economical preparation of the crystalline form C of prasugrel hydrobromide with desired particle size distribution, improved stability and yield and high purity in an environmentally-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an amorphous form of prasugrel hydrobromide;    (2) preparing amorphous form of prasugrel hydrobromide comprising (a2) providing a solution of prasugrel hydrobromide in a solvent, and (b2) isolating the amorphous form of prasugrel hydrobromide by removing the solvent;    (3) a crystalline form of prasugrel hydrobromide having PXRD pattern with characteristic peaks as given in the specification;    (4) preparing crystalline form of prasugrel hydrobromide, comprising (a3) slurrying the crystalline Form A of prasugrel hydrobromide in acetonitrile, and (b3) isolating the crystalline form of prasugrel hydrobromide; and    (5) a pharmaceutical composition comprising the crystalline form C, amorphous form or crystalline form of prasugrel hydrobromide and carrier.
NOVELTY - Biosynthesis of silver nanoparticles comprises: exposing mycelial mat of Magnaporthe oryzae into a solution to harvest the cell filtrate under specific conditions; and adding silver nitrate salt, where the secreted extracellular enzymes reduce silver ions to silver nanoparticles.    USE - The method is useful for biosynthesis of silver nanoparticles, which are useful: as antibacterial and antifungal agents; as biopesticidal agents in crop field; as apoptogenic agents (all claimed) to treat cancer; as quantum dots, nanorods, nanowires and potential biomarkers; and in cell labeling, bio-imaging, and drug delivery systems. Test details are described but no results given.    ADVANTAGE - The method: is simple; is eco-friendly; does not give rise to harmful byproducts; provides silver nanoparticles having a total antioxidant capacity, which is higher than the total antioxidant capacity of cell filtrate and ascorbic acid, where the total antioxidant capacity is estimated based on the formation of phosphomolybdenum complex; produces silver nanoparticles with naturally protein capped structure for purpose of stabilization into the cell, where artificial capping of nanoparticles when prepared synthetically requires a complex expensive means and a strong interaction between nanoparticles and the coat protein; produces silver nanoparticles that exhibit apoptogenic property in a dose dependent manner in eukaryotic cells (claimed); does not require specialized equipments; and is cost effective.
NOVELTY - Bacterial or biofertilizer composition comprises strains of Pseudomonas fluorescens, Herbaspirillum frisingense, Herbaspirillum sp. and Bacillus subtilis isolated from forage grass Bouteloua gracilis. The composition is formulated with agronomically acceptable carrier, which serves as a vehicle for bacterial strains to maintain viability of bacteria for 5-9 months at minimum concentration of 10-109 colonies forming unit (CFU) per gram or milliliter of final formulated product.    USE - Bacterial or biofertilizer composition used for increasing production of agricultural crops after applying the composition on seeds, roots, seedlings, leaves, stems and fruits of plants, and soil or substrate.
NOVELTY - The utility model claims a kind of solar energy heater and the solar energy use system for producing biological diesel oil, the phase change heat accumulating type solar heater, comprising a phase-transition energy-accumulating heater, a solar heat collector and a supporting phase change heat storage heater and solar heat collector bracket, phase change heat storage heater comprising a box body, a heat pipe, and a phase-transition energy-accumulating material. For producing biological diesel oil by using solar energy system, comprising the phase change heat accumulating type solar heater, an oil container, a device, a circulating pump, a control device and a solar power supply. The solar energy power supply is a device, a circulating pump and a control device;
NOVELTY - This utility model claims a biomass fuel gas purifier, comprising a front panel (1), a radiating cover (2), a back panel (6), a base (20), a bottom panel (21), a left side plate (22), a dust baffle plate (23), pipe (24), a sieve plate (28), a dust catcher (29), inlet and outlet (31) and the bent pipe (35), a radiating hole (39), a top panel (40), an upper clapboard (53), an air outlet (56), the upper tube plate (59), heat exchanging pipe (60) and the right side plate (61), a water outlet pipe joint (62), lower tube plate (63). This utility model has advantages as follows: the biomass fuel gas purifier has simple structure, reasonable design, can ensure high efficiency, stable operation, improves the purifying effect and saves space.
NOVELTY - This utility model claims a kind of improved production line of methanol gasoline comprises gasoline component section, additive field, the production tank, standing tank, a finished product tank, gasoline component area, and additive field meet a production tank through the pipeline connected with, the production tank and a standing tank, a finished product tank in turn by the pipeline, wherein the production tank is provided with a pipeline and a circulating pump for circulating system is connected with a soft pipe on the circulating system tank, the other end is connected with the special additive. Because of adopting said structure, on the basis of the existing production facility is added with a pipeline, the circulating pump by the existing small special additive is present in an amount for producing suction tank without reopening the hole with special additive mentioned tank top removing, to ensure the safety of the operator, at the same time, and improves the efficiency of adding special additive.
NOVELTY - This utility model claims a methanol gasoline production pipeline, it comprises additive raw material tank, a gasoline raw material tank, gas production tank, a pipeline placing the semi-finished product tank and a finished product tank, additive raw material tank discharge pipe is connected to the gasoline production tank feeding pipe, a gasoline raw material tank discharge pipe connected to the pipe E connected to point D is connected to the gasoline production tank discharge pipe and standing the semi-finished product tank feeding pipe through a pipeline A, gasoline production tank discharge pipe is connected with standing the semi-finished product tank feeding pipe, standing the semi-finished product tank discharge pipe is connected to the finished product tank, a feeding pipe and a discharge pipe for gasoline production tank and the product tank, standing and additive raw material tank and a discharge pipe of the gasoline raw material tank are provided with valve, the gasoline raw material tank discharge pipe of the pipeline A between the valve and the connecting point D on the tapping a pipeline B to produce gasoline tank feeding pipe, the pipeline B with a valve. The utility model is provided with the oil production efficiency, and realizes pipe for further use, a multifunctional tank, which saves the process.
NOVELTY - This utility model claims a biogas purifying for the desulfurizing tower, comprising a tower body, wherein the tower body is provided with at least one section packing layer, side of the bottom is provided with a charging hole, a discharging hole, an air inlet pipe and a drain pipe, a feeding hole and a discharging hole is located on the tower body of the filler layer of the tower body is provided with a marsh gas outlet pipe and a drainage pipe, gas inlet pipe is connected with the tower body of the distributor. This utility model is used for marsh gas purifying tower as the service process flow to process unit, crisp advanced technology, low cost, safe and effective, and it is convenient to popularize the purpose and innovative. It not only ensures the technical index, but also for large scale reduces the height and the weight of the equipment, saves the construction cost, reduces the manual operation cost, at the same time reduce the resistance of the device and improves the efficiency of desulphurization.
NOVELTY - Composite fuel comprises 15-35 wt.% sewage treatment plant domestic sludge, 15-70 wt.% carbonized biomass toner, 10-50 wt.% crushed biomass raw material, and 0.8-2 wt.% coal agent.    USE - Composite fuel.    ADVANTAGE - The composite fuel is energy saving, protects the environment, and has reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composite fuel production comprising preprocessing the raw materials, biomass raw material crushing, uniformly mixing with sewage treatment plant domestic sludge, carbonized biomass toner, and coal agent for 8-72 hours, drying the mixture, and shaping.
NOVELTY - This utility model claims a sewage treatment plant by using sludge to save the energy and reducing the system, comprising of the aeration tank, concentrating tank, a fermenting tank, a marsh gas purifier, marsh gas generator and dryer, the marsh gas generator at the same time is connected with the aeration tank and a fermenting tank. To reduce the sludge treatment cost of sewage sludge volume is greatly reduced and it is convenient to transport and manage, which avoids the treatment field large floor area, bad smell and so on, reduces the sewage plant sludge treatment and transportation cost, effectively using the sludge contained in the energy, avoids resource waste, reducing the consumption of sewage process, and it further reduces the investment and operation cost of the sewage.
NOVELTY - Scenedesmus (CHX1) with preservation number CGMCC No. 6649 is new. Scenedesmus is isolated from swine wastewater treatment tank.    USE - The Scenedesmus (CHX1) is useful in the treatment of swine wastewater for removing nitrogen and/or phosphorus, and for producing biodiesel (all claimed).    ADVANTAGE - The Scenedesmus (CHX1): efficiently removes nitrogen and phosphorus in the wastewater; has high biological yield and oil yield; and produces fatty acids with more than 70% 16-18C content.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) Scenedesmus optimizing culture medium comprising 1 ml A5+Co solution, 5 g glucose, 3 g sodium nitrate, 0.04 g dipotassium phosphate anhydrate, 0.075 g magnesium sulfate heptahydrate, 0.036 g calcium chloride dihydrate, 0.006 g iron-ammonium complex of formula (Fe(NH4)3C18H10O14), 0.001 g disodium EDTA, and water (remaining amount), where A5+Co solution comprises 2.86 g boric acid, 1.81 g manganese chloride hydrate, 0.222 g zinc sulfate heptahydrate, 0.079 g copper sulfate pentahydrate, 0.39 g sodium molybdate dihydrate, 0.049 g cobalt(II) nitrate hexahydrate and water (remaining amount), and is obtainable by diluting solute solution to 1 liter, the optimizing culture medium has an initial pH of 8, and after inoculating, the culture medium is allowed to grow until the initial concentration reaches to 0.16 optical density at 690 nm; and(2) use of Scenedesmus optimizing culture medium, comprising culturing Scenedesmus (CHX1) to obtain seed culture liquid by using Scenedesmus optimizing culture medium.
NOVELTY - A green sheet is produced by tape-casting raw material powder comprising diffusion prevention layer, fuel anode layer, and solid electrolyte layer, and laminated and adhered on one surface of metal support using warm isostatic press process, to obtain metal-supported solid oxide fuel cell. The metal-supported solid oxide fuel cell further has air electrode layer.    USE - Production of metal-supported solid oxide fuel cell (claimed).    ADVANTAGE - The metal-supported solid oxide fuel cell having improved strength and flexibility is produced with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell stack or fuel cell generation system.
NOVELTY - This utility model claims a sealed excrement and organic garbage is oxygen supplying system for garbage fermentation tank, a riding wheel mechanism to rotate with the tank body of the rotary vane, stirring the material to the outlet direction, inclining to the inlet direction, pushing the material and under the action of the gravity, collapsing back, air ventilation system, oxygen supplying system for garbage fermentation, rigid added material, if environment temperature cycling air heating system, when the material fermentation by producing heat, the air processed by ozone purifying train is discharged into the atmosphere, the production efficiency is high, and it can control the fermentation temperature and oxygen content, uniform fermentation effect is good, which ensures the quality of the product and large-scale production, which completely solves environmental pollution problem. Northern area also capable of one year continuous production.
NOVELTY - This utility model claims a biomass gasification furnace irregular material feeding device, a top cover with a feeding port at the top of the storage hopper (2), (1), a storage hopper (2) is connected with the lower end of the sliding plate (4) passes through the gasification furnace wall (8) extends into the biomass fuel gas of gasifying furnace inner container interlayer is equipped with wedge-shaped plug board guide box (7), a wedge-shaped plate guiding box (7) lower side of the wedge plate groove at one side of the furnace wall is connected with the gasification furnace (8) of the storage hopper (2) (3) is installed on the side face of the storage hopper (2), a wedge-shaped plate (5) is inserted in the wedge plate groove (3) is connected with a handle (6) on the upper end is fixed on the surface of the wedge-shaped inserting plate (5). The feeding hopper of good leak tightness, convenient and simple operation and solves the problem that the long term a gasification furnace with the development of the problem, and has popularization and application value.
NOVELTY - This utility model claims a biomass gasification gas purification processing device of biomass gasification furnace, the biomass gasification gas wire material, biomass gasified fuel gas cap water washing, the first and the second biomass gasified fuel gas tar purifying absorber, biomass gasified fuel gas condenser, a blower (group), biomass gasified fuel gas storage bag (device), the third biomass gasified fuel gas tar purifying absorber and combustion gas generator (groups) are arranged in order, the first, second, third, fourth, fifth, sixth, seventh, eighth and ninth conveying pipe is connected with the gasification furnace, an absorber, a condenser, a blower and a gas storage bag and motor (group) to make the electric generator (set) by the gasification gas purification treatment, a motor (group) to provide clean energy, environmental protection and economic benefit is obvious, has practicability and popularization value.
NOVELTY - A granary grain oil insecticidal composition comprises 10-35 wt.% sophora flavescens, 10-50 wt.% chinaberry, 5-35 wt.% radix stemonae, 25-30 wt.% extracting solvent, 5-20 wt.% starch, 3-20 wt.% euphorbia fischeriana root, and 10-50 wt.% wintergreen.    USE - Granary grain oil insecticidal composition used for killing Tribolium castaneum, lesser grain borer and maize weevil; and preventing and killing Bruchus rufimanus, Gelechiidae, Ephestia cautella or Indian meal moth and weevil in coffee beans, green beans and broad beans (all claimed).    ADVANTAGE - The composition is simple to prepare, has insecticidal rate of up to 80-85% and long validity period, and delays development of drug resistance. Preparation method is environmentally friendly and has no waste.
NOVELTY - The method involves passing mixture of raw material oil and hydrogen gas by high and low temperature operation reactor. The hydrogen-rich gas separated from stream generated from hydrogenation is recycled. The sub-hydrogen gas separated from stream generated from hydrocracking is recycled. The separated liquid product is subjected to fractionation to obtain various low aromatic hydrocarbon solvent oil products. The active components of hydrogenation catalysts are used at two stages under reaction states. The sulfur containing light oil product is included for hydrogenation process.    USE - Two-stage hydrogenation method for producing high-quality low freezing point motor fuel from biological oil e.g. vegetable oil such as soybean oil, peanut oil, castor oil, rapeseed oil, corn oil, olive oil, palm oil, coconut oil, tung oil, linseed oil, sesame oil, cotton seed oil, sunflower seed oil and rice bran oil and animal oil (all claimed) such as butter, lard, mutton fat and fish oil.    ADVANTAGE - The activity stability of the catalyst can be ensured. The stable and long period hydrogenation operation can be ensured effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the production of high-quality low freezing point motor fuel from biological oil. (Drawing includes non-English language text)
NOVELTY - A motor fuel producing method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing hydrogenation reactors, where the mixture passes through a low temperature operation reactor and a high temperature operation reactor followed by recycling hydrogen-rich gas at first stage, supplying liquid into a second stage hydrogenation modification reaction zone, recycling the sub-hydrogen gas at second stage, and subjecting the liquid product to fractionation to obtain naphtha and low freezing point diesel oil.    USE - Method for producing motor fuel.    ADVANTAGE - The method enables producing the motor fuel with high quality and low freezing point.    DETAILED DESCRIPTION - A motor fuel producing method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing greater than or equal to 2 hydrogenation reactors, where the mixture passes through a low temperature operation reactor and a high temperature operation reactor followed by recycling hydrogen-rich gas at first stage, supplying liquid into a second stage hydrogenation modification reaction zone, recycling the sub-hydrogen gas after hydrogenation modification at second stage, and subjecting the liquid product to fractionation to obtain naphtha and low freezing point diesel oil.
NOVELTY - The method involves adopting biological oil as raw material oil. The stream generated from hydrogenation is separated to obtain hydrogen-rich gas. The sub-hydrogen gas is separated from the oil generated through second stage hydrogenation recycled at the second stage circulation. The hydrogenation activity components of the hydrogenation catalyst are used at the stage in which materials are selected from sulfurization state. The catalysts are tungsten, molybdenum, nickel and chromium used at the second stage in which materials selected from reduction state.    USE - Two-stage hydrogenation method for producing low freezing point motor fuel.    ADVANTAGE - The motor fuel can be produced low freezing point, activity stability of the catalyst can be ensured, and operation of the device can be ensured.    DETAILED DESCRIPTION - The separated liquid product is subjected to fractionation to obtain naphtha and low freezing point diesel oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of two-stage hydrogenation process. (Drawing includes non-English language text)
NOVELTY - A motor fuel producing method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing greater than or equal to 2 hydrogenation reactors, where the mixture passes through a low temperature operation reactor and a high temperature operation reactor, recycling hydrogen-rich gas at the first stage, supplying the liquid into a second stage hydrogenation modification reaction zone, recycling the sub-hydrogen gas at the second stage, and subjecting the liquid product into fractionation to obtain naphtha and low freezing point diesel oil.    USE - Method for producing motor fuel.    ADVANTAGE - The method enables producing motor fuel having low freezing point.    DETAILED DESCRIPTION - A motor fuel producing method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing greater than or equal to 2 hydrogenation reactors, where the mixture passes through a low temperature operation reactor and a high temperature operation reactor, recycling hydrogen-rich gas at the first stage, supplying the liquid into a second stage hydrogenation modification reaction zone, recycling the sub-hydrogen gas at the second stage, and subjecting the liquid product into fractionation to obtain naphtha and a low freezing point diesel oil, where the active components of the hydrogenation catalyst at the first stage and second stage are selected from sulfurization state tungsten, molybdenum, nickel and cobalt.
NOVELTY - Potassium bicarbonate and silicon dioxide are added to melting furnace, melted under sealed environment and temperature of the furnace is controlled to 1200-1500 degrees C. The obtained melted material is mixed with deionized water, dissolved and the solution modulus is adjusted to 2.3-2.5. The obtained dissolved solution is filtered, to obtain liquid silicon-potassium fertilizer. The molar ratio of potassium bicarbonate and silicon dioxide is 2:1-3:1.    USE - Manufacture of liquid silicon-potassium fertilizer (claimed).    ADVANTAGE - The method effectively provides liquid silicon-potassium fertilizer by environmentally-friendly process, in a short period of time.
NOVELTY - A low-condensation point motor fuel production method involves selecting biolipid as raw oil, passing the raw oil and hydrogen pass through a first-stage hydrogenation reaction zone under hydrogenation operation conditions, where the first-stage hydrogenation reaction zone comprises greater than or equal to 2 two hydrogenation reactors, and the raw oil and hydrogen pass through one reactor operated at low temperature and pass through the other reactor operated at high temperature followed by separating the material flow generated in hydrogenation stage.    USE - Method for producing low-condensation point motor fuel.    ADVANTAGE - The method enables producing low-condensation point motor fuel with high stability.    DETAILED DESCRIPTION - A low-condensation point motor fuel production method involves selecting biolipid as raw oil, passing the raw oil and hydrogen pass through a first-stage hydrogenation reaction zone under hydrogenation operation conditions, where the first-stage hydrogenation reaction zone comprises greater than or equal to 2 two hydrogenation reactors, and the raw oil and hydrogen pass through one reactor operated at low temperature and pass through the other reactor operated at high temperature followed by separating the material flow generated in hydrogenation stage, recycling obtained hydrogen-rich gas, supplying obtained liquid into a second-stage hydro-upgrading reaction zone, separating material flow generated in hydro-upgrading stage, recycling hydrogen, and fractionating to obtain naphtha and low-condensation point diesel oil, where an active component of a hydrogenation catalyst used in a first stage and a second stage is selected from tungsten, molybdenum, nickel and cobalt.
NOVELTY - The method involves mixing raw material oil and hydrogen with bio-oil by first hydrogenation reaction zone which is provided with hydrogenation catalyst beds in which content of hydrogenation active component increases. The hydrogenation generation stream is separated while obtained hydrogen-rich gas is recycled. The obtained liquid product is subjected to fractionation to obtain naphtha and low-condensation point diesel oil. The active component of hydrogenation catalyst is tungsten, molybdenum, nickel and cobalt in reaction state.    USE - Hydrogenation modification method of producing low solidifying point motor fuel using bio-oil.    ADVANTAGE - The low-condensation point motor fuel can be produced while guaranteeing activity stability of the catalysts and long-period stable operation of the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the hydrogenation modification process of producing low solidifying point motor fuel using bio-oil. (Drawing includes non-English language text)
NOVELTY - Providing a current of the titanium anode plate, comprising a titanium base material, the titanium base material is coated on the surface P salt and an iridium oxide coating. The utility model improves the anti-reducing capability of the anode, it is suitable for the electrolyte to a chlorine ion concentration, a reverse electrode in the electrolysis process, capable of preparing hydrogen, oxygen evolution potential of iridium tantalum, ruthenium can be replaced anode, the electrolysis water industry, Ru8 + is virulent, and platinum-coated anode because of cost is high, it is not capable to realize industrialization, and platinum with anti-cancer effect, is provided with good catalytic activity, and shows excellent performance in removing scale in the process of using the reverse current.
NOVELTY - The utility model relates to a biomass gasification field, specifically, referring to a multifunctional biomass gasification furnace. A gasification reaction system, a filtering system and an oxygen supply system, wherein the gasification reaction system comprises a reaction barrel, comprising a filter sealing the top cover of reaction tank top part and is set on the wind cavity at the lower part of the reaction barrel, the wind head through a reaction barrel connected with the inner cavity, the filter system is provided with a first air outlet pipe on the cleaning pipe of the filter top and an air outlet pipe and a sealing tube and a filter is set on the filter, and the oxygen supply system comprises a fan box and a fan in the fan box, the fan pipe is connected with the oxygen supply tube, the oxygen supply tube and connected with wind by the fan; the middle part of the reaction barrel, the upper part is provided with the second air outlet pipe, which are respectively connected with the air inlet of the filter; This utility model can make biomass raw material of carbon into the combustible gas, so as to effectively improve the utilization rate of the biomass, and it is safe, environment-friendly and energy-saving.
NOVELTY - This utility model claims a biomass gasification fuel gas tar purifying absorber, and the top end of the absorber with a cover plate main body side wall and the side wall is set with an air inlet pipe and an air outlet pipe are connected with the inner cavity of the suction body exhort the absorber main body is an air inlet pipe, an air outlet pipe from bottom to top and is in turn provided with a bottom bracket, a middle bracket, a middle bracket and upper bracket, upper-layer non-woven cloth, a layer of non-woven fabric, wherein a layer of non-woven fabric and the bottom layer non-woven fabrics are respectively arranged on the bracket, a bracket, a middle bracket and a bottom bracket, a waste water barrel of the waste water pipe from the adsorber main body is connected with the bottom of the absorber main body inner cavity. This kind of tar purifying absorber can make the biomass gasification tar in the fuel gas for the effective separation, but also to remove the moisture and dust in the gasification gas, but a gas generator or civil provide clean biomass gasification fuel gas and has practical value.
NOVELTY - Celecoxib is prepared by mixing 4,4,4-trifluoro-1-(4-methylphenyl)-1,3-butanedione and sulfonamide phenylhydrazine or 4-sulfonamide phenylhydrazine hydrochloride with organic solvent and performing cyclization reaction in which organic solvent is low-molecular-weight organic acid or low-molecular-weight organic acid aqueous solution.    USE - Preparation of celecoxib (claimed).    ADVANTAGE - Preparation of celecoxib is simple and low cost, has high product yield, high product purity, and convenient post-treatment, and uses non-toxic solvent, and refining and condensing processes are easy and environment-friendly.
NOVELTY - The furnace has a circulating fluidized bed provided with a turbulent fluidized bed and a reactor bed. A bottom turbulent fluidized bed is provided with a gas distributor and a discharging pipe. The discharging pipe is equipped with a biomass feeding opening at a bottom part of the reactor bed. A top part is provided with two grade gas-solid separators. One of the two grade gas-solid separators is provided with a circulation return pipe that is filled with coarse particles. Small diameter of a straight pipe is formed by a head pipe piece.    USE - Biomass gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace.
NOVELTY - Sweet wormwood extract is prepared by performing extraction using supercritical carbon dioxide (CO2) in which entrainer is peppermint oil.    USE - Preparation of sweet wormwood extract for insect repellent daily products e.g. bath gel, lotion, hand sanitizer, soap, perfume, or mosquito repellent (all claimed).    ADVANTAGE - Sweet wormwood extract mosquito repelling effect is good and long lasting, sweet wormwood extract has low viscosity, is safe and non-toxic, does not block device pipeline, and extracting efficiency is high.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) composition containing sweet wormwood extract and pharmaceutically or physiologically acceptable carrier or auxiliary material; and    (2) insect repellent.
NOVELTY - The tank has a fermentation tank main portion (1) which comprises an inner plate and an outer plate. A sealed hollow area is formed between the inner plate and the outer plate. A heat conducting oil is filled in the sealed hollow area. An electric heating device is provided with several electric heating rods arranged in the closed hollow region, and is used for heating the heat-conducting oil. A thermocouple is arranged in the temperature control device, for performing real-time temperature detection on the heat-conducting oil.    USE - Electric heating/drying/stirring fermentation tank for processing kitchen waste such as crushing fruit and crushing vegetable rice.    ADVANTAGE - The fermentation process and the drying process are integrated, so that the processing speed and the processing efficiency of kitchen waste are conveniently improved. The temperature of material in the fermentation tank main portion can be increased evenly and quickly, by the heating of the heat-conducting oil. The internal temperature of the fermentation tank main portion can be conveniently controlled to constant temperature. The electrical energy can be saved during the fermentation process, and the fermentation effect can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electric heating/drying/stirring fermentation tank.    Fermentation tank main portion (1)    Rotating shaft (201)    Drive gear (202)    Stirrer (203)
NOVELTY - Anaerobic composting of small-scale food waste comprises crushing food waste, dehydrating; taking into fermentation tank, adding anaerobic fermentation inoculum, stirring and mixing uniformly, controlling temperature and pH, fermenting for 24-72 hours; discharging into dryer; and drying to obtain fertilizer.    USE - Method for anaerobic composting of small-scale food waste used for preparing fertilizer (claimed).    ADVANTAGE - The method has short degradation and processing time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the components of fermentation tank.
NOVELTY - An organic fertilizer comprises 15-25 wt.% pig manure, 25-35 wt.% chicken manure and 45-55 wt.% cleaning sludge.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has easy to obtain raw materials, low cost and high organic matter content of 60-70%; improves soil fertility and protects environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising taking pig manure, chicken manure and cleaning sludge, putting in processing field, spreading raw materials, controlling water content to 55 plus minus 5%, fermenting, putting in rolling machine for 24-72 hours, stacking for 4-8 days, maintaining temperature, fermenting for 12-20 days, stacking to form semi-finished product, turning over, granulating, vibration sieving, controlling water content of 5-25%, packing and sealing.
NOVELTY - A plant sludge and eryngii mushroom residue organic fertilizer formulation comprises 45 plus minus 5 wt.% pharmaceutical or food factory sludge, 22 plus minus 5 wt.% chicken manure, 30 plus minus 5 wt.% cultivated eryngii mushroom residue and 3 plus minus 1 wt.% plant ash.    USE - Plant sludge and eryngii mushroom residue organic fertilizer formulation.    ADVANTAGE - The fertilizer formulation has high organic matter content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of plant sludge and eryngii mushroom residue organic fertilizer formulation comprising taking all raw materials, mixing uniformly, fermenting with mixed thermophilic aerobic bacteria for 16-23 hours, heating at 55-65 degrees C, turning over for 18-20 days, controlling moisture content of 42-46%, carrying out secondary fermentation at 42-46 degrees C for 28-35 days, turning over for 4-5 times, drying, mechanical grinding and bagging.
NOVELTY - This utility model claims a kind of capable of moving the processing device of road plant waste, comprising a generator, a centrifugal fan, a ventilating pipeline and a stack, the generator is connected with the centrifugal fan, wherein the centrifugal fan is connected with the ventilation pipe, wherein the ventilation pipe is paved on the stack, the stack through input end of the temperature control system is connected with the centrifugal fan. This utility model is featured with simple structure, low cost and convenient installation and repeated use, a generator and a centrifugal fan capable of being detached and moved in a plurality of points at the same time on the road, the use temperature control system in real time when a temperature of a reactor body to the single chip so as to control the conveying wind of a centrifugal fan, a control.
NOVELTY - This utility model claims a kind of penicillin production is waste gas processing device, comprising a waste gas discharge pipeline and soda lime water pool, the waste gas discharge pipeline connected with one end of a soda lime pool, the other end production plant and penicillin to air conditioner system air outlet. This utility model claims a waste gas processing device, it can effectively avoid the penicillin production process waste gas, dust is harm to human body and environment, and has good application prospect.
NOVELTY - A composite semiconductor photocatalyst comprises titanium dioxide-cadmium telluride, titanium dioxide-cadmium selenide, or titanium dioxide-cadmium sulfide compounds which contain cobalt, nickel, and/or iron.    USE - A composite semiconductor photocatalyst (claimed).    ADVANTAGE - Preparation of highly efficient composite semiconductor catalyst is fast, simple, stable, and low cost and does not require template or initiator.    DETAILED DESCRIPTION - A composite semiconductor photocatalyst comprises titanium dioxide-cadmium telluride (TiO2-CdAxTe), titanium dioxide-cadmium selenide (TiO2-CdAxSe), or titanium dioxide-cadmium sulfide (TiO2-CdAxS) compounds.    A=Co, Ni, and/or Fe; and    x=0.02-1%.    INDEPENDENT CLAIMS are included for:    (1) catalyst preparation method which involves using TiO2 as carrier surface of quantum dots, adsorbing mercaptopropionic acid on surface of quantum dots, adding biomass derivatives, and assembling cobalt, nickel, or iron salts or complexes on optical surface of photocatalyst; and    (2) semiconductor-type photocatalytic system comprising CdTe quantum dot, CdSe quantum dot, or CdS quantum dot, TiO2, cobalt salt, cobalt complex, nickel salt, nickel complex, iron salt, iron complex solution, and aqueous solution of biomass derivatives under alkaline condition and UV and/or visible light irradiation condition in which biomass derivative is triethanolamine, triethylamine, methanol, ethanol, propanol, butanol, ethylene glycol, glycerol, glucose, sucrose, fructose, maltose, or mannose.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the X-ray diffraction pattern of titanium dioxide quantum dot, titanium dioxide and cadmium sulfide quantum dot before adding cobalt(II) chloride hexahydrate, and titanium dioxide and cadmium sulfide after adding cobalt(II) chloride hexahydrate.
NOVELTY - The device has a heat carrier outlet (3), heat carrier pipe (4), stirrer (5), heat preservation layer (6), heat carrier inlet (7), disc (9), air outlet (10) and lower opening. The inner wall of the furnace is provided with a heat carrier inlet and a heat carrier outlet. The heat carrier guide tube and external heat supply device is composed of heat exchange circulation, so that the heat is uniformly distributed on the inner wall of the furnace.    USE - Domestic rubbish decomposing device.    ADVANTAGE - Since the domestic rubbish is completely converted into carbon and combustible gas, the energy utilization rate is high. The required components for the decomposing device are minimized, so that the device investment is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of domestic rubbish decomposing device.    Heat carrier outlet (3)    Heat carrier pipe (4)    Stirrer (5)    Heat preservation layer (6)    Heat carrier inlet (7)    Disc (9)    Air outlet (10)
NOVELTY - Processing kitchen food waste comprises putting food waste in container, stirring, putting in reflux heating device, introducing steam, stirring and heating.    USE - Method for processing kitchen food waste (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste treatment device.
NOVELTY - Organic fertilizer quick fermentation device comprises vertically open fermentation tank (1), rotary motor (2) and bracket (8). The tank body is set with supporting column (14) and snake-shaped heating pipe (7) connected to heat conducting oil heater (15). The rotary motor is connected to cross stirring frame (4) via support frame (3). The insulating layer is provided with aeration pipe (9) equipped with oxygen nozzle (10). The aeration pipe is connected to blower (17).    USE - An organic fertilizer quick fermentation device.    ADVANTAGE - The device has small floor area requirement, short heating time and high degree of mechanization. The device does not pollute the environment.    DETAILED DESCRIPTION - Organic fertilizer quick fermentation device comprises vertically open fermentation tank (1), rotary motor (2) and bracket (8). The vertically open fermentation tank comprises tank body with insulating layer and tank bottom. The tank body is set with supporting column (14) and snake-shaped heating pipe (7) connected to heat conducting oil heater (15). The rotary motor is connected to cross stirring frame (4) via support frame (3). The cross stirring frame through rotary supporting roller (5) is fixed on bracket. The cross stirring frame is provided with stirring rod (6). The insulating layer is provided with aeration pipe (9) equipped with oxygen nozzle (10). The aeration pipe is connected to blower (17).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic fertilizer quick fermentation device.    Fermentation tank (1)    Rotary motor (2)    Support frame (3)    Cross stirring frame (4)    Snake-shaped heating pipe (7)    Bracket (8)    Aeration pipe (9)    Oxygen nozzle (10)    Supporting column (14)    Oil heater (15)    Blower (17)
NOVELTY - A composite fertilizer comprises 38-56 wt.% organic matter, 10-15 wt.% composite amino acid, 10-15 wt.% chelating agent, 2-4 wt.% trace element, and 20-30 wt.% nitrogen-phosphorus-potassium.    USE - Composite fertilizer used for agricultural crops.    ADVANTAGE - The fertilizer improves soil rationalizing property, promotes soil aggregate formation, improves soil water retention, increases agricultural product yield, and improves quality and taste of agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by dissolving composite amino acid to water to prepare 20-30% solution, adding chelating agent, borax, zinc sulfate, magnesium sulfate, ammonium sulfate, and ferrous sulfate, stirring to completely dissolve, continuously stirring for 20 minutes, sufficiently stirring, spray drying, pulverizing, and sieving through 80 meshes sieve to obtain mixed material; and crushing nitrogen-phosphorus-potassium, sieving with 80 mesh sieve, adding organic matter, stirring, and uniformly mixing with obtained mixed materials.
NOVELTY - The utility model claims a kind of using sludge drying waste heat feeding mud to digestion process for pre-heating device, a sewage treatment plant comprises a sludge drying system and the sludge digestion system, wherein the device comprises a sludge drying system for heat waste water collecting lifting device; the sludge digesting system connected with the heat exchange device, a collecting lifting device and heat exchange device is set with hot waste water underground hot waste water conveying pipe. This utility model combined with our country the key component, generating modified outside " town sewage treatment plant sludge treatment technique guide (anaerobic digestion, dehydration, drying trial (March, 2011), land use of typical operation, fully using sludge drying waste heat, a sludge drying the condensed water generated by the heat waste water and middle temperature anaerobic digestion process of the mud by indirect heat exchange, improving acid production of sludge digestion process temperature, feeding the sludge digestion process required to heat the marsh gas production, drying fully using sludge anaerobic digestion to generate methane gas flow for providing sludge;
NOVELTY - This utility model claims a waste water filter residue processing device, comprising a stable blending device, dehydrating and drying equipment and alkaline water circulating system, and it can process the waste water generated by the semi-liquid and solid for taste. The device can disinfect waste water processing device and a toilet sewage treatment device using a hospital, so as to effectively the waste water processing device is dirt and filtrate to gain a treatment, removing a harmful material to environment recontamination, protecting public environment and public health, the waste; The device has simple structure, reasonable technique, good decontamination effect and low cost. The device is especially suitable for large-scale reservoir water area treating domestic sewage engineering, secondary water pollution to avoid filter residue landfill;
NOVELTY - The utility model claims a kind of human excrement into production device for fertilizer metering device, a transmission half-dry excrement conveyer belt of the bottom transmission belt is provided with a steam pipe, the upper transmission belt is provided with a shell and a condensing plate is multiple number of shell, wherein the shell is provided with a connecting channel. The utility model technical solution, it can save resource and reduce pollution, it has good economic benefit and social benefit.
NOVELTY - This utility model claims a kind of capable of separating liquid gas straw dry distiller to a state, comprising a furnace body, an air chamber, a separating device, a gas purifier, a liquid collecting device, a fuel gas collecting device, a temperature sensor and a controller, the furnace body through the air chamber is connected with the separation device, separating device by a pipeline is respectively connected with the gas and liquid collecting device, the separating device is provided with a fuel gas outlet valve, and the other one is provided with a liquid outlet valve, gas purifier connected with gas collecting device by a pipeline, the temperature sensor is installed in the air outlet chamber, and sending the detected temperature value to the controller, the controller receives the temperature sensor by the comparator compares the temperature value with the preset value, judging whether the opening/closing gas valve/liquid valve. By the control device for straw carbonization, separating the gaseous and liquid material, the chamber gas long pipeline, the solid substance-separating due to gravity and liquid gaseous material recycling effect is good.
NOVELTY - This utility model claims a wood drying technology field, especially relates to a kind of drying and charring wood integrated device, wherein, comprising a kiln body and a control device, wherein the kiln body is provided with a fan, a heater, a pipe for spraying atomized water, and used for generating saturated steam water tank, the kiln body is provided with humidity-discharging window, a fan motor is connected with a variable frequency device electrically connected with the variable frequency device is connected with the integrated control device are electrically connected. The difficulty of the utility model is a drying and carbonization to concentrate on a kiln body, which overcomes the drying and charring integrated technology, the wood is kiln cooling and drying is carried out, reduces the energy consumption, the energy saving and emission reduction effect.
NOVELTY - This utility model claims a kind of use municipal sludge supercritical method for pyrolyzing a biological oil processing system, the structure is as follows: the front end of the reaction kettle (4) through the connecting pipe is orderly provided with a nitrogen storage tank (1), booster pump (2) and the high pressure gas storage tank (3), the top end of the reaction kettle (4) is provided with a sampling port (14), a sampling port (14) of the back end is connected with a cooling pipe (6) and the condenser (7), reaction kettle (4) is further provided with a kettle body rotating discharge hole (15), rotating discharge hole (15) is connected with the filter (10), liquid distributor (12) and a rotary evaporator (13). Using the utility model avoids the oil preparing technique of sludge drying and dehydrating process, it breaks through the large amount of catalyst, at the same time, it avoids the secondary pollution of heavy metal to obtain the bio-oil with higher added value.
NOVELTY - A biomass gas tar removing method involves feeding high-temperature biomass gas containing tar generated by a biomass gasifier to a spray cooling unit, spraying and cooling by heavy tar liquid to obtain primarily purified biomass gas, feeding the primarily purified biomass gas to a coarse capture unit, removing polycyclic aromatic hydrocarbon tar by capillary condensation and interception performance of a coarse material, feeding the processed two-stage purified biomass gas to an adsorption, and removing light tar to obtain clean gas by the adsorption effect of an adsorbent or an absorbent.    USE - Method for removing biomass gas tar.    ADVANTAGE - The method enables removing biomass gas tar in an inexpensive manner.    DETAILED DESCRIPTION - A biomass gas tar removing method involves feeding high-temperature biomass gas containing tar generated by a biomass gasifier to a spray cooling unit, spraying and cooling by heavy tar liquid to obtain primarily purified biomass gas, feeding the primarily purified biomass gas to a coarse capture unit, removing polycyclic aromatic hydrocarbon tar by capillary condensation and interception performance of a coarse material, feeding the processed two-stage purified biomass gas to an adsorption or absorption unit, removing light tar to obtain clean gas by the adsorption effect of an adsorbent or an absorbent and reducing the dew point of the biomass gas tar to -30 to 0 degrees C.
NOVELTY - Sisal residue is crushed, filtered, centrifuged, to obtain transparent liquor. The resultant liquid is fermented and centrifuged, to obtain sisal paste. The sisal paste and concentrated sulfuric acid are added to reactor, heated, acidolysis is carried out, dried, neutralized, heated, dried under vacuum and crushed, to obtain tigogenin crude powder. The crude saponin is extracted using hot ethanol, in tigogenin. The resultant product is filtered, concentrated, boiled under vacuum, centrifuged, saponin crystals are collected, heated and dried, to obtain tigogenin.    USE - Extraction of tigogenin from sisal residue (claimed).    ADVANTAGE - The method provides tigogenin having high quality and purity, by simple and environmentally-friendly process with less energy consumption and high recovery rate.    DETAILED DESCRIPTION - Sisal residue is crushed to, obtain sisal juice. The sisal juice is filtered, to obtain coarse residue filter liquor. The obtained liquid is centrifuged, to obtain transparent liquor. The resultant liquid is fermented at room temperature, to obtain sisalagenin fermentation liquor. The obtained liquor is centrifuged, to obtain sisal paste. The sisal paste and concentrated sulfuric acid are added to reactor, heated, acidolysis is carried out, dried, neutralized using calcium hydroxide solution, heated, dried under vacuum and crushed, to obtain tigogenin crude powder. The crude saponin is extracted using hot ethanol, from obtained tigogenin. The resultant product is filtered, concentrated, boiled under vacuum, centrifuged, saponin crystals are collected, heated and dried, to obtain tigogenin.
NOVELTY - Using ammonia-containing off-gas of electronic industry for preparing reproducible high pure ammonia, comprising a filter, an ammonia decomposition device, a first purifier, a booster pump, a purifier and a high pure ammonia synthesis device, the nitride reactor through a pipeline with the filter, the filter is connected through a second pipeline with the ammonia decomposing device, the ammonia decomposition device through the third pipeline and a purifier connected with the first purifier through the pipeline and the booster pump is connected with the booster pump through a fifth pipeline and a purifier and the second purifier through the sixth pipeline and the high-purity ammonia synthesis device. This utility model is green and environment-friendly, energy-saving effect is obvious, safe production process, reduces the production cost and the product quality is stable.
NOVELTY - The utility model claims a kind of filtering and sterilizing the biogas, comprising a cylinder body, the cylinder body is provided with a biogas pipe, output pipe and the liquid output pipe, wherein the cylinder body is divided into an upper chamber and a lower chamber, the liquid passage is provided with the concentric inner chamber, the upper part of the cylinder body is provided with the centre of the top of the inner cylinder, wherein the inner cylinder is provided with the concentric stainless steel filter screen, a stainless steel filter screen and the top of the liquid channel is connected against the bottom of the cylinder bottom, the lower part is provided with an ozone input pipe and an ozone conveying pipe in the lower chamber by the division ring is provided with a motor, an output shaft of the electric motor is supported on the cylinder axis by a bearing of the top and the bottom, the output shaft is located in the stainless steel filter screen is provided with a outer edge winding the spiral blade, the liquid channel and the clear liquid cylinder is provided with a spiral channel, wherein the biogas slurry into a stainless steel filter screen at the bottom of the lower part of the cylinder body, the liquid output pipe enters the upper part of the liquid passage from the top of the cylinder body, the output pipe is located at the upper part of the cylinder body.
NOVELTY - This utility model aims to provide one kind of intelligent aerobic ferment compost optimizing system, comprising a fermentation tank, fermentation material, and, ePTFE composite film, a monitoring point, a monitoring device, a control centre, a bottom aeration fan groove bottom aeration pipe. The utility model uses the groove type composting engineering with dynamic and static compost, it can realize multiple layer structure, intelligent control, capable of realizing full-automatic unmanned operation can realize totally-enclosed operation, reduces the corrosion of the workshop. The fermentation material in the fermentation tank, passes through is provided with real time monitoring and analyzing new waterproof antenna with enlarging function for oxygen temperature monitoring device, a multi-sample monitoring oxygen concentration and stack temperature of the fermentation stack, sending oxygen temperature data by a monitor in real time to the data analysis control centre for processing, control aeration fan aeration frequency and aeration through stack temperature and oxygen concentration data analysis control centre, when the temperature exceeds a monitoring device to ferment, the turner for turning, so as to realize intelligent turning pressing. Turner adopts roller type turning. Turning at the same time as the material the component film.
NOVELTY - The utility model claims a biomass gasification furnace, comprising an ash outlet opening of the secondary furnace, a secondary furnace ash, furnace cracking cavity, an air flow cover, a filter screen, an air outlet pipe, a heat exchanger, a vent-pipe, uniformly distributed guide cover, a feeding hopper, a flashboard, a main combustion chamber, fire grate, furnace ash outlet, the main furnace ash, the main furnace, air connecting pipe, the auxiliary furnace. The main furnace is provided with a main furnace chamber and the main furnace ash, furnace top of the main combustion chamber is set with thickened hopper, a feeding hopper is set with uniformly distributed guide cover and an inserting plate, the upper part is provided with the secondary furnace cracking furnace cavity and the auxiliary furnace ash cavity, the middle part of the cracking cavity is equipped with an air flow cover and a filter screen, the upper part of the cracking cavity is equipped with heat exchanger, and is provided with air outlet pipe, a ventilating pipe are respectively connected with the air flow cover in the main combustion chamber and the secondary furnace cracking cavity, the two end of the vent of the connection pipe are connected with the lower part of the cracking chamber and the main combustion chamber. The product has rational design precision, is provided with gas, separating and purifying function, speed, gas flow, gas high purity, no impurity, gasification combustion for a long time, is energy-saving and environment-friendly, long service life, and it is widely suitable for family and factory, and heat exchanger using the waste heat utilization, high comprehensive utilization rate.
NOVELTY - This utility model claims a domestic garbage coupled fluidized bed through hierarchical pyrolysis gasification furnace, a crusher, removing sleeve type roller dryer, coupled fluidized bed, a gas distributor, air inlet pipe, a feeding port, a gas-solid separator, rough ash circulation returning pipe, a returning device, a gas-solid separator, the fine ash circulation returning pipe, the air flow bed, a gas outlet coupled at the front end of the fluidized bed is provided with a removing grinder and a sleeve type roller dryer, the bottom coupling fluidized bed is provided with a gas distributor and a discharging pipe, is provided with an air bed from the bottom 1000-2000 mm, and the position of the air flow 500-3000 mm is provided with a feeding port, and the top is provided with the first grade gas-solid separator and the secondary gas-solid separator, the first grade gas-solid separator the crude particle ash circulation returning pipe connected with the material returning device and the coupling fluidized bed, a gas-solid separator of a fine particulate ash circulation returning pipe by returning the air bed.
NOVELTY - The method involves connecting a platinum electrode and a gold electrode with a pulse direct current power source to form a discharge loop. The two electrodes are immersed in carbon carrier dispersion relative to a holding position for a certain distance. High energy plasma is generated between the two electrodes according to the production control reaction time, after discharging a solution by centrifugal separation. The two electrodes are dried to obtain the loaded molybdenum alloy nano-cluster material.    USE - Method for manufacturing loaded type molybdenum alloy nano-cluster material used as electro-catalyst in fuel cell and lithium-air battery.    ADVANTAGE - By generating the high energy plasma between the two electrodes, the crystal property of the cluster material can be improved with particle size of 2 nm. The manufacturing process of the molybdenum alloy nano-cluster material can be simplified. The cluster material with high dispersibility can be obtained and can be controlled to realize mass production. The generation of impurities during manufacturing of molybdenum alloy nano-cluster material can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device used for manufacturing loaded type molybdenum alloy nano-cluster material. (Drawing includes non-English language text)
NOVELTY - Nutrient fertilizer comprises 60-70 pts. wt. tea seed cake powder, 30-40 pts. wt. fruit residue, 1-3 pts. wt. effective microorganisms (EM) bacteria, 2-3 pts. wt. brown sugar, 0.01-0.03 pt. wt. citric acid and 15-20 pts. wt. water.    USE - Nutrient fertilizer used for promoting crop growth, and reducing plant diseases and insect pest.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nutrient fertilizer comprising:    (A) preparing raw materials; mixing brown sugar and water, heating to 85-90 degrees C, adding citric acid, cooling to 25-30 degrees C, adding EM bacteria, activating for 1 hour to obtain fermentation liquid;    (B) mixing uniformly tea seed cake and fruit residue, adding mixture into fermentation liquor, stirring uniformly, sealing and fermenting; and    (C) during fermenting period, monitoring temperature change, when temperature reaches 55 degrees C, turning yeast, fermenting until brownish black and no smell.
NOVELTY - Processing animal carcasses comprises high temperature sterilizing animal carcass, setting temperature to 150-300 degrees C, pressure to 3-12 kg/cm2, sterilizing for 3-8 hours to kill pathogenic microorganism; crushing animal body tissue to less than 50 mm fine particles; placing in horizontal cylinder degradation reactor, adding auxiliary material and biodegradable agent, maintaining temperature at 55-80 degrees C and humidity at 40-60%, degrading for 120 hours, discharging product, and placing in stacking tank.    USE - Method for processing of animal carcasses used as soil fertilizer (claimed).
NOVELTY - Plant organic residues fast harmless processing and fertilizer by using processing device, comprising a pre-processing device, a heating device and an automatic fermentation device, a pre-processing device for crusher, automatic fermentation device comprises a shell, a spiral stirring mechanism, a transmission system, a ventilation system and a control part, the transmission part is an electric motor, arranged on one side of the shell, a spiral stirring mechanism is set in the shell, the lower part of the is connected with the speed reducer through a chain wheel and a chain, a rotating under the driving of the motor, the control part is set on the shell, a ventilation system is composed of a fan and a pipeline, is set under the machine body, heating device is set on the automatic fermenting device, the shell is connected to the automatic fermentation device through soft pipe; This utility model is simply structured, convenient to use and capable of quickly and effectively for processing vegetable, prevent the pollution environment, vegetable residues processing technique effect is better.
NOVELTY - This utility model claims a kind of multilayer reciprocating chain drying furnace, wherein the drying furnace comprises a furnace body, the furnace body below the baking device, the furnace body is provided with at least two conveying fertilizer particle of type chain, a chain are overlapped, and the last chain end and the front end of the chain; The utility model is provided with the laminated chain, the chain is a multilayer reciprocating operation, the large area single layer long distance drying furnace, a compact space can be smaller in the space heat focus even the effect, energy saving and reducing consumption. Production is obviously improved, and a net chain, it can avoid the damage to the particle to ensure the integrity and smooth surface, reduces the loss and improve the quality and yield of the product, which is good for storage and transportation of the product.
NOVELTY - Nutritional multivitamin organic fertilizer comprises 1-30 %mass activated carbon, 1-90 %mass organic carbon, 1-50 %mass processed animal waste, 1-90 %mass feather meal, 1-40 %mass monosodium glutamate residue, 1-30 %mass starch residue, 1-45 %mass sugar, 1-10 %mass kaolin and 1-30 %mass zeolite powder.    USE - As nutritional multivitamin organic fertilizer (claimed).    ADVANTAGE - The nutritional multivitamin organic fertilizer is natural, environmentally-friendly, easy to store, and decomposed and absorbed within short time, contains all nutrients and retains soil moisture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing above-mentioned fertilizer, which involves (a) crushing raw materials separately to 50-80 mesh size, and granulating activated carbon to 1-2 mm size, (b) adding zeolite powder to granulated activated carbon, mixing uniformly, and granulating mixture to 1.5-4 mm size, and (c) adding water to granulated mixture, drying, detecting, measuring, and packing the mixture.
NOVELTY - The system has a power station boiler (4) whose tail part is connected with an air pre-heater (5). Bottom part of a fluidized bed gasification furnace (1) is connected with a bed material. A biomass material is fixed into a biomass feeding hopper (6). A high temperature cyclone separator (2) is connected with a dust gas inlet of a biomass gas burner (3). The biomass gas burner is connected with the power station boiler. Temperature of the fluidized bed gasification furnace is 100-500 degrees Celsius.    USE - Coal-fired power station boiler biomass gasification mixing system.    ADVANTAGE - The system realizes biomass fuel gas filtering process and alkali metal removing process and improves efficient utilization rate of biomass fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a coal-fired power station boiler biomass gasification mixing system.'(Drawing includes non-English language text)'    Fluidized bed gasification furnace (1)    High temperature cyclone separator (2)    Biomass gas burner (3)    Power station boiler (4)    Air pre-heater (5)    Biomass feeding hopper (6)
NOVELTY - The system has a gas passage inlet that is connected with an output pipe of a gas-solid separating device (19) which is connected with a pyrolysis device (1). The solid separating device is connected to the outer surface of heat supply device. A control valve (23) is connected with a water storage buffer tank (12). The connecting pipeline of the condensed water passage inlet is provided with a control valve (24). A gas passage is connected with a standing separating device through a condensed liquid outlet.    USE - Agricultural waste resource pyrolysis gasification comprehensive conversion and utilization system.    ADVANTAGE - The acetic acid is used efficiently as the biological foliar fertilizer. The utilization rate of the pyrolysis gasification comprehensive conversion and utilization system is improved. The plant diseases and insect pests are prevented in short period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolysis gasification comprehensive conversion and utilization system.    Pyrolysis device (1)    Water storage buffer tank (12)    Gas-solid separating device (19)    Control valves (23,24)    Light outlet (134)
NOVELTY - The system has a conversion air supply device (2) and a multifunctional heat exchange device (3). A pyrolytic device (1) is provided with a gas channel and connected with fuel gas output pipe. A heat exchanger (28) is provided with lower portion of pyrolytic device. A condensed water passage inlet (8) is connected with a water storage buffer tank (12) through a control valve (23). The pyrolytic device is connected with carbon powder collecting device (30) through pneumatic conveying apparatus (29).    USE - Agricultural waste resource pyrolytic carbon gasification comprehensive conversion and utilization system.    ADVANTAGE - The biomass waste resource conversion rate is improved. The maintenance cost and manufacturing cost can be reduced so as improve the economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an agricultural waste resource pyrolytic carbon gasification comprehensive conversion and utilization method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the agricultural waste resource pyrolytic carbon gasification comprehensive conversion and utilization system.    Pyrolytic device (1)    Conversion air supply device (2)    Multifunctional heat exchange device (3)    Condensed water passage inlet (8)    Water storage buffer tank (12)    Control valve (23)    Heat exchanger (28)    Pneumatic conveying apparatus (29)    Carbon powder collecting device (30)
NOVELTY - The method involves microbial-drying (1) garbage derived fuel. The garbage derived fuel is crushed (2). The metal is recovered (12) from crushed garbage derived fuel by garbage magnetic separation process. The vibrating sieve is processed to separate grain of diameter between 75-300 mm to enter into garbage sorting belt. The drying/crushing processes are repeated to get fine garbage derived fuel. The calcium based alkaline matter with 5% solid chlorine agent is added for solid chlorine, so as to refuse derived fuel forming machine for forming prepared refuse derived fuel.    USE - Method for preparing high quality garbage derived fuel.    ADVANTAGE - The garbage derived fuel can be prepared with high heating value at lower cost and low pollution thermal refuse derived fuel. The stability and applicability of the garbage derived fuel preparing system can be improved. The resource can be reduced and can protect the environment from pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process for preparing high quality garbage derived fuel. (Drawing includes non-English language text)    Step to dry garbage derived fuel (1)    Step to crush garbage derived fuel (2)    Step to provide hot air drying process (6)    Step to shape garbage derived fuel (9)    Step to recover metal (12)
NOVELTY - Flora containing Tangshan Rhine silent coli (Rheinheimeratangshanensis) having accession number CGMCC No. 5972, projecting light aeruginosa (Pseudomonasfluorescens) having accession number CGMCC No. 5974, Wickerhamomyces anomalus having accession number CGMCC No. 5975, is new.    USE - As flora used for preparing textile fiber (claimed).    ADVANTAGE - The flora has low production cost and high economic benefit; save energy; and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a textile fiber involving mixing O-bacteria liquid to bacteria water solution according to weight ratio of bacteria liquid:Tangshan bacteria:Pseudomonas fluorescent:Wickerhamomyces anomalus of 1-2:1-2:2-3; and 2) treating the remaining raw material by cutting, and putting the raw material into soaking pool.
NOVELTY - Flora containing Bacillus having conservation number is CGMCC No. 5971, tangshan (Rheinheimera tangshanensis) having conservation number is CGMCC No. 5972, Acinetobacter lwoffii having conservation number is CGMCC No.5973, fluorescence (Pseudomonas fluorescens) having conservation number is CGMCC No. 5974, is new.    USE - As flora for preparing a textile fiber (claimed).    ADVANTAGE - The flora does not pollute the environment, waste liquid is directly converted into organic fertilizer, realize zero discharge and zero pollution. Biological treatment process to protect the fiber, compared with the traditional chemical method, low production cost and high economic benefit. Not only save energy and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a textile fiber involving configuring the O-bacteria liquid, configuring compound flora to composite bacteria water solution according to the following weight ratio of the bacteria liquid:: tangshan with Brewster's bacillus, Pseudomonas fluorescens is 2-3:1-2:1-2:1-2; and 2) treating the remaining raw material by cutting, and putting the raw material into soaking pool.
NOVELTY - A bacterial composition comprises: Bacillus having preservation number of CGMCC No.5971, Acinetobacter lwoffii having preservation number of CGMCC No.5973, Pseudomonas fluorescens having preservation number of CGMCC No.5974, and Wickerhamomyces anomalus having preservation number of CGMCC No.5975.    USE - In preparing cellulose additive ester film for optical use (claimed).    ADVANTAGE - The bacterial composition provides cellulose additive ester film using a method that convert waste liquid directly into organic fertilizer, does not pollute the environment, and save energy thus economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cellulose additive involving: providing bacterial liquid including Bacillus, Acinetobacter lwoffii, Pseudomonas fluorescens and Wickerhamomyces anomalus according to weight ratio of 2-3:1-2:1-2:2-3; cutting woody raw material or herbal ingredients in slices and soaking in pool for swelling; and preparing fiber involving: crushing and grinding the swell raw material, soaking the raw materials in the bacterial liquid, and sterilizing to obtain biodegradable raw material, grinding the biodegradable raw material to make fiber, and soaking the prepared fiber in warm water, followed by drying, grinding and sterilizing to obtain cellulose additive.
NOVELTY - A bacterial composition comprises: Bacillus having preservation number of CGMCC No.5971, Rheinheimera tangshanensis having preservation number of CGMCC No.5972, Acinetobacter lwoffii having preservation number of CGMCC No.5973, and Wickerhamomyces anomalus having preservation number of CGMCC No.5975.    USE - In preparing cellulose additive ester film for optical use (claimed).    ADVANTAGE - The bacterial composition provides cellulose additive ester film using a method that convert waste liquid directly into organic fertilizer, does not pollute the environment, and save energy thus economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cellulose additive involving: providing bacterial liquid including Bacillus, Rheinheimera tangshanensis, Acinetobacter lwoffii, and Wickerhamomyces anomalus according to weight ratio of 2-3:1-2:1-2:2-3; cutting woody raw material or herbal ingredients in slices and soaking in pool for swelling; and preparing fiber by: crushing and grinding the swell raw material, soaking the raw materials in the bacterial liquid, and sterilizing to obtain biodegradable raw material, grinding the biodegradable raw material to make fiber, and soaking the prepared fiber in warm water, followed by drying, grinding and sterilizing to obtain cellulose additive.
NOVELTY - Flora containing Acinetobacter iwoffii having preservation number CGMCC No. 5973, Pseudomonas fluorescens preservation number CGMCC No. 5974, Wickerhamomyces anomalus preservation number CGMCC No. 5975, is new.    USE - As flora used for preparing textile fiber (claimed).    ADVANTAGE - The flora has low production cost and high economic benefit; save energy; and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing textile fiber involving mixing O-bacteria liquid to bacteria water solution according to weight ratio of bacteria liquid:Tangshan bacteria:Pseudomonas fluorescens:Wickerhamomyces anomalus of 1-2:1-2:2-3; and 2) treating the remaining raw material by cutting, and putting the raw material into soaking pool.
NOVELTY - A composite flora comprises Bacillus (Bacillus species) (CGMCC No. 5971); anatipestifer (Rheinheimera tangshanensis) (CGMCC No. 5972), acinetobacter (Acinetobacter lwoffii) (CGMCC No. 5973), Pseudomonas (Pseudomonas fluorescens) (CGMCC No. 5974), and Wickerhamomyces anomalus (CGMCC No. 5975).    USE - For producing textile fiber (claimed).    ADVANTAGE - The method has low production cost; saves energy; is environment-friendly; and provides high economic benefit. In the method, the waste liquid is directly converted into organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a textile fiber, involving (i) taking Bacillus, anatipestifer, acinetobacter, Pseudomonas, and Wickerhamomyces anomalus in mass ratio of 2-3:1-2:1-2:1-2:2-3; (ii) cutting all raw material into segments and then putting into a soaking pool swelling; (iii) soaking the prepared bacterial liquid into hydrophobic solution; sterilizing the biodegradable raw material; obtaining fiber for the first time period from the sterilized raw material, grinding fiber bundle to make the fiber being separated into single fiber, then drying, and carding; putting the prepared fiber in warm water for soaking, then drying, and carding to give the textile fiber.
NOVELTY - Bacterial composition comprises Bacillus sp. having preservation number of CGMCC No. 5971, Rheinheimera tangshanensis having preservation number of CGMCC No.5972, Acinetobacter lwoffii having preservation number of CGMCC No. 5973, and Wickerhamomyces anomalus having preservation number of CGMCC No. 5975.    USE - In the preparation of textile fiber (claimed).    ADVANTAGE - The composition prepares textile fiber by using the method that does not pollute the environment, converts the waste liquid into organic fertilizer, realizes zero discharge and zero pollution; provides biological treatment process to protect the fiber, as compared with the traditional chemical method; is low cost and high economic production method; and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing textile fiber involving preparing composite bacteria water solution: mixing Bacillus sp., Rheinheimera tangshanensis, Acinetobacter lwoffii, and Wickerhamomyces anomalus at weight ratio of 2-3:1-2:1-2:2-3 with bacterial liquid to form composite bacteria water solution; raw material treatment: cutting raw material and putting into soaking pool for swelling; seal coat fiber: steam sterilizing the soaked raw material, preparing fiber bundle, fine grinding the fiber bundle to make separated single fiber, screening, filtering after a period of grinding and the slurry after the second fine grinding of the fiber bundle, and then grinding to make it into single fiber, drying; and carding: soaking the prepared fiber in warm water, and then drying, carding to form textile fiber.
NOVELTY - Bacterial composition comprises Bacillus sp. having preservation number of CGMCC No. 5971, Rheinheimera tangshanensis having preservation number of CGMCC No. 5972, Acinetobacter lwoffii having preservation number of CGMCC No. 5973, and Wickerhamomyces Anomalus having preservation number of CGMCC No. 5975.    USE - In the preparation of paper pulp (claimed).    ADVANTAGE - The composition prepares paper pulp by using the method that recycles the waste liquid and converted into marsh gas or organic fertilizer that used as energy source; is environment-friendly; realizes zero discharge and zero pollution; and reduces 30% energy consumption as compared to traditional pulping.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing paper pulp involving preparing bacteria liquid by mixing Bacillus sp., Rheinheimera tangshanensis, Acinetobacter lwoffii, and Wickerhamomyces anomalus at weight ratio of 1-3:1-3:1-2:2-3; cutting woody raw material and soaking in pool; mitigating the swelling of the thread raw material, crushing and grinding, soaking the biodegradable material; steam sterilizing the soaked biodegradable material; roughly grinding slurry to form fiber bundle, fine grinding to make fiber beam and separating single fiber, screening, filtering, and washing with water to form paper pulp.
NOVELTY - Bacterial composition comprises Rheinheimera tangshanensis having preservation number of CGMCC No. 5972, Acinetobacter lwoffii having preservation number of CGMCC No. 5973, and Wickerhamomyces anomalus preservation number of CGMCC No. 5975.    USE - In the preparation of paper pulp (claimed).    ADVANTAGE - The composition prepares paper pulp by using the method that does not pollute environment; converts waste material into organic fertilizer; realizes zero discharge and zero pollution; reduces 30% energy consumption as compared with the traditional pulping; is low cost production method; and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing paper pulp involving preparing bacteria liquid by mixing Rheinheimera tangshanensis, Acinetobacter lwoffii, and Wickerhamomyces anomalus at weight ratio of 1-3:1-2: 2-3; cutting woody raw material and soaking in pool; mitigating the swelling of the thread raw material, crushing and grinding, soaking the biodegradable material; steam sterilizing the soaked biodegradable material; roughly grinding slurry to form fiber bundle, fine grinding to make fiber beam and separating single fiber, screening, filtering, and washing with water to form paper pulp.
NOVELTY - A composite biological flora comprises Bacillus species (CGMCC NO: 5971), Acinetobacter lwoffii (CGMCC NO: 5973), Pseudomonas fluorescens (CGMCC NO: 5974), and Wickerhamomyces anomalus (CGMCC NO: 5975).    USE - As a composite biological flora used in biological bacterial liquid pulping application, and in paper-making process (claimed).    ADVANTAGE - By using composite biological liquid for paper pulping, paper of more than AA level can be obtained. The waste liquid generated in pulping process is recycled, and is used for conversion into marsh gas or organic fertilizer, thus the process not only saves energy, but also is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for paper-making process by using bacterial liquid involving adding Bacillus species, Acinetobacter lwoffii, Pseudomonas fluorescens and Wickerhamomyces anomalus in water at a weight ratio of 1-3:1-2:1-2:2-3, cutting all materials into sections, soaking the cut materials into soaking pool for swelling, then crushing and grinding the materials, sterilizing the biodegradable raw material by putting it into bacterial liquid to roughly grinding into slurry, to form fiber bundle, fine grinding the slurry, to form fiber beam, then screening and filtering the slurry, followed by washing by soaking single fibers in warm water to prepare paper pulp.
NOVELTY - A bacterial composition comprises: Rheinheimera tangshanensis having preservation number of CGMCC No.5972, Acinetobacter lwoffii having preservation number of CGMCC No.5973, and Pseudomonas fluorescens having preservation number of CGMCC No.5974.    USE - In the preparation of textile fiber (claimed).    ADVANTAGE - The bacterial composition provides textile fiber using a method that convert waste liquid directly into organic fertilizer, does not pollute the environment, and save energy thus economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing textile fiber involving: providing bacterial liquid including Rheinheimera tangshanensis, Acinetobacter lwoffii, and Pseudomonas fluorescens according to weight ratio of 1-2:1-2:1-2; cutting ramie raw material and soaking in pool for swelling; and preparing fiber by: soaking raw material in the bacterial liquid, and sterilizing to obtain biodegradable raw material, grinding the biodegradable raw material to make fiber, and soaking the prepared fiber in warm water, followed by drying and carding to obtain textile fiber.
NOVELTY - A composite flora comprises: Acinetobacter lwoffii (CGMCC No. 5973), Pseudomonas fluorescens (CGMCC No. 5974) and Wickerhamomyces anomalus (CGMCC No. 5975).    USE - For preparing paper (claimed).    ADVANTAGE - The method has low production cost; saves energy; is environment-friendly; and provides high economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for making paper in bacterial liquid, involving: taking Acinetobacter lwoffii, Pseudomonas fluorescens and Wickerhamomyces anomalus in a weight ratio of 1-2:1-2:2-3; cutting all raw material into segments and then putting into a soaking pool swelling; soaking the prepared bacterial liquid into hydrophobic solution; sterilizing the biodegradable raw material; obtaining fiber from the sterilized raw material, grinding fiber bundle to make the fiber separated into single fiber, drying, and carding; putting the prepared fiber in warm water for soaking, then drying, and carding to give paper.
NOVELTY - A composite flora comprises: Bacillus species) (CGMCC No. 5971), Acinetobacter lwoffii (CGMCC No. 5973) and Pseudomonas fluorescens (CGMCC No. 5974).    USE - For producing textile fiber (claimed).    ADVANTAGE - The method has low production cost; saves energy; is environment-friendly; and provides high economic benefit. In the method, the waste liquid is directly converted into organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a textile fiber, involving (i) taking Bacillus, Acinetobacter, and Pseudomonas, in mass ratio of 2-3:1-2:1-2; (ii) cutting all raw material into segments and then putting into a soaking pool swelling; (iii) soaking the prepared bacterial liquid into hydrophobic solution; sterilizing the biodegradable raw material; obtaining fiber for the first time period from the sterilized raw material, grinding fiber bundle to make the fiber being separated into single fiber, then drying, and carding; putting the prepared fiber in warm water for soaking, then drying, and carding to give the textile fiber.
NOVELTY - A penicillin G acylase mutant derived from Escherichia coli ATCC 11105 penicillin G acylase wild type base amino acid having amino acid sequence containing 846 amino acids as given in the specification and comprising specific amino acid mutations, is new.    USE - For catalyzing reaction between 6-APA-HPGM.HCl and amoxicillin; in expression vector; in a suspension or dispersion of nanoparticles; and for synthesizing amoxicillin (claimed).    ADVANTAGE - The mutant easily generates drug resistance and does not easily cause allergy. The mutant as compared to wild type greatly improves utilization rate of raw materials, reduces production cost, and reduces energy consumption and environment pollution.    DETAILED DESCRIPTION - A penicillin G acylase mutant derived from Escherichia coli ATCC 11105 penicillin G acylase wild type base amino acid having amino acid sequence containing 846 amino acids (SEQ ID No. 1) and comprising any of 1-8 amino acid mutations selected from alpha Asn110Gln, alpha Asp154Glu, beta Asn176Gln, beta Gln204Asn, beta Glu85Asp, beta Lys95Arg, beta Gln233Asn, and beta Asp334Glu, is new. INDEPENDENT CLAIMS are included for the following:    (1) new nucleic acid coding the penicillin G acylase mutant;    (2) an expression vector comprising the nucleic acid;    (3) a suspension or dispersion of nanoparticles comprising the expression vector according to a host cell; and    (4) a method for synthesizing amoxicillin involving combining the penicillin G acylase mutant, (+)-6-aminopenicillanic acid (6-APA) and hydroxyphenylglycine methyl ester (HPGM).HCl and a synthetic amoxicillin.
NOVELTY - A Streptomyces fradiae tylosin fermentation culture medium, comprises a primary seed culture, a secondary seed culture medium and a fermentation culture medium, where the primary seed culture medium contains peanut cake powder, the secondary seed culture medium contains corn oil, and the fermentation culture medium contains mixed meal of peanut meal and corn oil.    USE - As Streptomyces fradiae tylosin fermentation culture medium (claimed) for producing tylosin useful as macrolide antibiotics.    ADVANTAGE - The method effectively improves fermentation unit and shortens fermentation period, and at the same time further replaces soybean raw materials into corn oil, a fish meal and peanut meal; reduces the production cost; maximizes the reduction of sources of raw materials from the environment, to ensure their adequate supply; and achieves stable and high efficient production of tylosin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation involving: 1) sterilizing first level seed culture medium, cooling, and keeping sterile air, then under the protection of inert gas, cultivating Streptomyces fradiae mother bottle fermentation liquid in first level seed tank to culture, controlling inoculating volume amount to 5-10% at the first level seed culture medium; 2) second level seed culture medium sterilizing, cooling, and keeping a sterile air, and then moving all the first level seed liquid to second level seed tank to culture; and 3) sterilizing the fermentation culture medium, cooling, and keeping a sterile air, and then adding the whole second level seed liquid into fermentation tank to culture.
NOVELTY - The system has a tower (57), a dryer (58), a mercury separating tank (59), a dust filter (60), a cooler (62), a compressor (61), a heat exchanger (54), a heavy hydrocarbon separation tank (23) and a nitrogen tank (41). A connecting pipe (53) is connected with a cold inlet pipe. The cold inlet pipe is connected with the nitrogen tank by a pipeline (52). The pipeline is connected with the cold inlet pipe. The heat exchanger is connected with the compressor and a condenser. The cooler connected with a fuel system.    USE - Natural gas double-cooling agent and liquefying system.    ADVANTAGE - The system is simple and has low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a block circuit diagram of natural gas double-cooling agent and liquefying system. '(Drawing includes non-English language text)'    Heavy hydrocarbon separation tank (23)    Nitrogen tank (41)    Pipeline (52)    Connecting pipe (53)    Heat exchanger (54)    Tower (57)    Dryer (58)    Mercury separating tank (59)    Dust filter (60)    Compressor (61)    Cooler (62)
NOVELTY - Device comprises: a first chamber having a grinding mechanism operable to grind the refuse or shearing device operable to break up the refuse; a second chamber attached to the first chamber, where the second chamber stores the ground refuse to promote the composting; and a conduit interconnecting the first chamber to the second chamber, to share thermal energy and moisture between the first and second chamber.    USE - The device is useful for transforming refuse into compost (claimed) where the compost is useful in farming.    ADVANTAGE - The device: performs certain functions automatically without user input operations; facilitates the cleansing of the device itself; is operable to facilitate and maintain the cleanliness of the device; and facilitates introduction of refuse into the device where user direct handling and manipulation of the refuse is minimized.
NOVELTY - Dry shampoo comprises a base comprising 0.1-30 wt.% of a sebum absorber, a polyol and a propellant.    USE - The dry shampoo is useful for cleansing the hair.    ADVANTAGE - The dry shampoo is capable of cleansing the hair without washing with water and leaving white residue on the hair, and provides a clean feel to the user.
NOVELTY - A hydrogen generating apparatus (100) has modifier (3) which produces hydrogen containing gas by modification reaction of raw material, material supply device (1) which supplies raw material to the modifier, air supply device (2) which supplies air to the modifier, transformer (4) which reduces carbon monoxide in the hydrogen-containing gas by shift reaction using conversion catalyst for oxidative degradation, and controller (5) which controls the air supply device and decreases air supply rate to the modifier in connection with the temperature rise of the conversion catalyst.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Oxidative degradation of a conversion catalyst is suppressed.    DETAILED DESCRIPTION - A hydrogen generating apparatus (100) has modifier (3) which produces hydrogen containing gas by modification reaction of raw material, material supply device (1) which supplies raw material to the modifier, air supply device (2) which supplies air to the modifier, transformer (4) which reduces carbon monoxide in the hydrogen-containing gas by shift reaction using conversion catalyst for oxidative degradation, and controller (5) which controls the air supply device and decreases air supply rate to the modifier in connection with the temperature rise of the conversion catalyst while supplying raw material and air to the modifier and heating up the modifier from the material supply device and the air supply device. INDEPENDENT CLAIMS are included for:    (1) fuel cell system; and    (2) operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generating apparatus.    Material supply device (1)    Air supply device (2)    Modifier (3)    Transformer (4)    Controller (5)    Hydrogen generating apparatus (100)
NOVELTY - Preparing upgraded pyrolysis oil, comprises: providing a biomass-derived pyrolysis oil stream having an original oxygen content; hydrodeoxygenating the biomass-derived pyrolysis oil stream under catalysis in the presence of hydrogen to form a hydrodeoxygenated pyrolysis oil stream comprising a cyclic paraffin component; and dehydrogenating at least a portion of the hydrodeoxygenated pyrolysis oil stream under catalysis to form an upgraded pyrolysis oil stream.    USE - The process is useful for preparing upgraded pyrolysis oil.    ADVANTAGE - The process removes oxygen and other heteroatoms from a biomass-derived pyrolysis oil stream and converts naphthenes or cyclic paraffin compounds with at least one alkane ring to their corresponding aromatic compounds, thus maximizes fuel value for the upgraded pyrolysis oil.
NOVELTY - This utility model is a kind of used for exogenous microbial enhanced device for biochemical sewage treatment, comprising a device box body is set on the box body, the two sections of bioreactor component, comprising a waste water pre-processing part and fungicide activating part, electric mechanical part to sewage condition and flow control part, and control process. The waste water pre-processing part comprises a pipeline connected with a sewage or tap water inlet pre-processing filter and ultraviolet disinfector, the microbial inoculum activating part comprises the first reactor and the second reactor, the ultraviolet sterilizer is connected with the reactor through the pipeline; This utility model can realize automatically activating strain, automatic and continuous feeding and multilevel control amount, does not need manual feeding, it only needs to periodically change agent box, and is small in volume, easy to install, free of maintenance.
(CN202898244-U)   NOVELTY - This utility model is a kind of microwave kitchen garbage processor, comprising a machine frame, the machine frame is provided with a hopper, the hopper is provided with a mixing rod, hopper and the mixing rod are respectively connected with the driving motor, wherein it is provided with a microwave generator on the upper part of the hopper and the exhaust fan, the hopper up and down and the middle is provided with a position sensing switch is further provided with a temperature and humidity probe, temperature-humidity probe is connected with the temperature and humidity meter, wherein the said hopper, the said driving motor, a micro-wave generator, temperature and humidity meter, an exhaust fan and position sensing switch are electrically connected with the PLC controller, the utility model uses microwave drying technology, the semi-finished product after drying, adding the organic the formulation, kitchen processor because of microwave technology to use, the machine is special anti-radiation design, avoids the drying process of the microwave leakage, electricity-saving, small volume, not generate the smell and noise.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a microwave kitchen waste processor.
NOVELTY - Aerobic digestion of sludge comprises using microbial inoculum, Bacillus subtilis, Bacillus stearothermophilus, Bacillus pumilus, Bacillus licheniformis at mol ratio of 1-4:2-6:1-5:1-4, processing to pre-concentrated tank and standing; and concentrating, adding 0.5-10% microbial inoculum into reactor, reacting for 72-120 hours, refluxing for 3 hours, controlling pH at 6-9 and temperature at 45-65 degrees C, storing, and processing sludge self-heating-type high-temperature aerobic digestion into sludge collecting pit.    USE - Method of aerobic digestion of sludge (claimed).    ADVANTAGE - The method reduces sludge treatment process and has low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the aerobic digestion of sludge.
NOVELTY - Treatment of excess sludge comprises adding 1-5% residual sludge and 0.1-0.8% mixed enzyme, mixing, and adding into liquid fermentation tank to ferment. The bacteria liquid contains Bacillus subtilis, Bacillus megaterium, Bacillus licheniformis or Bacillus natto; and the mixed enzyme comprising amylase, protease, hemicellulase and amylase.    USE - Method of treatment of excess sludge (claimed).
NOVELTY - Dry-type anaerobic fermentation device comprises a feeding straw kneading machine and a material collecting tank. A bucket elevator enclosure is fixed at the material collecting tank. A bucket elevator feed port is abutted against a straw rubbing machine discharge port. A bucket elevator is installed at the bucket elevator enclosure. A bucket elevator discharge port arranged at the bucket elevator enclosure is abutted against a material pushing conveyer feed port on a material pushing conveyer. A discharge port is inserted into an anaerobic fermentation tank.    USE - Used as a dry type anaerobic fermentation feeding device.    ADVANTAGE - The compact dry type anaerobic fermentation feeding device easily and simply avoids the phenomenon of feeding blockage with cost effective manner.    DETAILED DESCRIPTION - Dry-type anaerobic fermentation device comprises a feeding straw kneading machine and a material collecting tank. A bucket elevator enclosure is fixed at a bottom of the material collecting tank. A bucket elevator feed port installed on the one side wall of the bucket elevator enclosure is abutted correspondingly against a straw rubbing machine discharge port arranged on the straw rubbing machine. A bucket elevator is installed at the top end of the bucket elevator enclosure. A bucket elevator discharge port arranged at the top end of the bucket elevator enclosure is abutted correspondingly against a material pushing conveyer feed port on a material pushing conveyer located at the upper part of the bucket elevator enclosure. A discharge port at the tail end of the material pushing conveyer is inserted into an anaerobic fermentation tank.
NOVELTY - A detoxification fermenting agent comprises Lactobacillus plantarum 6002, abnormal Hansenula yeast 2-300, gordonia bauxite, Bacillus subtilis, and manure fiber unit.    USE - As detoxification fermenting agent for preparing foliar fertilizer, solid biological organic fertilizer, and organic matter-decomposing inoculant (claimed).    ADVANTAGE - The detoxification fermenting agent prepares fertilizer that promotes the growth and development of plant, reduces environment within plant pesticide and nitrate, provides nontoxic high-efficient good biological product, promotes soil indigenous microbe, improves root soil ecological environment, improves soil physical and chemical properties, enhances soil acid-base buffer ability of the soil, is good for absorption and utilization of crops, greatly reduce loss of fertilizer, improves ability to resist disease, regulates plant metabolism, enhances stress resistance of the plant disease, and improves yield and quality of the crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing detoxification fermenting agent involving culturing Lactobacillus plantarum 6002 in culture medium at 30-36 degrees C for 24 hours, culturing Hansenula in potato culture medium at 25-30 degrees C for 20-24 hours, inoculating activated lactobacillus plantarum 6002 and abnormal Hansenula yeast at 1:1 ratio, into the fermentation tank to obtain microbial inoculum (I); inoculating bauxite gordonia to obtain microbial inoculum (II); inoculating bacillus subtilis with potato culture medium, to obtain microbial inoculum (III), inoculating the manure fiber 91081 in potato culture medium to obtain microbial inoculum (IV); and mixing microbial inoculum (I), (II), (III), and (IV) at volume ratio of 0.5-1:1-2:1-2:1-2 to obtain detoxification fermenting agent.
NOVELTY - This utility model claims a kind of integrated type garbage landfill gas pre-processing and torch sleeve device, comprising a pre-processing and control system, a pre-processing pipeline inlet and outlet is orderly provided with a gas-water separator, a condenser, a purifying system and a vacuum air pump, the vacuum air pump is provided with a first output end and a second output pipeline output pipeline, the first output pipeline is provided with an automatic valve, a temperature transmitter, a pressure transmitter and a flow meter, and gas generating set passes through fire arrestor and the second output pipe is connected to the torch, the second output pipeline is provided with a second automatic valve, said automatic valve, a temperature transmitter, a pressure transmitter, a flow meter and a second automatic valve are respectively connected with the control system. This utility model is the whole integrated box-type design, can be movably mounted, a gas pipe will not be blocked by the control system at the first output and the second output pipe pipeline is a component integrated control, convenient operation and use.
NOVELTY - Production of alkaline fertilizer involves mixing phosphate rock tailings or low-grade phosphate rock with insoluble sylvine-containing rock in the weight ratio of 1:0.4-0.9, adding 3-8 wt.% blind coal, obtaining mixed material, drying and grinding the mixed material into 60-150 meshes, obtaining powder material, providing the powder material into a rotary kiln, baking for 30-150 minutes at 1000-12000 degrees C to prepare sintered clinker, quenching the sintered clinker, cooling to 400-700 degrees C for 1-10 minutes, draining, drying, crushing and grinding.    USE - Production of alkaline fertilizer (claimed).    ADVANTAGE - The alkaline fertilizer is economically and efficiently produced with excellent maneuverability without polluting the environment, by a simple process.
NOVELTY - Method for preparing fermented bed litter, involves using raw materials comprising 20-50 wt.% sawdust, 20-50 wt.% rice hull, 20-30 wt.% crop straw, 2-3 wt.% auxiliary materials, and 0.1-0.3 wt.% fermenting agent, where sawdust is obtained from bushes, trees, shrubs or their pulverized product, crop straw is cut into 1-2 cm, and obtained from crushed corn stalks, cotton stalks or their mixtures, and fermenting agent is fermented using Bacillus subtilis (CGMCC 1.1413) and Lactobacillus casei (CGMCC 5182).    USE - The method is useful for preparing fermented bed litter which is useful as breeding material for pig (claimed).    ADVANTAGE - The fermented bed litter absorbs, degrades and digests excrement of pigs during breeding, and hence pig manure is degraded in situ in fermenting bed, and source pollution of rural environment in pig industry is eliminated.
NOVELTY - This utility model relates to precipitate submerged biological filter tank, comprising a sedimentation tank, a biological filler layer, a strip-shaped grid, screen stencil and a sludge pump, a biological filler layer, strip-shaped grid and interception screens are set in the sedimentation tank, biological filler layer is immersed filter the sedimentation tank in the middle, the strip-shaped grid on the biological filler layer, the screen on the lower part of the biological filler layer, a sludge pump is set on the mud side of the sedimentation tank, the mud and the sedimentation tank are connected with each other. Compared with the existing technology, this utility new drawing by using sludge pump, the biological filler layer agglomeration by interception screens action of filler dispersed along with the water flow into the sedimentation tank, and solves the problem that the biological filter pool is easy to block;
NOVELTY - A kind of gas storage integrally assembled biogas biological fermentation device, comprising a fermentation tank and a storage bag, a fermentation tank provided with opening flange, the side vertical surface of the flange provided with semicircular groove, and matched with the groove of the sealing ring, is cylindrical and the top is semi-spherical, and its bottom is open, the upper part of the marsh gas side of the air cylinder is further provided with a binding belt for binding the bag tightly storing. This utility model has good leak tightness, no leakage, it is safe to use; the gas with the gas storage integrated because of the combination mode, the device is featured with simple structure, low cost and convenient installation, which not only reduces the special setting traditional product in a marsh gas storage device, saves the mounting time of the product, but also reduces the production cost, at the same time, realize the product in the transportation process of the large volume of high transportation cost so as to further enlarge the covering range of the biogas biological fermentation device, and it has good economic and social benefit.
NOVELTY - A kind of marsh gas voltage-stabilizing and recycling device, belonging to the technical field of marsh gas, comprising a marsh gas inlet pipe, the first container, the second container, the third container and marsh gas outlet pipe, the first container is filled with water, the air outlet end of the air inlet pipe is inserted into the marsh gas in the first container, the upper end of the first container and the second container through the first gas pipe, the second container is filled with water and the water level is a water level and a third container depth is half of irrigation, the depth of the second container, the third container, the second container and the third container through the first water pipe is connected to a container of the marsh gas outlet pipe is connected with the upper end of said third container is provided with a water outlet pipe. This device has the stabilized voltage and recycling the marsh gas and using the function.
NOVELTY - A kind of the shell can avoid the biogas generating device, belonging to the technical field of marsh gas, comprising a tank body, a tank cover, a tank cover is provided with a material inlet and a gas outlet pipe, the tank body is provided with a stirring device. The stirring device comprises a motor, a speed reducer, a transmission shaft, a rotating disc, a stirring rod, an electric motor is fixed at the top of the tank cover, the motor is equipped with a speed reducer, a transmission shaft is connected with the speed reducer, and the lower end is connected with the rotating disc, a stirring rod is fixed on the rotary disk edge. This utility model can effectively avoid the pool in the body happen crust.
NOVELTY - Biogas tank residue extractor device, belonging to the field of marsh gas, comprising a cylinder body, a supporting column, a through-hole and a lifting lug, the upper part of the cylinder body is provided with a lifting lug, the bottom cylinder is provided with a supporting column, the side wall of the cylinder is provided with a plurality of through holes. The lifting lug is circular, the bottom of the cylinder is provided with three supporting rods are equal. The side wall of the cylinder body is opened with 15 rows of through holes, each row is provided with a through hole (12) are equal. The whole cylinder hanging from the marsh gas tank, wherein the inner wall of the cylinder of the slag is taken out is very convenient, which greatly saves the labour force.
NOVELTY - Biogas tank residue pressing device, belonging to the field of marsh gas, comprising a cover, a lock catch, a barrel body, a hydraulic device, a support leg, a bottom frame, a rocking handle, a bottom plate, a water outlet hole and a lifting lug, the cover buckled on the barrel body by a lock catch, the lock catch is fixed on the cover, the lower barrel body is welded with a support leg, and a hydraulic device is welded on the bottom frame, the bottom plate is welded on the hydraulic device on the lifting rocking control hydraulic device, so as to drive the up and down movement of the bottom plate, the bottom plate is opened with a water outlet hole. The lock catch is fixed with four symmetrically distributed on the cover, the top end of the barrel body is provided with the outer edge, the lock buckle. Cover, barrel body, support leg, bottom support and a bottom plate is made of stainless steel material, the side wall of the barrel body is provided with a lifting lug. The residue in the barrel body, a compressed, extruding water, which not only increases the volume and does not influence the road environment, the device has simple structure, the operation is convenient to carry;
NOVELTY - Marsh gas pool dreg, belonging to the marsh gas production field, comprising an inner rod, a main rod, a sliding groove, a connecting rod, a rotating shaft, a supporting rod, a handle, a grabbing body housing net, the main rod is hollow, one end is welded and fixed on the supporting rod, the middle section of the main rod is provided with a sliding groove, the rod extends into the inner part of the main rod passes through one end of the rotating shaft and two connecting rods are connected with the inner rod and the main rod are in clearance fit, one end of the connecting end of the other one end of the handle rod is connected with the handle through the rotating shaft of the middle section is connected to the supporting rod through the rotating shaft, the grabbing body and welding end fixed on the grab body with cover. This utility model through the upper part of the inner rod to move up and down to drive the grabbing body close, the whole device is controlled by the connecting rod mechanism, the screen water, improve the efficiency of dredging residue, the operator can stand on the marsh gas tank opening for dredging residue, so as to effectively prevent the marsh gas pool dredging when fishing for the safety of human body, is provided with simple structure, convenient and safe operation and so on.
NOVELTY - This utility relates to a kind of solar energy and marsh gas energy are combined with a device, specifically a solar energy marsh gas tank system, comprising a marsh gas tank, feeding the liquid in the marsh gas tank, marsh gas tank is set on the upper part of the pressure meter and a biogas outlet, biogas tank is provided with a periphery cylinder, the periphery through a water inlet pipe and a water outlet pipe respectively connected with the integrated water heater is provided with a solar optical collector is set the corresponding position of the water heater, the water outlet pipe is provided with a water pump, the utility model can realize the single biogas normally fermenting, and it will not damage biogas fermentation bacteria.
NOVELTY - A kind of chlorine-alkali workshop of the utility model relates to chlorine-alkali industry field of concentrating procedure of steam condensed water recycling device. The technical solution is as follows: comprising a condensing water tank, the inlet is connected with the steam pipeline and a condensed water evaporation and condensation water pipeline, and the steam condensing water tank is connected with a heat exchanger and brine, and then is connected with the salt water pipeline. The upper part of the steam condensed water pipeline is provided with a branch pipeline and aniline by-product steam system. This utility model is a steam condensed water in the process of concentrating and heat evaporation and condensation water recycle together for pre-heating the refined salt water, and a condensed water also can be linked with the aniline industrial system, as soft water producing steam, and the reasonable use of steam condensed water and evaporation and condensation water, energy saving and emission reduction, at the same time, greatly reduces the production cost.
NOVELTY - Catalyst, comprising ferric oxide, copper oxide, manganese oxide, ruthenium oxide, rhodium oxide and aluminum oxide complex, is new.    USE - The catalyst is useful for preparation of dimethyl sulfoxide.    ADVANTAGE - The dimethyl sulfoxide preparation method: utilizes catalyst/catalyst composition, which has high catalytic activity in preparing dimethyl sulfoxide; utilizes only oxygen as an oxidizing agent in comparison with nitric acid and potassium permanganate used in conventional methods; does not produce any harmful substances in the preparation process, thus does not pollute the environment.    DETAILED DESCRIPTION - Catalyst, comprising ferric oxide, copper oxide, manganese oxide, ruthenium oxide, rhodium oxide and aluminum oxide complex having formula (aFe2O3.bCuO.cMnO2M.dRuO2.eRh2O3.fAl2O3), is new.    a, b, c = 0-15; and    d, e, f = 0.01-10.    INDEPENDENT CLAIMS are also included for:    (1) preparation of the catalyst;    (2) catalyst composition, comprising the catalyst and a photosensitizer in a ratio of 1:0.1-10; and    (3) preparation of dimethyl sulfoxide, comprising adding solvent into dimethyl thioether, adding the catalyst as mentioned above, irradiating with light of wavelength 190-780 nm at an air or oxygen atmosphere of 1-30 atm, reacting at 0-50 degrees C for 48 hours, where the weight ratio of solvent and catalyst is 1:0-50:0.01-2.
NOVELTY - An organic materials separating device comprises loading bunker which is installed under sieve slope, vibrator which is rigidly connected with sieve slope, and adenosine triphosphate part provided in the sieve slope. A section is connected with vibrator and is made in form of concave elastic cores. A cantilever is fixed on axis with possibility of changing slope angle relative to sieve slope. The vibrator works with transresonant frequency.    USE - Device for separation of organic materials.
NOVELTY - Device for processing biogas and organic fertilizer of agricultural wastes, comprises solid-phase and methane tanks connected together by conduits in upper part for introducing a liquid fraction of substrate, and in bottom part for circulation of filtrate; loading branch pipe in upper part of solid-phase methane-tank; unloading branch pipe for removing recycled substrate in bottom part of methane-tank; and branch pipe for selection of biogas.    USE - The device is useful for processing biogas and organic fertilizer of agricultural wastes (claimed).    DETAILED DESCRIPTION - Device for processing biogas and organic fertilizer of agricultural wastes, comprises solid-phase and methane tanks connected together by conduits in upper part for introducing a liquid fraction of substrate, and in bottom part for circulation of filtrate; loading branch pipe in upper part of solid-phase methane-tank; unloading branch pipe for removing recycled substrate in bottom part of methane-tank; and branch pipe for selection of biogas, where solid-phase methane-tank is supplied with horizontal micromesh, placed lower than level of the liquid fraction of the substrate, outlet opening of loading branch pipe is placed under the grid, and branch pipes for introducing a liquid fraction of the substrate are installed above the grid, where branch pipe for circulation of filtrate from the solid-phase methane-tank in methane-tank is installed tangentially to the internal the surface of the latter.
NOVELTY - Manufacture of solid fuel involves providing livestock dung discharged from the stud farm of excrement separation system, and mixing composition with biomass and waste oil.    USE - Manufacture of solid fuel used as fuel for cement kiln, calcination furnace and boiler (all claimed).    ADVANTAGE - The solid fuel is economically and efficiently manufactured with excellent handling property, and reduced dehydration of livestock dung.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining the manufacture of solid fuel. (Drawing includes non-English language text)    Livestock dung collection process (1)    Solid-liquid-separation process (2)    Fermentation composting process (3)    Mixing process (4)    Stud farm (11)
NOVELTY - A personal care product has an outer container, a partially expanded collapsible bag (418) disposed in the outer container, an elastic member surrounded a portion of the collapsible bag in order to stretch the elastic member axially and radially, and a personal care composition (419) disposed in the collapsible bag, where the elastic member is constructed of an elastically extensible material that permits the transfer of infrared radiation through a portion of the elastic member.    USE - Personal care product for applying a personal care composition to skin in the form of a film.    ADVANTAGE - The product does not need to be highly pressurized, and applies personal care composition without use of an additional applicator to skin in a safe and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an article.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-section view of the skin care product.'(Drawing includes non-English language text)'    Shaped container (412)    Overcap (414)    Material dispensing system (416)    Collapsible bag (418)    Personal care composition (419)
NOVELTY - Improving tolerance of rapes to petroleum and lead contaminated soil comprises before rapeseeds are sowed, spraying dilute bacterial agent to soil, diluting bacterial agent, soaking the seeds in the dilute bacterial agent and sowing the seeds; after the rapeseeds are sowed, infiltrating dilute bacteria in each hole; and in the rape growth process, monitoring the content of rape chlorophyll every week from the seedling stage.    USE - The method is used for improving tolerance of rapes to petroleum and lead contaminated soil (claimed).    ADVANTAGE - The method above is environment-friendly. The method provides rape plants with increased chlorophyll and carotenoid content. The plants are tall, and have thick stalks, and improved dry weight and fresh weight. The plants have improved proline, peroxidase and phytochelatin content and reduced malonaldehyde content. The physical and chemical properties of the soil can be very remarkably improved and the soil fertility is improved.    DETAILED DESCRIPTION - Improving tolerance of rapes to petroleum and lead contaminated soil comprises before rapeseeds are sowed, spraying dilute bacterial agent to soil, diluting bacterial agent, soaking the seeds in the dilute bacterial agent and sowing the seeds; after the rapeseeds are sowed, infiltrating dilute bacteria in each hole; and in the rape growth process, monitoring the content of rape chlorophyll every week from the seedling stage: selecting typical plants in a population, selecting the latest fully-unfolded leaves, determining the content of the chlorophyll, or at the budding stage and the full-bloom stage, respectively taking and spraying calcium chloride solution on leaf surfaces once if the content of the chlorophyll is low, and then taking, diluting and spraying photosynthetic bacteria agent stock solution once.
NOVELTY - Bio-organic fertilizer is prepared by mixing and fermenting mushroom residue, humic acid, bovine blood polypeptide and high-efficiency microbial agents with a ratio of 1:2:1:2.    USE - As bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer has comprehensive and lasting nutrients and fertilizer efficiency as long as 120 days, can continuously transform soil nutrients, contains several beneficial microorganisms, and hence secrete biologically-active substance, improves soil structure, solves problem of soil hardening, and recovers soil self-production capacity. The bio-organic fertilizer reduces pesticide residues, and improves living environment of the plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned bio-organic fertilizer, which involves performing the above-mentioned step.
NOVELTY - Bacterial manure is obtained by preparing fish protein hydrolysate, using photosynthetic bacterium liquid culture, 5406 actinomycetes liquid culture and Bacillus subtilis liquid culture, and mixing the liquids in a certain proportion, where photosynthetic bacteria contain antiviral substances, 5406 actinomycetes has inhibiting effect to more than 30 pathogenic bacteria, and propagation of Bacillus subtilis can achieve the aims of improving the soil fertility and improving crop yield and quality.    USE - As bacterial manure.    ADVANTAGE - The bacterial manure improves soil fertility, crop yield, quality, disease resistance and stress resistance of plants, and crop quality under synergistic effect of beneficial bacteria, and promotes crop growth.
NOVELTY - Method of using adsorption resin to recover paracetamol from mother liquor comprises providing refined mother liquor from paracetamol production refining process, absorbing by resin filled in resin column of refined mother liquor of paracetamol, and performing solution evaporation and crystallization.    USE - Method for using adsorption resin to recover paracetamol from mother liquor (claimed).    ADVANTAGE - The method reduces energy consumption, has simple process and easy operation and has high recovery rate.
NOVELTY - Preparation of N-L-alanyl-L-glutamine comprises dissolving D-2-substituted-acrylic acyl-L-glutamine in water, replacing air with an inert gas, carrying out ammonia ammonolysis reaction after decompressing to remove ammonia, discoloring, adding strong polar organic solvent and crystallizing to obtain product.    USE - Method of preparation of N-L-alanyl-L-glutamine (claimed).    ADVANTAGE - The method avoids waste and reduces environment pollution and has low cost and is suitable for industrial production.
NOVELTY - Method for inhibiting generation of methane-containing gas, involves laying a sediment modifier on the sediment of the water area. The sediment modifier comprises steelmaking slag containing 10 %mass or more total iron content and 0-20 %mass granulated blast furnace slag.    USE - Method for inhibiting generation of methane-containing gas (claimed).    ADVANTAGE - The method stably inhibits the generation of methane-containing gas from sediment of river, lakes, marshes water area, culture water area and domestic wastewater.
NOVELTY - A catalyst comprises perovskite oxide (I) containing rare earth elements, alkaline earth metal element or alkali metal element and transition metal element or metalloid element.    USE - Catalyst used for manufacturing thermochemical fuel (claimed) used as clean energy for industrial applications and clean industrial source of chemical applications.    ADVANTAGE - The catalyst is economical and carries out conversion storage of the solar energy with high efficiency, and provides catalyst with reduced usage amount of rare metal.    DETAILED DESCRIPTION - A catalyst comprises perovskite oxide of formula: AXO3 plus minus delta (I).    A=rare earth elements, alkaline earth metal element and/or alkali metal element;    X=transition metal element and/or metalloid element;and    delta =0-1.    An INDEPENDENT CLAIM is included for manufacture of thermochemical fuel, which involves manufacturing fuel from heat energy using two-stage thermochemical cycle, using the catalyst at temperatures (T1, T2). The temperature (T2) is below the temperature (T1). The temperature (T1) is 600-1600 degrees C and the temperature (T2) is 400-1600 degrees C.
NOVELTY - Fermenting drum (1) comprises a hollow cylindrical drum container (2) comprising a tubular drum wall (3) and terminated on two opposite end faces with a respective front wall which has a filling opening (9) and a discharge opening (10), and is rotatably supported on a bearing device. The end faces respectively comprise a centrally arranged bearing axle and the bearing axles are connected by radial support structures with the drum wall.    USE - The fermenting drum is useful for continuous fermentation of biomass.    ADVANTAGE - The fermenting drum: ensures continuous fermentation of the biomass; and has large-volume with simple and inexpensive rotatable mounting.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of a rotatable cantilevered fermenting drum having a bearing shaft at its end faces.    Fermenting drum (1)    Drum container (2)    Drum wall (3)    Filling opening (9)    Discharge opening (10)
NOVELTY - The apparatus (10) has rotary motor (13) which is made to rotate rotary element (12) centering on rotating shaft (11). An electrolysis unit (15) is provided, such that the water accommodated in inside of water storage pipe (21) is electrolyzed to the front-end of water storage pipe for generating hydrogen and oxygen. A hydrogen recovery tube (18) collects hydrogen generated by electrolysis unit, so that the supply of hydrogen is possible even if hydrogen recovery tube is extended from front-end of water storage pipe.    USE - Apparatus for manufacturing high-pressure hydrogen used as fuel for fuel cell electric vehicle.    ADVANTAGE - The hydrogen recovery tube collects hydrogen generated by electrolysis unit for enabling supply of hydrogen, so that the working efficiency of apparatus can be improved, and the high-pressure hydrogen can be manufactured efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the high-pressure hydrogen manufacturing apparatus.    High-pressure hydrogen manufacturing apparatus (10)    Rotating shaft (11)    Rotary element (12)    Rotary motor (13)    Electrolysis unit (15)    Hydrogen recovery tube (18)    Water storage pipe (21)
NOVELTY - The system (1) has an ozone supply apparatus (7) that adds ozone to activated sludge. Immersion film tub (4) purifies organic waste water sent from an activated sludge tank (2) via immersion film (4A) provided in middle of a path connecting activated sludge tank and immersion film tub. Retention tank retains organic waste water more than preset time when ozone concentration of organic waste water that passes immersion film becomes below allowable ozone concentration of immersion film. The organic waste water is passed from activated sludge tank to immersion film tub.    USE - Waste-water-treatment system for processing organic waste water such as sewage and excrement from foodstuff factory, industry and kitchen.    ADVANTAGE - Since the organic waste water from which ozone is removed can be sent to immersion film tub, the deterioration of immersion film can be prevented. Since the suspended matter in the organic waste water flowing into immersion film tub can be removed in retention unit, the clogging of immersion film is prevented. The improvement of waste-water-treatment capability and the sludge settle-ability improvement by reproduction suppression of filamentous fungi can be attained. The waste-water by high process flow volume can be filtered effectively, without degrading the film and membrane module structural element. The high-degree waste water treatment is performed, so as to completely remove the solid substance remaining in the treated water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a wastewater treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the waste-water-treatment system. (Drawing includes non-English language text)    Waste-water-treatment system (1)    Activated sludge tank (2)    Immersion film tub (4)    Immersion film (4A)    Ozone supply apparatus (7)
NOVELTY - The method involves decomposing organic waste into pyrolysis gas and char with an internal circulation kiln (20). The pyrolysis gas is separated into tar liquid and dry gas. The separated tar liquid is cooled to 100 degrees C or less and is fed into the circulation kiln. The flow volume of gas is controlled, so that the pressure in internal circulation kiln is set to atmospheric pressure. The level of char is measured from the presence or absence of electric current applied to an electrode pair. The char is extracted continuously while maintaining the level of char in predetermined range.    USE - Thermal decomposition gasification method of organic waste e.g. wood type biomass such as mowed grass, pruned branch, coppiced timber, fallen leaves, and bark, general wastes such as municipal solid waste and purification-tank sludge, industrial waste such as sewage sludge, paper, wood chip, waste plastic, rubber and animal-and-plant residue, and radioactive organic waste such as foodstuff, forest products and marine product.    ADVANTAGE - The gasifier can be provided to thermally decompose organic waste and to take out high calorie fuel gas with reduced volume of radioactive organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a thermal decomposition gasifier of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the thermal decomposition gasifier.    Feed hopper (10)    Internal circulation kiln (20)    Tar splitter (30)    Dry gas blower (50)    Thermal decomposition gasifier (100)
NOVELTY - The heat-processing installation has a preset steam generation unit to collect the potential heat of dry waste gas emitted with drying machine, and to generate preset steam. A specific steam generation unit generates specific steam by using emitted combustible gas. A pressure rise unit pressure-rises preset steam one portion by making specific steam into drive source. A steam compression unit compresses preset steam remainder portion mechanically. A pressure-rise steam supply unit supplies the pressure-rise steam as a heat source and dries a to-be-processed object with drying machine.    USE - Heat-processing installation for heating to-be-processed object e.g. sewage-sludge dried with indirect heating-type drying machine e.g. steam tube dryer used for drying woody biomass, foodstuff, organic substance, and organic waste.    ADVANTAGE - The heat recovery can be economically carried out from dry waste gas, when heating to-be-processed object by heating installation after drying the to-be-processed object containing moisture content and organic substance. The process unit price of 1,700 yen/t of sewage sludge is reduced, when processing amount of sewage-sludge is 100t /day and the emission amount of conversion carbon-dioxide is reduced. The requisite quantity of pressure-rise steam can be given to indirect heating-type drying machine as heat source which dries to-be-processed object with indirect heating-type drying machine without receiving the fluctuation of moisture content of to-be-processed object.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heat-processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the heat-processing installation. (Drawing includes non-English language text)
NOVELTY - The method involves crushing potato pulp subjected to compaction of biomass in a dispenser to particle size of 3 to 5 mm, to obtain proper mixing uniformity of compaction of biomass in a conditioner. The main component of biomass is selected in form of bran, oat, wheat and rye when used for the production of pellets with the participation of pulp. The main component is used as exaggerated cereal pellets for using as fuel to provide function of feed additive.    USE - Method for producing fuel and fodder granules.    ADVANTAGE - The method enables crushing potato pulp subjected to compaction of biomass in the dispenser to particle size of 3 to 5 mm, to easily obtain proper mixing uniformity of compaction of biomass in the conditioner.
NOVELTY - A core-shell magnetic composite is disclosed, which includes: a magnetic core; a shell containing a protective layer and a porous layer, wherein the magnetic core is coated with the protective layer and the porous layer is the outmost layer of the shell; and a hydrophobic functional group grafted to the shell. In addition, the core-shell magnetic composite can be bound to a lipase to act as a transesterification catalyst. The present invention also relates to a method for producing biodiesel.
NOVELTY - A blending method of pyrolysis biomass fuel and diesel for replacing diesel in power engine, which firstly mixes diesel with Span 80 in a specific proportion under the temperature of 0 to 120 degrees Celsius so as to form a first fuel, and mixes Bio-fuel with Tween 80 in a specific proportion under the temperature of 0 to 120 degrees Celsius so as to form a second fuel, and then mixes the first fuel with the second fuel according to a specific proportion, thus forming the biomass fuel for replacing diesel. Such a biomass fuel can be used directly or used as a fossil diesel additive, which is applicable to power equipments, such as diesel engine, boiler, generator, burner and so on, and will not separate the added fuel material from one another after leaving alone for a long time.
NOVELTY - Making a fractionated extractive products comprises: converting at least a portion of native cellulose I( beta ) to cellulose III(I) by treating plant biomass with liquid ammonia and/or at least one organic solvent to produce a treated plant biomass containing lignin and a lignin fraction; and extracting lignin and/or other plant cell wall components from the lignin fraction to produce a lignin extract capable of being fractionated.    USE - The method is useful for making a fractionated extractive products such as fractions (F1)-(F4) and pure lignin, where the fractions (F1) and (F2) are both useful as a fertilizer, the fraction (F3) is useful in catalytic transformation using hydrogenation reactions, and containing primarily low molecular weight lignin components are useful as antimicrobial agents in paints, adhesive binders and coatings, the fraction (F4) is useful as a polymer precursor, and the pure lignin is useful in carbon fiber production or energy generation (all claimed).    ADVANTAGE - The method: is cost effective; provides higher yields of clean lignin; avoids the use of binders for improving the logistical properties or stability of the resulting hydrolyzable particulates; and recovers more than 97% of the ammonia, with the remaining 3% having reacted with cell wall components which is re-used during pretreatment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a fractionated extractive product made by the process as above per se; and    (2) a reactor system comprising a reactor adapted to convert native cellulose I( beta ) to cellulose III(I) by treating plant biomass with liquid ammonia and/or at least one organic solvent to produce a treated plant biomass containing lignin and a lignin fraction and extract lignin and/or other plant cell wall components from the lignin fraction to produce a lignin extract, and a monitoring system to monitor the reactor.
NOVELTY - The hydrogen accumulating device includes an electrolyzer water, a fuel element, fuel element separators, and connecting conduits. An electrolysis cell and the fuel element are provided with temperature control units coupled with each other and with a user thermal network by the connecting conduits.    USE - Hydrogen accumulating device.
NOVELTY - Houttuynia cordata extract is produced by performing washing process and dehydration process for foreign material and microbe elimination of Houttuynia cordata using acidic water after harvesting, crushing to obtain Houttuynia cordata raw juice, filtering raw juice to obtain transparent red liquid of Houttuynia cordata extract, mixing honey in Houttuynia cordata extract, fermenting, and drying.    USE - Houttuynia cordata production for processed goods, such as cooked rice, salad, vinegared rice, alcohol- processed food, milk-processed food, fish-meat- processed food, pickles-in-vinegar-processed food, drink, processed soybean, wheat-processed food, starch-processed food, agar-processed food, seasoning-processed food, cosmetics e.g. shampoo, rinse, skin lotion, lotion, milky lotion, and cream, clothing e.g. undergarments, socks, muffler, T-shirt, and handkerchief, wound therapeutic agent, preservatives, detergent for fruit and vegetable washing, agricultural goods e.g. soil dispersant, foliar application agent, and insect repellent, and foodstuff and drinks for humans and animals (all claimed).    ADVANTAGE - Production process is convenient and environment-friendly, and product has good-quality taste, antimicrobial property, and room-temperature storage stability and improves health of person, animal, or livestock.
NOVELTY - The fuel cell system has water pump which supplies reformation water in water tank to evaporation portion. A rotation speed sensor detects rotation speed of per unit time of water pump based on physical quantity regarding rotation speed of water pump. A control unit allows fuel cell to continue to generate power and repeats short-time increase and short-time decrease of rotational speed of water pump with respect to abnormal rotational speed, thus repeating short-time increase and short-time decrease of S/C value in reforming reaction and averaging S/C value.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system can maintain S/C value in appropriate region even when the rotational speed of water pump is abnormal with respect to target rotational speed region during the power generation operation of fuel cell in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating the control process for increasing or decreasing rotation speed of motor. (Drawing includes non-English language text)
NOVELTY - A metallic compound contains an anionic aromatic polycarboxylic acid having 6-22 aromatic ring-forming carbon atoms and at least three carboxylate groups, and at least one metal ion chosen from alkaline-earth metal ion.    USE - Metallic compound is used for adsorbent for adsorbing carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane and organic vapor, occlusion material for occluding carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia and organic vapor, and separation material for separating carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane and organic vapor, and methane, carbon dioxide and hydrogen, carbon dioxide and nitrogen, carbon dioxide, ethylene and carbon dioxide, methane, ethane and ethane, ethylene and propane, propene or air and methane (all claimed).    ADVANTAGE - The metallic compound has excellent gas-adsorption characteristics, gas occlusion capacity, and gas-separation characteristics. The occlusion material containing the metallic compound has excellent water resistance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) adsorbent;    (2) occlusion material;    (3) separation material;    (4) separation method, which involves contacting metallic compound and mixed gas at pressure of 0.01-10 MPa; and    (5) manufacture of metallic compound, which involves reacting and depositing anionic aromatic polycarboxylic acid and metal ion in a solvent.
NOVELTY - Obtaining molecular hydrogen from water involves electrochemical method in presence of catalyst, where the catalyst is used salt which has a stable electron in the excess radical, and which performs the role of background electrolyte, where an electrochemical process machines has the potential of 0 to -1 B.    USE - For obtaining molecular hydrogen from water (claimed).
NOVELTY - The method involves performing decomposition process of water using resonance electromagnetic field and two resonance outlines. The tension vectors of electric fields of first circuit and second circuit are acted on water. The tension of magnetic fields is coincided and perpendicularly directed to vectors of electric fields, to produce change of dielectric constant of water condenser, and to adjust operation of adjustable circuit in resonance mode. The resonance values are determined from maximum production rate of isolated gas, with respect to obtained results in series product.    USE - Method for judging maximum production rate for decomposition of water using hydrogen loop (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen loop.
NOVELTY - Installation for generating biogas, comprises loading bunker; flow meter; three-way crane; centrifugal pump; manometer; cavitation heat-generator; measuring units; tank; and valve, where the installation is pre-manned by bioreactor, by methane-tank and by container for unloading, and cavitation heat-generator is applied with hydrodynamic heat generator-destructor.    USE - The installation is useful for generating biogas (claimed).
NOVELTY - The device has a cylindrical drum (6) mounted on rollers (5). A rotating frame (1) is provided with seat rings (7). A motor (10) is provided with a driven gear (9) and a gear sprocket (8). The cylindrical drum is wrapped in a thermal insulator layer (11). The cylindrical drum is equipped with a temperature sensor (12). Inside the cylindrical drum is installed with knives (15) and an agitator (16). An outlet channel (27) of the cylindrical drum is provided with a gas sensor (30). The gas sensor is connected with an electronic gas measurement unit (31) through a wire.    USE - Device for composting organic waste.
NOVELTY - System has engines with electric generators. Fuels are also provided which include hydrogen and natural gas. Fuel is introduced in an ignition system.    USE - System for generating electricity for industries and homes.    ADVANTAGE - The system enables to generate electricity automatically and economically.
NOVELTY - The stirrer comprises a set of impellers arranged on a stirring shaft in a spaced apart manner and fixed to a brace that is arranged on a main blade, and an auxiliary blade arranged on the brace between the main blade and the stirring shaft, where a horizontal type anaerobic extinguishing device is arranged along a length of a stirring axis. The main blade horizontally meets the impeller in the stirring axis. The impellers are arranged in a rotational direction of the stirring axis. The auxiliary blade is mounted on the middle part of the brace.    USE - The stirrer is useful in a horizontal type anaerobic extinguishing device (claimed) that is used to treat organic waste and produce biogas i.e. methane.    ADVANTAGE - The main blade and auxiliary blade uniformly stir the organic waste so as to perform the treatment process in an efficient manner with improved transition speed and by optimizing the possession angle of the main blade.    DETAILED DESCRIPTION - The stirrer comprises a set of impellers arranged on a stirring shaft in a spaced apart manner and fixed to a brace that is arranged on a main blade, and an auxiliary blade arranged on the brace between the main blade and the stirring shaft, where a horizontal type anaerobic extinguishing device is arranged along a length of a stirring axis. The main blade and the brace are equipped on the XZ plane, where an axial direction of the stirring axis is Z-direction, a vertical direction of the stirring axis is Y-direction and the horizontal direction of the axis is X-direction. The auxiliary blade is arranged on the XY plane. The main blade horizontally meets the impeller in the stirring axis, where the length of the auxiliary blade is 1/3-1/2 of the main blade. The brace is provided with two bars. The impellers are arranged in a rotational direction of the stirring axis. The auxiliary blade is mounted on the middle part of the brace.
NOVELTY - A pool is collected, moisture content of collected pool is maintained to 3-7%, dried in drying pool and hot-air dried to cut pool having length of 0.1 mm to 2 cm and crushed. 5-9 weight% Charcoal dust, 8-10 weight% pool seed, 75-85 weight% twig and residual wood, 1-3 weight% pyroligneous liquor, and 1-3 weight% sericite powder are added and mixed material is molded under pressure of 0.5-1.5 ton/cm2 for 5-20 minutes, to obtain molding frame. The material is mixed in molding frame, discharged from mold, dried naturally and compressed, to obtain grass briquet.    USE - Manufacture of grass briquette (claimed).    ADVANTAGE - The grass briquette is efficiently manufactured.
NOVELTY - The device has half reactor carbide (200) which feeds fuel to richness type combustor (300) and synthetic gas combustor (400) supplies heat to the biomass dryer (100) the exhaust gas from the half reactor carbide is spread to the anoxic exhaust gas. The half reactor carbide is provided with the dried biomass and the biomass dryer drying the biomass. The biomass dryer dries the biomass through the exhaust gas from the synthetic gas combustor.    USE - Biomass torrefaction device.    ADVANTAGE - The biomass within the biomass dryer is dried through the combustion of gas generated in the half reactor carbide and the anoxic exhaust gas generated in the fuel richness type combustor. The thermal efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biomass torrefaction device. (Drawing includes non-English language text)    Biomass dryer (100)    Half reactor carbide (200)    Richness type combustor (300)    Synthetic gas combustor (400)
NOVELTY - The method involves heating the red mud, crushing heated red mud in a fixed bed reactor at 300-1000 degrees C, introducing controlled amounts of an organic compound and carbon source into the fixed bed reactor in an inert atmosphere. The reduction of iron hydroxide is performed by using organic compound for forming the magnetic phase. Carbon is deposited in the form of amorphous carbon and graphite nanofibers or nanotubes.    USE - Method for conversion of red mud waste into amphiphilic material including mineral oil, essential oil, diesel, biodiesel, gasoline, fat, decalin, tetralin, toluene, kerosene, xylene, grease and vegetable oils, such as olive oil, soybean oil, corn oil, canola oil, flaxseed oil, peanut oil, coconut oil, cotton oil, sunflower oil and castor oil (Claimed).    ADVANTAGE - The method ensures easy conversion of red mud waste into amphiphilic material in an eco-friendly manner.
NOVELTY - This utility model claims a kind of biological diesel oil reaction device, mainly comprising a high-level tank, a methanol oil tank, a flow meter, a set of reaction column, a separating tank, methanol tank, oil tank are respectively connected with the flow meter and the reaction column pipe, wherein a SK static mixer and the flow meter and the reaction column, a static mixer is a reaction column outlet and inlet connected with a separating tank after each set of reaction column. The beneficial effect of the utility model is, it can make the biological diesel oil ester exchange reaction of the different stages respectively, that caused by a phase ester exchange reaction and improves reaction conversion rate.
NOVELTY - A marsh gas filtering device comprises two carbon dioxide removing containers (2) which are cylindrical and connected in series. The upper part of first carbon dioxide removing container has air inlet (1) connected with an air inlet pipe (3). The upper part of second carbon dioxide removing container has air outlet (6) and feeding port (7), and the lower part has discharging hole (8).    USE - Marsh gas filtering device.    ADVANTAGE - The device is simple, has low cost and simple operation, and uses sodium hydroxide solution for absorbing carbon dioxide and residual hydrogen sulfide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of marsh gas filtering device.    Air inlet (1)    Carbon dioxide removing container (2)    Air inlet pipe (3)    Air outlet (6)    Feeding port (7)    Discharging hole. (8)
NOVELTY - Simultaneous cleaning and improving quality of biogas comprises putting biogas slurry in multistage reactor comprising multiple single-stage photobioreactors connected in series, and performing photosynthetic carbon fixation using fermentation waste liquid as culture medium and microalgae as inoculum.    USE - Simultaneous cleaning and improving quality of biogas (claimed).    ADVANTAGE - The economical and environment-friendly method has strong practicability.
NOVELTY - A methanol gasoline comprises 60-80 pts. wt. methanol, 10-25 pts. wt. gasoline, 5-8 pts. wt. xylene, 1-4 pts. wt. aniline, 1-2 pts. wt. trinitrotoluene, 1-2 pts. wt. nitrobenzene, 10-13 pts. wt. dibutyl phthalate, 10-15 pts. wt. dimethyl carbonate and 8-12 pts. wt. acetone.    USE - Methanol gasoline.    ADVANTAGE - The gasoline reduces cost of fuel and protects environment.
NOVELTY - Domestic garbage gasification furnace comprises through-hole at furnace bottom, which is divided into upper and lower parts, where upper part is a gasification chamber, and lower part is a motor chamber, and discharging device having discharging through-hole connected with gasification chamber through furnace bottom plate. The gasification chamber is divided from top to bottom into gasification area, high temperature area, and feeder, which are respectively connected by gas pipe. The high temperature area is provided with a turning device.    USE - Domestic garbage gasification furnace.    ADVANTAGE - The device has high efficiency and low investment, is energy-saving and environment-friendly, and enables recycling of household garbage.    DETAILED DESCRIPTION - Domestic garbage gasification furnace comprises through-hole at furnace bottom, which is divided into upper and lower parts, where upper part is a gasification chamber, and lower part is a motor chamber, and discharging device having discharging through-hole connected with gasification chamber through furnace bottom plate. The gasification chamber is divided from top to bottom into gasification area, high temperature area, and feeder, which are respectively connected by gas pipe. The gasification area is provided with feeder; and the high temperature area is provided with a turning device, which is fixed on a hollow rotating shaft connected with a cylinder. The motor chamber comprises turbine cylinder driven by motor and gear box operation.
NOVELTY - A methanol fuel additive comprises 40-50 pts. wt. dimethoxymethane, 15-25 pts. wt. xylene, 3-8 pts. wt. fatty acid amine, 1-2 pts. wt. potassium chloride and 3-6 pts. wt. methyl tert-butyl ether.    USE - Methanol fuel additive.    ADVANTAGE - The additive improves heating value of methanol and efficiency of promoting combustion rate. It has good corrosion resistance and good temperature adaptability.
NOVELTY - A lipase mutant with increased optimum temperature obtained by lipase gene sequence (GenBank EF405962), is new, where the amino acid of the mutant is Asp310Val.    USE - The lipase mutant is useful in oil processing, synthetic biodiesel or bread baking fields (claimed).    ADVANTAGE - The mutant has important industrial application.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing mutant strain; and    (2) method for producing genetically engineered strain, involves inoculating 10 volume/volume% inoculum size to 25 ml buffered glycerol-complex Medium (BMGY) culture medium at 30 degrees C for 16-20 hours, centrifuging the collecting thalli, diluting the culture medium to optical density (OD)600, adding the above-mentioned medium and culturing for 3-4 days, collecting fermentation liquid, concentrated the supernatant by 10 KD ultrafiltration membrane, cation exchange chromatography and Phenyl-Sepharose hydrophobic chromatography column chromatography to obtain the purified mutation lipase activity.
NOVELTY - Mutant Nannochloropsis sp. (OZ-I HP-1) with a preservation number CGMCC No. 6140, is new.    USE - The strain is useful for production of oil, biodiesel oil, fatty acid, chlorophyll A, carotenoid and/or biomass (claimed).    ADVANTAGE - The strain: increases biomass accumulation rate to 19%, chlorophyll A content to 45% and carotene content to 47% when compared with wild strain; increases oil accumulation in the biomass to 33%, increases oil yield to 28%, and increases triacylglycerol content in oil composition to 14% when compared with wild strain; and has fast growth, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for mutation breeding of the mutant Nannochloropsis sp. (OZ-I HP-1).
NOVELTY - This utility model claims a kind of biological diesel oil removing device, mainly composed of a ((/yanlu:)) groove (1), a liquid inlet (5), a liquid outlet (6), a salt water outlet (7), wherein the ((/yanlu:)) groove (1), the lower part of the baffle plate (4), there is a step on the ((/yanlu:)) groove of the baffle plate (4) (1) is provided with a baffle plate (2). The baffle plate (4) is made of stainless steel with a certain gap. Baffle plate (4) and clapboard (2) divides the ((/yanlu:)) groove (1) is divided into a left chamber (1a) and the right chamber (1b), the lower chamber (1c) of chamber, the left chamber (1a) and the lower chamber (1c), the lower chamber (1c) and the right chamber (1b), a left chamber (1a) and the right chamber (1b). The left chamber (1a) of the baffle plate (4) is placed a plurality of layers of metal silk screen (3), screen mesh (3) is from up to down layer by layer. ((/yanlu:)) Is a method to remove water of bio-diesel, continuously removing the purpose of saving water. This utility model is the action capable of continuous operation, has the advantages of convenient operation, simple use and so on.
NOVELTY - The utility model claims a reinforced biological diesel oil ester exchange reaction synthesizing device, wherein the device comprises a raw material storage tank, a flash evaporator, a heat exchanger, a ester exchange reaction device, short chain alcohol distilling device, purifying device and a finished product oil storage tank, wherein the device further comprising a manifold in fluid communication with an ester-exchanging reaction device of short chain alcohol and catalyst, the ester exchange reaction device is the ester exchange reaction, the ester exchange reaction device is mainly composed of a pump body, a pump cover, a rotating shaft and a rotating shaft with a blade of the impeller in the pump body are respectively opened with suction port and ester exchange reaction product outlet, the suction port and the suction tube is provided with a raw material inlet and a short chain alcohol and catalyst inlet; Strengthening ester exchanging reaction device of the utility model uses the strong mechanical impact force and high shearing high speed vortex generated by the force and cavitation function principle, the mass transfer process of ester exchange reaction to obtain reinforced, so as to shorten the reaction time, the finished bio-diesel.
NOVELTY - A mutant lipase with improved activity, obtained by introducing mutation in wild-type lipase comprising a 317 amino acid sequence (SEQ ID NO: 8) fully defined in the specification, is new.    USE - The mutant lipase is useful for producing biodiesel (claimed).    ADVANTAGE - The biodiesel can be produced cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide encoding the mutant lipase;    (2) expression vector comprising the polynucleotide;    (3) transformant obtained by introducing the expression vector or the polynucleotide into the host cell;    (4) method of producing the mutant lipase; and    (5) method of producing the biodiesel, involves obtaining the transformant, culturing the transformant, collecting the lipase from the culture material or supernatant and producing the biodiesel.
NOVELTY - Methanol gasoline additive comprises 20-50 wt.% of methanol, 30-40 wt.% of gasoline, 8-10 wt.% of ethanol, 0.3-0.6 wt.% of isobutyl alcohol, 0.02-1.5 wt.% of tertiary butyl alcohol, 1-4 wt.% of acetone, 5-10 wt.% of dimethyl ether and 0-0.05 wt.% of corrosion inhibitor.    USE - The additive is used as a fuel.    ADVANTAGE - The methanol gasoline additive improves the combustion performance of the gas, heat efficiency, and increases performance of the gasoline.
NOVELTY - An environment-friendly methanol gasoline comprises 70-80 wt.% methanol, 10-15 wt.% heating value agent, 0.5-1 wt.% antifreeze, 0.5-2 pts. wt. acetone or butanone, 5-10 wt.% solubilizer, 0.5-1 wt.% additive, 0.5-1 wt.% wetting agent and 0.5-1 wt.% corrosion inhibitor.    USE - Environment-friendly methanol gasoline.    ADVANTAGE - The methanol gasoline has low flash point.
NOVELTY - Ethanol gasoline additive comprises 50-60 pts. wt. of gasoline, 20-30 pts. wt. of absolute ethyl alcohol, 3-8 pts. wt. of toluene, 1-8 pts. wt. of alkyl phenol polyoxyethylene ether, 3-9 pts. wt. of methyl tertiary butyl ether and 2-4 pts. wt. of hexamethyl phosphoric acid amine.    USE - The ethanol gasoline additive is useful for preparing fuel.    ADVANTAGE - The ethanol gasoline additive has equivalent oil consumption compared to that of national standard gasoline and discharge index according to the environment-friendly demand. The contents of sulfur and lead in the additive are much lower than the contents of sulfur and lead in the national standard and other similar ethanol gasoline additives.
NOVELTY - Alcohol-ether gasoline additive comprises 30-40 pts. wt. methanol, 30-40 pts. wt. ethanol, 2-5 pts. wt. isobutanol, 5-10 pts. wt. isopropanol, 0.5-3 pts. wt. dimethyl carbonate, 1-2 pts. wt. isobutane, 20-30 pts. wt. petroleum ether, 20-30 pts. wt. dimethyl ether and 5-20 pts. wt. methyl tert-butyl ether.    USE - Alcohol-ether gasoline additive.    ADVANTAGE - The additive has high cleaning performance, low production cost and no adverse reaction upon mixing with gasoline. It prevents corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of alcohol-ether gasoline additive comprising uniformly mixing methanol, ethanol, isobutanol and isopropanol to get modified methanol; uniformly mixing petroleum ether, dimethyl ether, methyl tert-butyl ether to prepare ether mixture; and mixing dimethyl carbonate, isobutane, modified methanol and ether mixture for 20 minutes and standing for 2 hours.
NOVELTY - Ethanol gasoline cosolvent comprises xylene, fatty alcohol-polyoxyethylene ether, isobutyl alcohol, methyl tert-amyl ether, butanone and nonylphenol ether.    USE - Ethanol gasoline cosolvent.    ADVANTAGE - The solvent has good stability. It combusts completely, does not knock, produces less exhaust and saves fuel.
NOVELTY - Methanol gasoline additive, comprises methanol and modifier in a weight ratio of 92-97:3-8, where the modifier comprises 5-25 pts. wt. of isobutyl alcohol, 10-20 pts. wt. of oleic acid, 18-22 pts. wt. of dimethyl carbonate, 7-13 pts. wt. of dimethyl ether, 1-3 pts. wt. of methyl tertiary butyl ether, 12-18 pts. wt. of ethyl ether, 9-11 pts. wt. of acetone, 3-7 pts. wt. of tertiary butyl alcohol, 0.8-1.2 pts. wt. of hexamethylene tetramine and 1.6-2.4 pts. wt. of benzotriazole.    USE - Used as methanol gasoline additive.    ADVANTAGE - The methanol gasoline additive reduces oil content rate of 6.5-9.8%, carbon rate of 40% and hydrocarbon rate of 60%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the methanol gasoline additive, comprising taking and adding the raw materials into a reaction kettle to obtain mixture, heating the obtained mixture at 50-55 degrees C for 30-45 minutes, and filtering the heated mixture.
NOVELTY - Producing synthetic natural gas and food-grade carbon dioxide using calcium carbide furnace gas, comprises purifying the calcium carbide furnace gas and then pressurizing, mixing the pressurized gas with medium-pressure steam, providing the obtained mixture in a shift-converter to carry out shift-conversion process, and providing the obtained gas in a methanation reactor to carry out methanation process and then providing in a decarbonization system to remove carbon dioxide.    USE - The process is useful for producing synthetic natural gas and food-grade carbon dioxide using calcium carbide furnace gas (claimed).    ADVANTAGE - The process enables economic production of synthetic natural gas and food-grade carbon dioxide in a rapid manner.
NOVELTY - Preparing biodiesel using imidazole anion-type alkaline ionic liquid as a catalyst, comprises adding soybean oil to a three-mouth round bottom flask, pre-heating a water bath to a set temperature, adding a mixed solution of catalyst and methanol into the flask, refluxing and reacting, cooling in an ice bath, and transferring into a separating funnel for stratification, recovering methanol by vacuum distillation, where the lower layer includes glycerol, catalyst and superfluous methanol, recovering methanol, and then adopting extraction process for recovering catalyst and glycerol.    USE - The method is useful for preparing biodiesel using imidazole anion-type alkaline ionic liquid as catalyst.    ADVANTAGE - The method adopts imidazole anion-type alkaline ionic liquid, which is convenient to recover and has high catalytic activity, good thermal stability and less corrosiveness.    DETAILED DESCRIPTION - Preparing biodiesel using imidazole anion-type alkaline ionic liquid as a catalyst, comprises adding soybean oil to a three-mouth round bottom flask, pre-heating a water bath to a set temperature, adding a mixed solution of catalyst and methanol into the three-mouth round bottom flask, refluxing and reacting at normal pressure, quickly cooling to room temperature in an ice bath, and transferring into a separating funnel for stratification of an upper-layer biodiesel oil (fatty acid methyl ester) and trace amounts of methanol, recovering methanol by vacuum distillation, and then adopting gas phase chromatography for yield analysis, where the lower layer includes glycerol, catalyst and superfluous methanol, recovering methanol by vacuum distillation, and then adopting extraction process for recovering catalyst and glycerol.
NOVELTY - The device has a porous permeable ion component (2) and common reinforcing film assembly (4) which are respectively fixed in a box main portion. The box main portion is divided into water storage cavity (1) hydrogen generating cavity (3) and oxygen generating chamber (5). The insulating layers are arranged on the peripheries of side surfaces of porous permeable ion component and common reinforcing film assembly.    USE - Efficient exchange membrane device for producing hydrogen by electrolyzing water.    ADVANTAGE - The structure of the efficient exchange membrane device can be simplified. The weight of the device can be reduced. The transformation efficiency, safety and reliability of the device can be improved. The processing difficulty of the device can be reduced. The manufacturing cost of the device can be reduced. The exchange membrane device can be produced without using several auxiliary equipments. The marketability of the device can be improved. The hydrogen energy can be widely used. The device can be easily installed in various places.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the efficient exchange membrane device.    Water storage cavity (1)    Porous permeable ion component (2)    Hydrogen generating cavity (3)    Common reinforcing film assembly (4)    Oxygen generating chamber (5)
NOVELTY - The bio-reactor has vapor direct injection portion (130) with the high temperature and high pressure and impeller (120) which are provided within the glycosylation reaction portion (100). The fetching unit (140) is set for collecting the product generated by the glycosylation reaction within the glycosylation reaction portion. The influx unit is set for supplying the biomass to the glycosylation reaction portion with addition. Biomass includes the marine algae or the cellulose class.    USE - Bio-reactor for saccharification of biomass with direct steam injection.    ADVANTAGE - The collapsing and accelerating the saccharification time can be reduced. The economic effect of the bio-reactor can be improved effectively. The process cost can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of biofuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the bio-reactor. (Drawing includes non-English language text)    Glycosylation reaction portion (100)    Impeller (120)    Vapor direct injection portion (130)    Fetching unit (140)    Exhausting portion (160)
NOVELTY - This utility model claims a biological diesel oil and a device, biological diesel oil removing device is mainly composed of a ((/yanlu:)) groove (1), screen mesh (3), an annular baffle plate (4), a liquid outlet (5), a salt water outlet (6), a liquid level meter (7), wherein the ((/yanlu:)) groove (1), the lower part of the baffle plate (4), is provided with an annular ((/yanlu:)) groove (1) is set in the middle of the first sedimentation pipe passes through the annular baffle plate (4) (2), an annular baffle (4) and sedimentation pipe (2) is ((/yanlu:)) groove (1) is divided into inner chamber (1b), an outer chamber (1a), the lower chamber (1c) of chamber, chamber (1b) and the lower chamber (1c), the outer chamber (1a) and the lower chamber (1c), chamber (1b) and the outer chamber (1a). ((/yanlu:)) Is a method to remove water of bio-diesel, continuously removing the purpose of saving water. This utility model is the action capable of continuous operation, has the advantages of convenient operation, simple use and so on.
NOVELTY - This utility model claims a rectification section return-flow system, comprising a rectifying tower, extracting pump, a cooling water heat exchanger, a product tank and a biologic diesel oil of the rectifying tower liquid collecting tank, the collecting tank and biological diesel oil extracting pump, extracting pump and a cooling water heat exchanger, the cooling water heat exchanger and the product tank through the pipeline is connected with the middle upper part of the rectifying tower is provided with a reflowing groove, the cooling water pump and the pipeline of the heat exchanger is connected with the raw material oil, the raw oil heat exchanger and a cooling water heat exchanger between the pipe and the groove is further connected with a pipeline. The rectification mesomere return-flow system avoids the malpractice caused by top reflux, so that the product is featured with relative good purity, colour and smell.
NOVELTY - Use of Schizochytrium thallus residue containing normal hexane is claimed for production of biogas. The production method involves pretreating Schizochytrium thallus residue, mixing pretreated liquid with straw in mass ratio of 1:1-1:25, where the liquid serves as nitrogen source and fermenting at 38-42 degrees C.    USE - The Schizochytrium thallus residue containing normal hexane is useful for producing biogas (claimed).    ADVANTAGE - Biogas is produced in an environmentally-friendly and cost-effective manner as Schizochytrium thallus residue generated as waste in production process of docosahexaenoic acid is utilized effectively.
NOVELTY - An immobilized cell capable of synthesizing biodiesel, is new. The immobilized cell is produced by (a) screening strains, (b) preparing porous polyamine chitosan microsphere carrier, (c) preparing whole-cell lipase and immobilizing the whole-cell lipase using porous polyamine chitosan microsphere, and (d) performing esterification of immobilized whole-cell lipase for producing biodiesel from slop oil or waste oil.    USE - The immobilized cell is useful for synthesizing biodiesel (claimed).    ADVANTAGE - The immobilized cell converts waste cooking oil into biodiesel.
NOVELTY - Producing cassava alcohol using cassava bagasse microbial fermentation method involves mixing cassava alcohol residue, weathered coal or humic acid grass (peat) straw ash, with water; adding the mixture in microbial inoculum (2%), stirring uniformly; and filling the stirred mixture into sealed bag, carrying out anaerobic fermentation at normal temperature for our country southern for 10 days, to produce ethanol having viable bacteria count of not less than 300 million/g.    USE - For producing cassava alcohol (claimed).    ADVANTAGE - The method has low cost, simple operation, high product quality; solves the problem of environmental pollution; reduces the cost; and provides environment-friendly cassava alcohol. The cassava alcohol improves soil environment, improves crop yield, and improves quality of crop of fertilizer.
NOVELTY - Water electrolysis hydrogen production system comprises power supply device (1), electrolytic tank (2), hydrogen separator (3), oxygen separator (6) and purification tower (5). The power supply device, hydrogen separator and oxygen separator are connected to electrolytic tank.    USE - A water electrolysis hydrogen production system.    ADVANTAGE - The system ensures high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of water electrolysis hydrogen production system.    Power supply device (1)    Electrolytic tank (2)    Hydrogen separator (3)    Purification tower (5)    Oxygen separator (6)
NOVELTY - Vehicle-mounted hydroxide machine comprises machine main body, electrolytic cell (3), electrode, electrode plate, bubble bottle (5), filter (7) and pressure regulator (9). The machine main body is provided with water injection port connected to water tank. The machine main body is provided with anode and cathode connected power supply (1), and hydroxide outlet (6). The electrolytic cell is set inside machine body.    USE - A vehicle-mounted hydroxide machine.    ADVANTAGE - The machine increases oxygen supply to promote combustion, saves fuel by 30%, increases kinetic energy by more than 30% and reduces emissions by 40%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of vehicle-mounted hydroxide machine.    Power supply (1)    Electrolytic cell (3)    Bubble bottle (5)    Hydroxide outlet (6)    Filter (7)    Pressure regulator (9)
NOVELTY - The cogeneration system has a brown gas formation unit (10) to electrolyze water and produce the brown gas. An igniter (30) ignites the brown gas supplied from a brown gas storage tank (20). A combustion chamber (40) combusts the ignited brown gas to heat a heating element. An electricity storage unit (50) supplies power to brown gas formation unit. A heat power plant (60) generates electricity from the heat supplied from the combustion chamber. An alternating current (AC) power source converter (70) converts the generated electricity to AC power source.    USE - Cogeneration system for supplying power to building.    ADVANTAGE - The waste of energy can be minimized. The degradation of the thermal conductivity can be prevented. The power generating efficiency of the system can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for power generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cogeneration system.    Brown gas formation unit (10)    Brown gas storage tank (20)    Igniter (30)    Combustion chamber (40)    Electricity storage unit (50)    Heat power plant (60)    AC power source converter (70)
NOVELTY - Invention refers to the method of gas separation during catalytic cracking of petroleum direction, which involves the main rectifying column with stillage part and circulation of quenching and removal of residue, which contains at least two circulation spraying devices and at least two steaming-stripping columns, from which distillates being the components of light and heavy gas oil are removed, and which is equipped with a sharp spraying device with outlet of unstable petroleum and fat gas to the gas fractioning part that includes a fractioning absorber having the heat supply to lower part and heat removal in upper part, a petroleum stabiliser having the stabilised agent outlet with partial return as an absorbent for spraying of the fractioning absorber, heat supply to lower part and sharp spraying with reflux outlet, absorber of amine cleaning of reflux from hydrogen sulphide with outlet of saturated amine that is regenerated from hydrogen sulphide in a proper regenerator having the heat supply to the still and outlet of acid gas, a column for separation of cleaned reflux into propane-propylene and butane-butylene fractions, which is equipped with a heater in the stillage part and sharp spraying device. At fractioning and separation of gases of catalytic cracking, heat distribution is optimised between cooled products of stillage residue and circulation sprays and heated flows of the system, which form heat supply to the bottom of the fractioning absorber, the stabilising column, the separation column of propane-propylene and butane-butylene fractions, regenerator of saturated amine, as well as partial heating of initial raw material.    USE - Oil and gas industry.    ADVANTAGE - Increasing the sampling of propylene and butylenes as merchantable products from propylene and butylenes, which were potentially formed during the cracking process, with simultaneous reduction of power consumption for the process implementation.3 cl, 2 dwg, 4 tbl, 4 ex
NOVELTY - Regeneration of waste hydrogen fuel using waste water-forming matter involves obtaining hydrogen fuel (water-forming matter) by using the phenomenon of spontaneous dispersion of aluminum and magnesium in molten alkali, where the spontaneous dispersion contains aluminum or aluminum-containing materials. Where the dispersion is formed by using spent water-forming substance, after appropriate processing, in the production of aluminum, as priming powder, and precipitating aluminum hydroxide from aluminate solutions.    USE - Regeneration of waste hydrogen fuel, used in internal combustion engines for hydrogen generation (claimed).
NOVELTY - Preparation of silkworm excrement compost mixed fertilizer, comprises stirring and uniformly mixing 80-89 wt.% silkworm excrement, 10-19 wt.% pig manure, 0.5-1 wt.% effective microorganisms (EM), stacking at 30-50 degrees C, natural fermenting for 15-18 days, drying and granulating to powder.    USE - Silkworm excrement compost used for improving fruit and vegetable taste quality (claimed).    ADVANTAGE - The silkworm excrement compost fertilizer improves the growth and development of fruits and vegetables, aides in the light absorption of plants, improves the central sugar and solid content of the fruits, has a wide market and industrial prospect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of the liquid fertilizer, comprising uniformly mixing and stirring 2.5-8 wt.% silkworm excrement, 1-6 wt.% pig manure, 0.2-1 wt.% raw lime, 85-96 wt.% water, boiling at 90-110 degrees C for 12-17 minutes, micro-boiling in mild fire for 35-45 minutes, filtering, diluting with water at a weight ratio of 1:10-20, and stirring; and    (2) application of silkworm excrement in fertilizing management, comprising applying prepared silkworm excrement compost on fruit and vegetable roots during the blooming and fruiting period, spraying liquid fertilizer 10-15 days after full bloom begins, and spraying once after 8-12 days.
NOVELTY - This utility model claims a special-shaped biomass gasification furnace of horizontal circulating fluidized bed furnace, comprising a fluidized bed, a gas distributor, a discharging pipe, an air inlet pipe, a feeding port, a primary gas-solid separator, a rough ash circulation returning pipe, material returning device, a gas-solid separator, silicon fertilizer outlet, gas outlet, fluidized bed is composed of a turbulent fluidized bed and bed reactor, the bottom turbulent fluidized bed is provided with a gas distributor and a discharging pipe, is equipped with a biomass feeding opening at the bottom of the reactor bed 100-2000 mm, the top part is provided with the first grade gas-solid separator and the secondary gas-solid separator, coarse particles of the first grade gas-solid separator the circulation return pipe by returning a special circulating fluidized bed at the bottom of the turbulent fluidized bed, high temperature the fine ash is a primary gas-solid separating device as outbound potash fertilizer from the fertilizer outlet, a gas from the gas outlet is used as product gas outwardly.
NOVELTY - Organic fertilizer comprises 10-15 pts. wt. straw, 20-25 pts. wt. waste fungus bud, 10-15 pts. wt. chicken manure, 10-15 pts. wt. swine manure and 30-40 pts. wt. cow manure and 5-10 pts. wt. active humic acid.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer accelerates soil nutrient mineralization, and is non-toxic.    DETAILED DESCRIPTION - Organic fertilizer comprises 10-15 pts. wt. straw, 20-25 pts. wt. waste fungus bud, 10-15 parts of chicken manure, 10-15 pts. wt. swine manure and 30-40 pts. wt. cow manure and 5-10 pts. wt. active humic acid. The active humic acid is extracted by taking 10% free humic acid or young lignite, pulverizing, passing through 60-200 mesh sieve, adding water at weight ratio of 1:5-15; continuously introducing air at 200-240 degrees C and atmospheric pressure, stirring at speed of 2000-3000 revolutions per minute for 4-8 hours; reacting for 5-19 hours at 70-175 degrees C and 5-6 atm; filtering precipitate through 60-100 mesh filter screen. An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing straw, waste fungus bud, chicken manure, pig manure and cow manure, mixing and stirring uniformly, fermenting for 25-30 days at normal temperature, mixing every 1-3 days, crushing completely fermented material into 60-100 mesh fine powder; adding active humic acid, mixing, stirring uniformly, conveying to granulating device, granulating, drying, cooling and sieving.
NOVELTY - The system has excrement treatment tank (10) whose bottom portion is provided with cross beam (11). The beam is provided with stirring device (7) having spiral stirring rod (9) whose upper end is provided with oil cylinder located along radial direction. One side of beam is equipped with feces pipe. The two ends of beam are provided with vertical sliding mechanism (4), and one side of tank is provided with liquid excrement groove (2). An air supply pipe (3) is provided with through holes. The tank is provided with feeding port and discharging port.    USE - System for processing excrement such as animal excrement in farm, human excrement, and organic matter in town refuse dump.    ADVANTAGE - The fermentation process of the excrement is easily performed at low cost. The occurrence of the environmental pollution is prevented, when the excrement is treated by performing aerobic fermentation with anaerobic biogas or filled strains.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for processing the excrement.    Liquid excrement groove (2)    Air supply pipe (3)    Vertical sliding mechanism (4)    Stirring device (7)    Spiral stirring rod (9)    Excrement treatment tank (10)    Cross beam (11)
NOVELTY - A nutritional meal fertilizer comprises 40-65 pts. wt. furfural residue, 20-30 pts. wt. animal manure, 25-30 pts. wt. plant ash, 20 pts. wt. biogas residue, 0.3-0.7 pt. wt. microbial compound bacteria, 3.5-6.5 pts. wt. microelements and 10-18 pts. wt. calcium ammonium nitrate. It is prepared by mixing all raw materials, stirring, adjusting pH to 6-7, fermenting and bagging.    USE - Nutritional meal fertilizer.    ADVANTAGE - The method is simple and has low production cost; has improved pest control and photosynthetic effect.
NOVELTY - Method for preparing foliar fertilizer from Chinese medicine herbs involves crushing 1.5-2.5 pts. wt. rhizoma coptidis, 2-3 pts. wt. Sophora flavescens, 2.5-3.5 pts. wt. Andrographis paniculata, 1.5-2.4 pts. wt. chinaberry seed, 1.5-2.5 pts. wt. radix stemonae and 2-3 pts. wt. common cnidium fruit, adding 0.1-0.3 pts. wt. bacterial composition to the crushed material and fermenting for 5-10 days, where the mixture is stirred 4 times daily and each stirring is carried out for 20-30 minutes.    USE - The method is useful for preparing foliar fertilizer from Chinese medicine herbs (claimed), which is useful for controlling diseases and killing insects.    ADVANTAGE - The method is simple and prepared fertilizer enables to increase yield and quality of agricultural product and produce good organic nuisanceless agricultural products and leaves no residue.
NOVELTY - This utility model claims a kind of widely used for continuously monitoring the concentration of methane and oxygen in the working environment under coal mine in flammable and combustible gas mixture of methane oxygen two parameters alarm. The electrochemical oxygen sensor (1) is set on the shell (16), the upper end of the ventilating window and through the filter screen is composed of a rotary cover (17) (18), digital display screen (2) is set on the shell (16) is set in the shell middle part, the touch switch (15) (16), circuit board (13) is set on the shell (16), a buzzer (9) and a heat catalyzing methane sensor (10) are respectively set on the shell (16) of the right end, and connected with a circuit board (13). Because the utility model adopts heat catalytic methane sensor and an electrochemical oxygen sensor, an intelligent control, a four-position LED display, a double-purpose, fast detecting speed, detecting a high accuracy, which greatly improves the working efficiency.
NOVELTY - The method involves performing biomass crushing operation to reduce diameter of a grain. Water content is pre-heated. A material is dried after crushing to obtain biomass powder. The biomass powder and coal powder are added into a gasification device. An amount of tar bio-carbon is calculated. A purifying device is utilized for purifying solid organic waste to make purified coal gas.    USE - Method for making total biomass and coal gas by utilizing solid organic waste.    ADVANTAGE - The method enables reducing pollution discharge of particulate matter and energy consumption and protecting an environment form being polluted.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for making total biomass and coal gas by utilizing solid organic waste.'(Drawing includes non-English language text)'
NOVELTY - The device has a cylindrical container (6) whose inner side is provided with an annular skirt plate (14). An upper part of an annular gas collecting cavity is filled with coal gas. A side wall of an output tube is connected with a container shell (5). A bottom part of the shell body is formed with a dust discharge hole. A bottom part of a container is connected with a cylindrical shell body that is formed with multiple air inlet holes (12A) or air inlet grooves (12B). An annular water sealing groove (4) is matched with a container cover.    USE - Wood coal gas production device.    ADVANTAGE - The device has high transmission distance, and reduces energy consumption rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a wood coal gas production device.    Annular water sealing groove (4)    Container shell (5)    Cylindrical container (6)    Air inlet holes (12A)    Air inlet grooves (12B)    Annular skirt plate (14)
NOVELTY - A bacterial composition comprises Bacillus having preservation number of CGMCC No.5971, Acinetobacter lwoffii having preservation number of CGMCC No.5973, and Wickerhamomyces anomalus having preservation number of CGMCC No.5975.    USE - In preparing cellulose additive ester film for optical use (claimed).    ADVANTAGE - The bacterial composition provides cellulose additive ester film using a method that convert waste liquid directly into organic fertilizer, does not pollute the environment, and save energy thus economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cellulose additive involving: providing bacterial liquid including Bacillus, Acinetobacter lwoffii and Wickerhamomyces anomalus according to weight ratio of 2-3:1 -2: 2-3; cutting woody raw material or herbal ingredients in slices and soaking in pool for swelling; and preparing fiber involving: crushing and grinding the swell raw material, soaking the raw materials in the bacterial liquid, and sterilizing to obtain biodegradable raw material, grinding the biodegradable raw material to make fiber, and soaking the prepared fiber in warm water, followed by drying, grinding and sterilizing to obtain cellulose additive.
NOVELTY - A composite biological flora comprises Bacillus species (CGMCC NO: 5971), Rheinheimera tangshanensis (CGMCC NO: 5972), Acinetobacter lwoffii (CGMCC NO: 5973), and Pseudomonas fluorescens (CGMCC NO: 5974).    USE - As a composite biological flora useful for producing cellulose additive, which is used in cellulose ester film for optical use (claimed).    ADVANTAGE - The composite biological flora forms cellulose additive by a process which does not pollute the environment; directly converts the waste liquid into organic fertilizer; realizes zero discharge and zero pollution; protects the fiber, compared with the traditional chemical method, has low production cost and high economic benefit, and is energy saving and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cellulose additive involving adding Bacillus species, Rheinheimera tangshanensis, Acinetobacter lwoffii and Pseudomonas fluorescens in water at a weight ratio of 2-3:1-2:1-2:1-2, cutting all materials into sections, soaking the cut materials into soaking pool for swelling, then crushing and grinding the materials, sterilizing the biodegradable raw material by putting it into bacterial liquid, then steam sterilizing, obtaining a fiber for the first time period from the sterilized raw material, grinding fiber bundle to make the fiber being separated into single fiber, then drying, and grinding; soaking the prepared fiber in warm water, followed by drying, sterilizing, and grinding; and putting the resultant fiber into cellulose, to obtain additive.
NOVELTY - Processing heavy metal contaminated soil repairing plant restoration material involves carrying out anaerobic fermentation of heavy metal contaminated soil repairing plant restoration material, and applying the fermented biogas fluid/slurry and biogas residue as fertilizer to nutrition element deficient soil.    USE - For processing heavy metal contaminated soil repairing plant restoration material, where the plant material is rapeseed, evening primrose, corn, or Chinese Mosla herb, the soil is contaminated with Clerodendrum trichotomum. The heavy metal element is copper or zinc (claimed). The biogas is used as foliage fertilizer, and feed additive.    ADVANTAGE - The method provides biogas residue that can be used as fertilizer applied to saline-alkali soil, and improves the growth of plant. The method provides economical and ecological benefits; improves soil quality; is environment-friendly, safe, and causes no pollution to the environment.
NOVELTY - The utility model claims a power equipment technology field, especially trimethoprim hydrogen oil increasing device, comprising an electrolytic water main box, a control circuit module, an electrolytic tank, a secondary filter, and the connecting air pipe, an electrolytic bath electrolytic water is set at the bottom of the main box, is connected with the input end of the air pipe is connected with the top of the electrolysis water main, is connected with the output end of the air pipe is connected with the top of the secondary filter is provided with a hydrogen-oxygen mixed gas to the gas output pipe of the engine and the secondary filter, the utility model by hydrogen ignition energy cost capable of improving a fuel ignition, add hydrogen combustion inherent propagation speed characteristic capable of faster flame propagation speed, the mixed gas in the cylinder more sufficient combustion, to improve the efficiency of the engine to realize the lifting engine power so as to effect and can reduce the discharge of energy-saving, and it can be applied to internal combustion engine is gasoline, diesel oil, natural gas and so on chemical fossil fuel as auxiliary energy saving improving system.
NOVELTY - This utility model claims a straw rod discharging channel, comprising a material channel, several supporting material conveying track of the supporting rod, the supporting rod of the base bottom is provided with material pressing tightly, simple structure, it is convenient to manufacture, stable structure and so on.
NOVELTY - This utility model claims a straw crushing machine, comprising a crusher, a drier, a second conveying belt and a crusher dryer is provided with high working efficiency, simple and convenient operation, high product percent of pass and so on.
NOVELTY - Microbial treatment of fish culture sewage by anoxic/oxic (A/O) biological contact oxidation method, comprises selecting Bacillus subtilis as flocculation strain; conducting strain activation and propagation with sterilized liquid culture medium, and dissolving lyophilized suspension in bacterial body; sterilizing to prepare bacterial suspension; inoculating bacterial suspension, and shaking to obtain fermentation culture medium; and purifying fish culture sewage to obtain clear liquid.    USE - Microbial treatment of fish culture sewage by anoxic/oxic bio-contact oxidation method.    ADVANTAGE - The method simplifies the process flow and reduces the process cost.    DETAILED DESCRIPTION - Microbial treatment of fish culture sewage by A/O biological contact oxidation method, comprises (A) selecting Bacillus subtilis as flocculation strain; (B) conducting strain activation and propagation with sterilized liquid culture medium in ampule, preserving dried frozen B. subtilis, and dissolving lyophilized suspension in bacterial body; (C) moving the bacterial suspension on flat plate culture medium and sterilizing at 30-32 degrees C for 36-48 hours, and carrying out same culture condition complete strain propagation at strain propagation normal method to prepare bacterial suspension; (C) inoculating bacterial suspension according to volume ratio of fish culture sewage and culture medium at 30 degrees C, shaking at 160 revolutions per minute (rpm) to obtain fermentation culture medium; and (D) purifying fish culture sewage to obtain centrifugal fermentation culture solution of clear liquid.
NOVELTY - Processing and recycling milk product wastewater comprises adding 16-2000 mg/L small molecular carbon source material and 55-1000 mg/L nitrogen source material to wastewater, adjusting pH value of wastewater to 7.0, then adding 24-2000 mg/L biogas swamp red Pseudomonas bacteria in wastewater, processing at 25-30 degrees C for 96-120 hours, controlling incandescent lamp as light source to 50-1500 lux light intensity, aerating the sewage, and controlling dissolved oxygen at 0.5-1.0 mg/L.    USE - Method of processing and recycling milk product wastewater.    ADVANTAGE - The method has simple and easy operation, simplifies the process flow, improves the sewage recycling degree, which avoids the secondary pollution problem of traditional sewage treatment process, and reduces the energy consumption.
NOVELTY - Biological tar collecting and comprehensive conversion utilization comprises collecting biomass and subjecting to pyrolysis, purifying and separating high-temperature gas mixture.    USE - Biological tar collecting and comprehensive conversion utilization method (claimed).    ADVANTAGE - The method is environment-friendly and solves the problem of carbon gasification technology process such as using agricultural waste and secondary pollution.
NOVELTY - The furnace has furnace cover (7) that is arranged on upper port of inner cylinder (1). The feed inlet (8) and air inlet (2) are located on furnace cover. A bottom portion of inner cylinder is connected to discharge hole (5). A fire grate (4) is mounted between inner cylinder and discharge hole. Several small air outlet holes (11) are evenly distributed on lateral side at lower portion of inner cylinder. An annular airway (12) is formed between outer cylinder (3) and inner cylinder. An air outlet pipe (6) is arranged on outer cylinder.    USE - Furnace for pyrolyzing agricultural waste, used in village factory. Uses include but are not limited to crop straw, tree trunk, branch, peel, root, waste wood, weed, mushroom dreg, furfural residue, vinegar residue, lees, fruit residue, excrement, biogas residue and biogas liquid of all kinds of animal etc.    ADVANTAGE - The pyrolyzing furnace can efficiently convert the agricultural waste into biological mixed gas or biomass carbon or a biological gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the agricultural waste pyrolyzing furnace.    Inner cylinder (1)    Air inlet (2)    Outer cylinder (3)    Fire grate (4)    Discharge hole (5)    Air outlet pipe (6)    Furnace cover (7)    Feed inlet (8)    Small air outlet hole (11)    Annular airway (12)
NOVELTY - Agricultural waste pyrolysis furnace comprises inner cylinder (1), outer cylinder (3), fire grate (4), discharge hole (5), air outlet pipe (6), furnace cover (7), feed port (8) and air inlet (2). The inner cylinder bottom is connected with discharge hole. The inner lower part is uniformly distributed with air outlet holes. The inner and outer cylinder forms annular air passage. The air outlet pipe is set on outer cylinder and connected with air channel. The furnace cover is cone-shaped, and distributing component is set in the cylinder.    USE - Agricultural waste pyrolysis furnace.    ADVANTAGE - The furnace transform efficiency is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of agricultural waste pyrolysis furnace,    Inner cylinder (1)    Air inlet (2)    Outer cylinder (3)    Fire grate (4)    Discharge hole (5)    Air outlet pipe (6)    Furnace cover (7)    Feed port (8)
NOVELTY - An agricultural biomass comprehensive transformation device comprises multifunctional biomass comprehensive transformation equipment, gas purification and separation equipment, liquid static separation equipment, gas purification equipment, biogas storage equipment, a hot water collection tank and a reservoir. The device can comprehensively transform biomass to five products including biogas, biological tar, charcoal, biological acetic acid and hot water.    USE - Agricultural biomass comprehensive transformation device (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of agricultural biomass comprehensive transformation device.
NOVELTY - Preparation of thermally cracking biomass into gas in a high-temperature and flash mode involves squeezing biomass to exhaust air, drying, performing volatile substance reaction, carrying out thermal cracking reaction, subjecting obtained biomass compound to secondary thermal cracking reaction, and converting energy elements in the biomass into gas.    USE - Preparation of thermally cracking biomass into gas in high-temperature and flash mode.    ADVANTAGE - The biomass is efficiently converted into high-grade energy products without generating dioxins. The amount of urban household garbage and discarded biomass is effectively reduced without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for thermal cracking device of biomass.
NOVELTY - Preparation of high density biomass fuel comprises crushing waste tobacco cigarette rods, waste tobacco stalks, and waste tobacco leaves to l-2 cm, 4-6 cm and 8-10 cm particle size, drying particles in hot-wind drying furnace to a moisture content of 7-16%, stirring and heating in a vessel at 65-96 degrees C, and subjecting to flat die molding machine.    USE - Method for preparing high density biomass fuel (claimed).    ADVANTAGE - The biomass fuel has no chemical additive, high density that can reach up to 1.2-1.4 g/cm3 density, and unit time that can reach 4 times as that of coal, and provides better heat capacity ratio than coal.
NOVELTY - Composite microbial inoculum comprises Phanerochete chrysosporium solution, Penicillium griseofulvum (Penicillium chrysogenum) fermenting liquid, onion Pseudomonas (Pseudomonas cepacia) fermenting solution and acetone-butanol Clostridium (Clostridium acetobutylicum) fermentation liquid.    USE - The composite microbial inoculum is useful for degrading organic impurities for producing biological coal bed gas such as methane in coal seam (claimed).    ADVANTAGE - The composite microbial inoculum has strong digestive capacity, and provides synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of composite microbial inoculum for degrading organic impurities for producing biological coal bed gas such as methane in coal seam.
NOVELTY - Pellet fuel of wood biomass comprises 80-90 pts. wt. wood chips, 6-12 pts. wt. residues left out after extraction of traditional Chinese medicine and 1-4 pts. wt. peanut shells.    USE - As pellet fuel of wood biomass.    ADVANTAGE - The pellet fuel has high combustion value, improved thermal value and significantly increased combustion rate and fuel efficiency, hence better compression ratio in the fuel is achieved, and simultaneously blackness of exhaust smoke is reduced below Ringelmann 1. The pellet fuel reduces abrasion of the cylinder and spiral shaft of machine, thus service life of the machine is prolonged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned pellet fuel, which involves (a) crushing the wood chips to obtain 0.5-1.8 mm sized wooden microparticles, (b) drying the wooden microparticles in rotating drum dryer until moisture content in the wooden microparticles reached 8% or less, (c) adding the above-mentioned residues and lubricant to obtained dried wooden microparticles, and stirring added materials uniformly to obtain mixture, (d) subjecting the mixture to extrusion and granulation process to obtain oily pellet fuel, where the pellet fuel has length of 2-3 cm, and diameter of 0.6-0.8 cm, and (e) cooling the pellet fuel inside cooling chamber for 30 minutes.
NOVELTY - This utility model is a garbage carbonization pyrolysis gasification device system without discharge of dioxin, comprising in turn connected with the mixed domestic garbage automatic comprehensive sorting device system, classifying and drying, storing and feeding device for feeding, pyrolysis and gasification furnace, a waste gas purifying device and a slag removing device, a waste water processing and recycling. The utility model uses a garbage treatment, and no discharge of dioxin, there is no waste water, no waste residue, no waste discharge, the harmless, full resource utilization, waste by waste, changing waste into recycling economy;
NOVELTY - The utility model claims a kind of pyrolysis to prepare bio-oil device, it is composed of a reaction kettle, a pressure gauge, an oil-water separator, a condensing pipe, a stirrer, a motor, an upper cover. The reaction kettle is equipped with an upper cover, a stirrer passes through the upper cover is inserted in the reaction kettle, a stirrer connected with the motor, a pressure gauge, an oil-water separator is set on the upper cover, an oil-water separator is connected with the condenser pipe. The product is simple in structure, rational in design, is set with vertical condensation and oil-water separating device can be directly obtained by oil-water separating, to obtain the target product, the volatile oil extractor connected to the vertical condensation reflux device, a condensing method is convenient and fast, it can reduce the loss of the target product, extracting rate is high.
NOVELTY - This utility model claims a biomass environmental-friendly civil honeycomb briquette, comprising a heating, porridge, fire and so on by more than one, the shape of the whole honeycomb briquette is cylindrical, the specific structure comprises the ignition layer, leading layer and the main body layer. Wherein the diameter of the circular surface of the honeycomb briquette heating at 90mm-100mm, and each of the cylindrical honeycomb briquette is provided with four burning holes, the aperture is 12mm-15mm. Porridge or circle diameter of the honeycomb briquette cooking for the 120mm-150mm, a number of a honeycomb briquette is set on the six combustion hole, the aperture is 18mm-25mm. Adopting the utility model provide a biomass environment-friendly honeycomb coal ignition not only fast, complete combustion, the combustion time is long, which effectively avoids fire waste, energy-saving and environment-friendly.
NOVELTY - This utility model claims a biomass carbon gas, continuous manufacturing system. The production system, comprising a gasification furnace, a gasification material supply device and fuel feeding device, gasification furnace is provided with a gasification chamber and a combustion chamber, the air outlet pipe is provided with the upper part of the gasification chamber, a cyclone separator is provided with the air outlet, wherein the production system further comprises a feeding port sealing of the vaporizing material feeding device for crusher and a material drying passage, material drying channel connected to the combustion chamber through the gas pipe with the material drying channel, it uses wood biomass raw material, orderly through the material crushing, drying, gasifying and collecting process, so as to realize the biomass gas and biomass carbon, continuous efficient production. This utility model can realize the biomass gas and biomass carbon is not continuous production and improves the production efficiency of the carbon, gas, increase in the unit time of the charcoal and gas yield, with higher economic value.
NOVELTY - Preparation of N-(2-pyrazine carbonyl)-L-phenylalanine-L-leucine boracic acid involves condensing sodium (2S)-3-phenyl-2-(pyrazin-2-ylformamido)propanoate with (1R)-3-methyl-1-((1S,2S,6R)-2,9,9-trimethyl-3,5-dioxa-4-boratricyclo(6.1.1.02,6)decan-4-yl)butan-1-amine compound under catalysis of O-benzotriazolyl-N,N,N',N'-tetramethyluronium tetrafluoroborate using dichloromethane, reacting obtained bortezomib pinanediol ester and butyl borate using methanol and normal hexane, removing piperazine alkyl diol protecting group under action of acid, recrystallizing and purifying.    USE - Preparation of N-(2-pyrazine carbonyl)-L-phenylalanine-L-leucine boracic acid (claimed).    ADVANTAGE - The N-(pyrazine carbonyl)-L-phenylalanine-L-leucine boracic acid having purity of more than 99% is prepared, with high productivity and reproducibility, and reduced generation of impurities and solvent dosage.    DETAILED DESCRIPTION - Preparation of N-(2-pyrazine carbonyl)-L-phenylalanine-L-leucine boracic acid involves condensing sodium (2S)-3-phenyl-2-(pyrazin-2-ylformamido)propanoate with (1R)-3-methyl-1-((1S,2S,6R)-2,9,9-trimethyl-3,5-dioxa-4-boratricyclo(6.1.1.02,6)decan-4-yl)butan-1-amine compound under catalysis of O-benzotriazolyl-N,N,N',N'-tetramethyluronium tetrafluoroborate using dichloromethane as solvent under protection of nitrogen at 0-10 degrees C with initial reaction temperature of -10 degrees C to 0 degrees C to obtain bortezomib pinanediol ester, reacting bortezomib pinanediol ester and butyl borate in molar ratio of 1:2-3 using methanol and normal hexane as solvent at -10 degrees C to 0 degrees C, removing piperazine alkyl diol protecting group under action of acid to obtain crude product, recrystallizing crude product using mixed solvent of ethyl acetate/organic acid and purifying recrystallized crude product. The organic acid is chosen from formic acid, acetic acid, oxalic acid and propionic acid.
NOVELTY - Transcritical power cycle mixed working medium comprises either difluoromethane and carbon dioxide, or difluoromethane and methane.    USE - Used as transcritical power cycle mixed working medium.    ADVANTAGE - The working medium: does not destroy the ozone sphere, hence ecofriendly; and has low greenhouse effect potential and excellent in circulating performance, preferably Rankine cycle efficiency of 6%, and net power output of greater than or equal to 9.8 kW.
NOVELTY - Co-pyrolyzed oil prepared by co-pyrolyzing lignocellulose biomass and waste printed circuit board as raw material at 300-800 degrees C under the vacuum condition, and condensing and collecting, is claimed.    USE - The co-pyrolyzed oil is useful for synthesizing phenolic resin with high mechanical performances and flame-retardant performance.    ADVANTAGE - The co-pyrolyzed oil: contains a large number of phenolic substances including phenol, 4-isopropylphenol and bisphenol A, which are relatively high in reactivity; contains bromo-phenolic substances which are relatively high in flame retardant performance; and greatly reduces synthesis cost of phenolic resin with high mechanical performances and flame-retardant performance without the addition of phenol, flame retardant and plasticizers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the co-pyrolyzed oil, comprising co-pyrolyzing lignocellulose biomass and waste printed circuit board as raw material at 300-800 degrees C under the vacuum condition, and condensing and collecting at -40 degrees C to 0 degrees C.
NOVELTY - A slagging system for biogas production, comprises a discharging tank and where the discharging tank is internally provided with a slagging pipe and a biogas slurry discharging pipe; the slagging pipe and the biogas slurry discharging pipe are connected and communicated with the inlet end of a discharging motor; the slagging system is also provided with an organic biogas slurry pipe communicated with a farmland, a feeding circulating pipe communicated with a feeding tank and a slagging filter tank pipe communicated with a liquid and slag separating tank.    USE - Slagging system for biogas production (claimed).    ADVANTAGE - The slagging system for biogas production has the effect of maximizing the comprehensive utilization of biogas, biogas slurry and biogas slag through respectively taking the biogas slurry and the biogas slag produced in the biogas production process away from the discharging tank through different pipelines.    DETAILED DESCRIPTION - A slagging system for biogas production, comprises a discharging tank and where the discharging tank is internally provided with a slagging pipe and a biogas slurry discharging pipe; the slagging pipe and the biogas slurry discharging pipe are connected and communicated with the inlet end of a discharging motor; the slagging system is also provided with an organic biogas slurry pipe communicated with a farmland, a feeding circulating pipe communicated with a feeding tank and a slagging filter tank pipe communicated with a liquid and slag separating tank; and the organic biogas slurry pipe communicated with the farmland, the feeding circulating pipe communicated with the feeding tank and the slagging filter tank pipe communicated with the liquid and slag separating tank are communicated with the outlet end of the discharging motor.
NOVELTY - Comprehensive utilization of lignocellulosic biomass, comprises processing lignocellulosic biomass with alkali solution, performing acid hydrolysis process of resulting alkaline hydrolysis residue and separating to obtain pentose solution and acid hydrolysis residue, carrying out enzymolysis of acid hydrolysis residue with cellulase to obtain glucose solution and enzymolysis residue, returning enzymolysis residue to acid hydrolysis treatment or combining enzymolysis residue and fresh alkaline hydrolysis residue and carrying out acid hydrolysis treatment, and repeatedly circulating.    USE - The method is useful for comprehensive utilization of lignocellulosic biomass (claimed).    ADVANTAGE - The method improves the conversion rate of cellulose enzymatic hydrolysis to achieve comprehensive utilization of lignocellulose biomass resources.    DETAILED DESCRIPTION - Comprehensive utilization of lignocellulosic biomass, comprises: (a) processing lignocellulosic biomass with alkali solution to extract lignin; (b) performing acid hydrolysis process of the resulting alkaline hydrolysis residue, and separating to obtain pentose solution and acid hydrolysis residue; (c) carrying out enzymolysis of the acid hydrolysis residue with cellulase to obtain glucose solution and enzymolysis residue, where the cellulase is obtained by culturing Penicillium decumbens PD-G3-08 with CCTCC M 2011195 preservation number; and (d) returning the enzymolysis residue to the step (b) acid hydrolysis treatment or combining the enzymolysis residue and fresh alkaline hydrolysis residue and carrying out the step (b) acid hydrolysis treatment, and then sequentially carrying out the steps (c) and (d), and repeatedly circulating to further convert hemicellulose into pentose, and cellulose to glucose by enzymolysis.
NOVELTY - Lignocellulosic biomass is processed by carrying out acid hydrolysis of lignocellulosic biomass to obtain pentose solution and acid hydrolysis residue, treating acid hydrolysis residue with alkali solution to extract alkali lignin, using cellulase to perform enzymolysis of hydrolysis residue and obtain glucose solution and enzymolysis residue, and repeating alkali solution treatment and enzymolysis steps to further extract lignin.    USE - Method of processing lignocellulosic biomass for ethanol production.    ADVANTAGE - Generation of furfural and acetic acid is prevented, hemicellulose is easily removed, extraction rate of cellulose is improved, and damage to lignin and cellulose is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the method of processing lignocellulosic biomass. (Drawing includes non-English language text).
NOVELTY - Method for comprehensively utilizing lignocellulose biomass involves subjecting the lignocellulose biomass to acid hydrolysis, using cellulase for enzymolysis of the acid hydrolytic residues, obtaining the cellulose through culturing Penicillium, using aqueous alkali to treat enzymatic residues, and subjecting the alkaline hydrolytic residues to enzymolysis again or alkaline hydrolytic residues to obtain acid hydrolytic residues and then subjecting to enzymolysis, repeating the operations, and extracting lignin and carrying out cellulose enzymolysis.    USE - The method is useful for comprehensively utilizing lignocellulose biomass (claimed).    DETAILED DESCRIPTION - Method for comprehensively utilizing lignocellulose biomass involves (a) subjecting the lignocellulose biomass to acid hydrolysis to obtain pentose solution and acid hydrolytic residues, (b) using cellulase for enzymolysis of the acid hydrolytic residues, such that glucose solution and enzymatic residues are obtained, obtaining the cellulose through culturing Penicillium, where the Penicillium is P.decumbens PD-G3-08 (CCTCC M 2011195), (c) using aqueous alkali to treat enzymatic residues such that to extract lignin in the enzymatic residues and obtain alkaline hydrolytic residues, and (d) subjecting the alkaline hydrolytic residues to enzymolysis again or alkaline hydrolytic residues to obtain acid hydrolytic residues and then subjecting to enzymolysis, carrying out steps (c) and (d) sequentially, repeating the operations, and extracting lignin and carrying out cellulose enzymolysis.
NOVELTY - Improving comprehensive utilization of lignocellulosic biomass, comprises preparing acid solution and adding into a first acid hydrolysis reaction kettle, discharging the acid solution in a second grade acid hydrolysis reaction kettle, followed by discharging the acid solution in a third level hydrolyzing reaction kettle and into a N-level hydrolyzing reaction kettle, and discharging the acid solution as the final pentose solution and then heating the acid hydrolysis residue with a wood cellulose biomass raw material, and continuously carrying out hydrolysis reaction.    USE - The method is useful for improving comprehensive utilization of lignocellulosic biomass (claimed).    ADVANTAGE - The method allows improvement of comprehensive utilization of lignocellulosic biomass thus maintaining the activity of lignin.    DETAILED DESCRIPTION - Improving comprehensive utilization of lignocellulosic biomass by deprocessing and N-stage acid hydrolysis, comprises preparing acid solution and adding into a first acid hydrolysis reaction kettle, discharging the acid solution in a second grade acid hydrolysis reaction kettle, followed by discharging the acid solution in a third level hydrolyzing reaction kettle and into a N-level hydrolyzing reaction kettle, discharging the acid solution as the final pentose solution and then taking out the acid hydrolysis residue and introducing into a first grade acid hydrolysis reactor and then heating with a wood cellulose biomass raw material, and continuously carrying out hydrolysis reaction of the lignocellulosic biomass, where N is greater than 2.
NOVELTY - This utility model claims a combustion device manufacturing technology field, especially relates to a kind of new type biomass gasification furnace pressure device. The pressing device is composed of a smoke cover (1), a sealing ring 2, a wind cover (3), a feeding furnace port (4), an air outlet 5, a connecting rod 6, wherein the pressure smoke cover (1) and a wind cover (3) by connecting rod (6) is rigidly connected with the inner sealing ring 2 is set in the annular groove of the air cover (3), a feeding furnace port 4 one side of air outlet 5, air cover (3) is furnace feeding port (4), a sealing ring (2). Compared with the existing technology, the sealing performance of the smoke better, and biomass fuel is more convenient to use.
NOVELTY - This utility model claims a kind of organic plant purifying granules, comprising a plant purifying isotope core and coated on the plant purifying isotope core on a sustained-release coating, the utility model has reasonable structure design, smart design, is coated with a sustained-release coating outside of the plant purifying isotope core, the plant purifying isotope core can have enough time to be absorbed by the plant, and a sustained-release coating can prevent the plant purifying isotope core applying is damaged to failure and watering in the process, which can greatly increase the medical effect of the product, it can activate microorganism capable of degrading different types of agricultural chemical recessive functional gene, fast degrade the fertilizer farm chemical metal residue in agricultural product and can be quickly set up a predominant bacteria, soil structure, which not only can realize the soil, water quality, environment pollution of the plant purifying, but also gets rid of the dependence on the agricultural chemical, it can be widely used for all kinds of grain crop, vegetable, fruit, cash crop and so on, which is good for wide popularization and application.
NOVELTY - Field using the utility model belongs to biomass energy, specifically to a biomass pyrolysis multi-joint device, comprising a hopper, a feeding system, a crawler-type pyrolysis reactor, a gas-solid separation system, pyrolysis gas condensing system, a gas burner, a gas heat exchanger, a coke grinder, cooling and discharging system, wherein the crawler-type pyrolysis reactor is composed of a steel track, a transmission shaft, a drive control system, a sealing reaction chamber and heat storage body. Biomass raw material into the crawler-type pyrolysis reactor via a hopper and feeding system, the pyrolysis reaction in the process of running the steel track, pyrolysis gas to obtain the liquid product and a gas is condensed after solid coke by crushing and cooling. This device for biomass pyrolysis in the process of generating a gas as heat source for supplying the heat needed by said dealkylation reaction pyrolysis so as to realize self pyrolysis process of the heat, and joint solid coke and liquid product.
NOVELTY - This utility model claims a crop fertilizer, comprising a marsh gas tank (1), wherein the marsh gas tank (1) is provided with a pre-processing tank (2), a methane tank (1) is connected with the marsh gas washing device (3), a methane tank (1) is provided with a biogas slurry extraction opening (4). This utility model using biogas slurry scouring device, the marsh gas pool is more convenient to feed, and it will not influence the concentration in the marsh gas tank, does not affect the daily use of the objective, in addition it can periodically stir the biogas slurry in the marsh gas tank and the raw material to remove the dead angle in the marsh gas tank, improve the utilization of the marsh gas tank.
NOVELTY - Waste-derived biomass resources are simultaneously saccharified and fermented by mixing waste-derived biomass resources e.g. papers, garbage, grass, and trees in reaction tank and simultaneously performing fermentation which assimilates saccharides from biomass resources in the presence of microorganisms and saccharification which hydrolyzes saccharides in the presence of enzyme.    USE - Simultaneous saccharification and fermentation of waste-derived biomass resources for manufacture of ethanol.    ADVANTAGE - Electric power consumption can be reduced, high concentration of biomass resources can be processed, and efficiency of reaction is improved.
NOVELTY - Organic wastewater and organic waste are processed by separating organic wastewater into solid and liquid, performing biological nitrogen process on solid-liquid separated wastewater to obtain surplus sludge, performing methane fermentation treatment of surplus sludge, performing gas-liquid contact of biogas obtained by methane fermentation treatment to aqueous medium, dissolving methane gas in biogas in aqueous medium, and supplying aqueous medium containing dissolved methane to denitrifying process as hydrogen donation source.    USE - Processing method of organic wastewater and organic waste, such as sewage, foodstuff waste material, and livestock farming waste material.    ADVANTAGE - Biogas emitted when denitrifying reaction can be promoted sufficiently, and methane fermentation treatment is carried out effectively. Methane gas concentration in biogas can be raised to contribute to effective usage of biogas by performing gas liquid contact of aqueous medium and biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the processing method of organic wastewater and organic waste. (Drawing includes non-English language text).
NOVELTY - Aluminum magnesium complex oxide is manufactured by mixing magnesium salt powder, aluminum salt powder, and alkali metal salt powder without heating and mixing powder of alkali chemicals with obtained mixture without heating.    USE - Manufacture of aluminum magnesium complex oxide for metal-supported catalyst used for carbon dioxide reforming of methane (claimed).    ADVANTAGE - Catalyst has excellent activity, long-term stability, and caulking resistance and is manufactured efficiently at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of metal-supported catalyst which involves making metal salt aqueous solution impregnate aluminum magnesium complex oxide and calcining.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the X-ray diffraction pattern of nickel/magnesium aluminate catalyst. (Drawing includes non-English language text).
NOVELTY - The furnace has a water jacket (3) being adjacent to a housing (1) and surrounding a process chamber (7), where a part of space of the water jacket is separated from a steam chamber (5) and remaining part acts as a heat exchanger (4) with coolant inlet and outlet (2). The process chamber is provided with a connector pipe (17) for injecting process gas and air dosing. A top part of the housing is closed with a lid (6) on which a magnetron (10) is arranged, and a bottom part is closed with a flap (13) in which an outlet (8) for liquid products obtained from a gasification process is arranged.    USE - Furnace for microwave gasification of biomass/gaseous/liquid products or substances to produce/extract combustible fuel/carbon oxide or coke gas and domestic hot water in households/industrial plants.    ADVANTAGE - The furnace uses a microwave generator to carry out gasification of products and substances that are subjected to gasification or oxygen-free degasification utilizing small amounts of oxygen or other gas depending on feedstock characteristics and requirements of the products. The furnace can be utilized for coke gasification to produce high-quality coke gas through use of the steam chamber, and temperature and process efficiency of the furnace can be controlled by reducing power of microwaves.    DETAILED DESCRIPTION - The housing is metal housing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a microwave gasification furnace.    Housing (1)    Coolant inlet and outlet (2)    Water jacket (3)    Heat exchanger (4)    Steam chamber (5)    Lid (6)    Process chamber (7)    Outlet (8)    Magnetron (10)    Flap (13)    Connector pipes (16, 17)
NOVELTY - Producing cassava alcohol involves subjecting alcohol production system to energy optimization improvement step including steaming liquefied mash section to distillation recycling and waste heat recovery.    USE - For producing cassava alcohol (claimed).    ADVANTAGE - The method uses waste heat from boiler thereby saving energy, saves electricity charge expenditure capital, uses variable frequency speed regulation motor system thereby saving energy, increases marsh gas amount, saves electric energy consumption, and allows clean production of alcohol.
NOVELTY - Promoting hydrolysis lignocellulose involves pre-treating lignocellulose raw material, adding water and mixing uniformly is configured to lignocellulosic substrate; adding metal ion solution, where the metal ion is selected from nickel ion, cobalt ion, magnesium ion, zinc ion and/or manganese ion; adding cellulase or hemicellulase to the substrate, carrying out hydrolyzing and saccharifying at pH of 4-7.5, at 30-80 degrees C under the condition for 12-120 hours to obtain glucose or sugar solution by filtration, and centrifugation.    USE - For promoting hydrolysis lignocellulose (claimed) which is applied to the wood cellulose hydrolysis process and biomass energy production and development field.    ADVANTAGE - The method is featured with simple operation; recycles metal ions; has low investment cost, wide using range and no pollution; and improves the cellulose hydrolysis efficiency.    DETAILED DESCRIPTION - Promoting hydrolysis lignocellulose involves pre-treating lignocellulose raw material, adding water and mixing uniformly is configured to lignocellulosic substrate; adding metal ion solution, where the metal ion is selected from nickel ion, cobalt ion, magnesium ion, zinc ion and/or manganese ion; adding cellulase or hemicellulase to the lignocellulosic substrate, carrying out hydrolyzing and saccharifying at pH of 4-7.5, at 30-80 degrees C under the condition for 12-120 hours to obtain glucose or sugar solution by filtration, and centrifugation, hydrolyzing and saccharifying process in batches, adding water in the hydrolyzing system metal ion concentration is 10 mM. The pre-treatment step involves grinding, ball milling, acid treatment, alkali treatment, heat treatment, stewing, steam explosion pulping or papermaking.
NOVELTY - This utility model claims a device for manufacturing liquefied natural gas, a manufacturing device of coke oven as main raw material is liquefied natural gas, comprising a gas purification unit, a methanation unit and liquefaction unit, and, further comprising a compression unit, wherein the gas inlet pressure of gas purification unit is disposed in the methanation unit is controlled to be 1.0 to 2.0MPaG, the increase is more than 3MPaG by the pressure of the synthesis gas after the methanation unit. According to the utility model can reduce the power consumption of the compressor. And it can reduce the operation pressure of the desulfurizing technique steps of the gas purification unit, obviously inhibit and process steps in the methanation, can solve the problem caused by the abnormal heating caused by methanation reaction, so it does not need take so as to dilute raw material gas or a cooling device through a gas after the desulphurization and so on;
NOVELTY - Extraction of vernine comprises adjusting pH of guanosine fermenting liquid to 10.5-12, processing micro-filtration, and further filtering micro-filtration filtering liquid to obtain ultra-filtration filtrate and ultra-filtration trapped fluid; concentrating ultra-filtration filtrate, adjusting pH to 6.8-7.5, cooling and crystallizing, filtering, dissolving filter cake by alkali solution, and ultra-filtering; and adjusting pH, cooling, crystallizing, filtering, dissolving filter cake, discoloring, filtering, cooling, crystallizing and filtering, and drying.    USE - Method for extracting of vernine used for bacteria protein feed and compound fertilizer (claimed).    DETAILED DESCRIPTION - Extraction of vernine comprises adjusting pH of guanosine fermenting liquid to 10.5-12, processing micro-filtration, obtaining micro-filtration filtering liquid and micro-filtration trapped fluid, and further filtering micro-filtration filtering liquid to obtain ultra-filtration filtrate and ultra-filtration trapped fluid; concentrating ultra-filtration filtrate to obtain concentrated solution to original volume of 25-50%, adjusting pH to 6.8-7.5, cooling and crystallizing, filtering to obtain filter cake and mother liquor, dissolving filter cake by alkali solution, and ultra-filtering; and adjusting pH of concentrated solution to 6.8-7.5, cooling, crystallizing, filtering to obtain filter cake and mother liquor, dissolving second filter cake, discoloring, filtering, cooling, crystallizing and filtering to obtain filter cake and mother liquor, and drying filter cake to obtain guanosine.
NOVELTY - Preparation of monodisperse hydrophobic medicine nanoparticles by template method comprises preparing anodic aluminum oxide (AAO) template by anodic oxidation method, modifying the surface properties of template by amphipathic solvent, putting the modified template on anticancer medicine solution, preparing medicament under normal pressure or reduced pressure condition, removing the template by acid or alkali, and cleaning to obtain monodisperse hydrophobic medicine nanoparticles.    USE - Preparation of monodisperse hydrophobic medicine nanoparticles by template method (claimed) useful for cancer diagnosis and treatment field.    ADVANTAGE - The method has simple operation, low cost, high yield, adjustable pharmaceutical components, and no environmental pollution, and provides product with controllable appearance, small size, narrow grain diameter distribution, and high drug loading capacity.
NOVELTY - Usage method of household garbage involves carrying out crushing, separating, dehydrating and burning household garbage continuously, carrying out themolyzis on separated light garbage materials e.g. waste plastics to prepare fuel oil and/or fuel gas products, and carrying out purifying standardization processing and discharging on waste water discharged by a dehydrator.    USE - Usage method of household garbage (claimed).    ADVANTAGE - The method is carried out efficiently and economically.
NOVELTY - One-step preparation of phenyl acetate from acetophenone comprises reacting metallic copper complex as catalyst and hydrogen peroxide as oxidant in solvent at ratio of 0.1:1-4:110-150 at 20-70 degrees C and atmospheric pressure to generate active components, adding acetophenone at acetophenone to metallic copper complex ratio of 15:0.1-0.3, stirring and reacting for 0.5-8 hours, distilling solvent and collecting phenyl acetate at 190-195 degrees C, where the solvent is acetonitrile, 1,4-dioxane, formic acid, acetic acid, butyric acid or dimethyl sulfoxide.    USE - One-step preparation of phenyl acetate from acetophenone (claimed).    ADVANTAGE - The environment-friendly and feasible method has high yield, conversion and selectivity reaching to 100%. It also has mild reaction condition, simple preparation of catalyst and low-cost and easy-to-obtain raw materials.
NOVELTY - Preparation of heme comprises mixing hematocrit with water, removing cell membrane by centrifugation, stirring, filtering, mixing and/or stirring, adding sodium carboxymethyl cellulose or sodium carboxymethyl starch, stirring and precipitating.    USE - The heme is used for foods, pharmaceuticals or feed compositions (claimed).    ADVANTAGE - The catalyst solves problem of easy oxidation and decomposition, low intensity, low efficiency, and rigorous reaction condition. The the production process of heme is environment-friendly without pollution.
NOVELTY - A heavy degree alkaline soil modifying agent comprises 88-92 pts. wt. desulfurization waste, 1-3 pts. wt. inorganic accelerator, and 5-11 pts. wt. organic accelerator.    USE - Heavy degree alkaline soil modifying agent.    ADVANTAGE - The soil modifying agent is suitable for use on soil having pH value of more than 8.7, alkalinity of 20-30%, and salt content of less than 0.5%. It utilizes desulfurization waste as calcium ion replacement for reducing soil alkalinity and also utilizes organic accelerator having fine pore structure to improve structure and physical properties of the soil, reduce pH value of the soil, and increase soil fertility. Further, the inorganic accelerator can improve soil granule structure, and the auxiliary inorganic fertilizer and organic fertilizer are capable of improving soil fertility and providing nutrition composition for the growth of crops. Thus, the soil modifying agent can effectively overcome soil nutrient imbalance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the heavy degree alkaline soil modifying agent, comprising mixing raw materials and pelletizing to obtain the soil modifying agent.
NOVELTY - A moderately alkaline soil modifying agent comprises 80-90 pts. wt. desulfurization waste, 3-5 pts. wt. inorganic accelerator, and 8-15 pts. wt. organic accelerator.    USE - Moderately alkaline soil modifying agent.    ADVANTAGE - The soil modifying agent is suitable for use on soil having pH value of more than 8.6, alkalinity of 10-20%, and salt content of less than 0.5%. It utilizes desulfurization waste as calcium ion replacement for reducing soil alkalinity and also utilizes organic accelerator having fine pore structure to improve structure and physical properties of the soil, reduce pH value of the soil, and increase soil fertility. Further, the inorganic accelerator can improve soil granule structure, and the auxiliary inorganic fertilizer and organic fertilizer are capable of improving soil fertility and providing nutrition composition for the growth of crops. Thus, the soil modifying agent can effectively overcome soil nutrient unbalance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the soil modifying agent, comprising mixing raw materials and pelletizing to obtain the soil modifying agent.
NOVELTY - A synthesis gas preparation method involves dividing water gas as raw materials into streams (1, 2, 3) and feeding the stream (2) into a carbon monoxide conversion device to enable the water gas to be converted into a stream (4) containing carbon dioxide and hydrogen, where the volume of the stream (3) is 10-95% of the total volume of the raw materials. The streams (3, 4) are fed into an acid gas washing device to remove sulfide and partial carbon dioxide, and mixing the washed stream with a stream (5) containing hydrogen to obtain the synthesis gas.    USE - Method for preparing a synthesis gas that is utilized for synthesizing methanol.    ADVANTAGE - The method enables solving the problem that the ratio of hydrogen-carbon dioxide/carbon monoxide-carbon dioxide in the synthesis gas produced from a carbon monoxide conversion device cannot meet the methanol production demand.    DETAILED DESCRIPTION - A synthesis gas preparation method involves dividing water gas as raw materials into streams (1, 2, 3) and feeding the stream (2) into a carbon monoxide conversion device to enable the water gas to be converted into a stream (4) containing carbon dioxide and hydrogen, where the volume of the stream (3) is 10-95% of the total volume of the raw materials. The streams (3, 4) are fed into an acid gas washing device to remove sulfide and partial carbon dioxide, and mixing the washed stream with a stream (5) containing hydrogen to obtain the synthesis gas, where the removal rate of the carbon dioxide in the acid gas washing device is 80-99% and the volume of the added stream (5) is 5-40% of the total volume of the raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing a synthesis gas.    Streams (1-5)
NOVELTY - Preparing organic fertilizer, by mixing effective microorganism (EM) bacteria with brown sugar water, sealing and fermenting to obtain viscous EM bacterial liquid, mixing bacterial liquid with the brown sugar liquid, adding rice bran, sealing and fermenting to obtain fermentation agent, adding calcium superphosphate, boron fertilizer, chelated iron and fermentation agent, stirring and stacking mixture, and covering and performing fermentation.    USE - The method is useful for preparing organic fertilizer using waste branches and leaves of cut flowers (claimed).    ADVANTAGE - The method is environmentally-friendly, as the method enables to recycle wastes of the cut flowers, produces no pollution and solves the problem that several waste branches and leaves of the cut flowers are difficult to recycle. The fertilizer improves soil quality and yield of crops.    DETAILED DESCRIPTION - Method for preparing organic fertilizer using waste branches and leaves of cut flowers, involves mixing effective microorganism (EM) bacteria with brown sugar water (8-12%) in the mass ratio of 1:80-120, sealing the mixture, fermenting at 20-25 degrees C for 10-15 days to obtain viscous EM bacterial liquid, mixing the EM bacterial liquid with the brown sugar liquid (3-8%) in the ratio of 1:80-120, adding rice bran, sealing the mixture, fermenting at 25-30 degrees C for 6-16 days to obtain a fermentation agent, adding 15-25 kg calcium superphosphate, 0.15-0.25 kg boron fertilizer, 0.8-0.12 kg chelated iron and 3-4 kg fermentation agent into each ton of crushed waste branches and leaves of the cut flowers, uniformly stirring and stacking the mixture, hermetically covering the mixture using plastic films, and performing fermentation at normal temperature to obtain the organic fertilizer.
NOVELTY - Seedling growing matrix comprises vinegar residue, vermiculite, peat, plant ash, perlite and small amount of inorganic fertilizers.    USE - The seedling growing matrix is useful for melons (claimed).    ADVANTAGE - The seedling growing matrix is cost-effective, light in mass and complete in nutrition, and excellent in soilless culture of gardening plants.
NOVELTY - Organic fertilizer is prepared by performing continuous fermentation, granulation, drying and screening on plant ash, industrial and agricultural waste enriched with organic matter, and inorganic fertilizer, inoculating bacteria to the obtained screened raw materials, and subjecting the inoculated raw materials for breeding process.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is environmentally-friendly, and enables to solve problem of soil hardening, and gradual fertilizer efficiency reduction during crop cultivation and urban greening process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer which involves (a) uniformly mixing the industrial and agricultural waste, (b) stacking the mixture at 65-75 degrees C, where the water content of the stacked mixture is 67-70%, and the pH of the mixture is 8-9, turning the stacked mixture for every 2-4 days, and reducing the temperature of the stacked mixture to 40-50 degrees C and the pH of the mixture to 6.5-6.9 to complete the composting process, and (c) drying and sieving the obtained mixture, and adding strain liquid to the sieved mixture, where the number of viable strain in the obtained product is 0.20-0.65 billion/g.
NOVELTY - Integration method for developing high efficient organic crop, involves using carbon bio-organic fertilizer, adopting promotion and popularization of microbial fertilizer as nuclear technical product, selecting high quality plant growth regulator to control the crop growth, using auxiliary fertilizer source to supplement and balance the crop nutrition, selecting soil fertility and improved technical products and several plant protective products, and selecting other several advanced field planting and management technical measures and methods.    USE - Integration method for developing high efficient organic crop (claimed).    ADVANTAGE - The method is suitable for crops including cotton, oil, tea, and other field crops, and polluted land, and desertified soils. The oraganic crop is of high quality and high yield, and cost-effective.    DETAILED DESCRIPTION - Integration method for developing high efficient organic crop, involves using carbon bio-organic fertilizer as foundation fertilizer source, adopting promotion and popularization of microbial fertilizer as nuclear technical product, selecting high quality plant growth regulator to control the crop growth, using auxiliary fertilizer source to supplement and balance the crop nutrition, selecting soil fertility and improved technical products and several plant protective products, and selecting other several advanced field planting and management technical measures and methods.
NOVELTY - Preparation of biomass briquette comprises crushing crop straw and mixing slurry, molding by extrusion, mixing furfural residue, crushed straw and slime in ratio of 9:6:10-32:8:10, adding calcined lime and industrial caustic soda which is 1-2% of total mass of raw materials.    USE - Method for preparing biomass briquette (claimed).    ADVANTAGE - The method solves low heat efficiency of direct combustion of furfural residue and crushed crop straw, increases combustion efficiency and solves problem of smoke. The method has low energy consumption, low cost, and no pollution; and the product is capable of replacing fuels such as raw coal, petroleum liquefied gas, natural gas and firewood and can be applicable in stoves and boilers.
NOVELTY - A gear-type biomass fuel pressing machine comprises ring mold (1) assembled on pressing roller (3). The ring mold has multiple inner gear teeth (2) and outer gear teeth (4) along the radial direction of through-holes (5).    USE - Gear-type biomass fuel pressing machine.    ADVANTAGE - The machine has good material-feeding performance, stable working condition, low failure rate, high production efficiency, regular grain-shaped biomass extrusion, compact structure and reduces idle rate and power consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of gear-type biomass fuel pressing machine.    Ring mold (1)    Inner gear teeth (2)    Pressing roller (3)    Outer gear teeth (4)    Through-hole (5)
NOVELTY - This utility model belongs to marsh gas technology field, claims a method for realizing constant temperature, has high glass fibre reinforced plastic marsh gas generation tank. The main technical solution is that the rotating shaft provided with a digestion tank body, wherein the tank body is driven by the power mechanism and a stirring mechanism is fixed on the rotating shaft of the blade is set on the tank body of the heating mechanism, a temperature sensing mechanism and a control terminal for controlling a temperature, a temperature sensing mechanism and a stirring mechanism, wherein the digestion tank structure from inside to outside in turn a layer of glass steel, heating mechanism is set on the inner lining layer, cooling mechanism and a temperature sensing mechanism and the outer side of the glass fibre reinforced plastics structure layer and the glass steel outer surface layer, composed of sensor through the temperature sensing mechanism lining to the biogas liquid in the tank body. The marsh gas generating tank can ensure the temperature at the air outlet is in the range, so as to guarantee the normal production of methane bacteria, which greatly improves the production efficiency of the marsh gas, at the same time, is provided with corrosion resistance, long service life.
NOVELTY - A kind of garbage processing industry a new technique of aerobic composting movable chamber, which can effectively reduce the floor space and investment, solves the odour pollution. It is to each fermenter top aerobic fermentation, two ends of door, sealing, the whole cover is formed by a plurality of sealing film is divided into left and right two parts, the fixing is less than the fermentation groove in the side wall, and the width of the left and right two parts cover the fermentation groove by half of the width of the steel structure, the middle joint by adding high-elasticity rubber plate, the front cover and the two ends of the last sealing a push pull the movable type is set with the slide rail. A sealing gasket for closure capable of effectively absorbing solar energy to improve the fermentation temperature, but also capable of blocking the air of nitrogen-oxygen molecule greater than the odour molecules to make it not can volatilize to outside environment passes through the sealing film, the structure of the movable chamber.
NOVELTY - A kind of rural environment-friendly high-efficient marsh gas pool, relating to the field of marsh gas tank, which is composed of a feeding port, the main fermentation tank, flow layer, slag discharge hole, discharge hole, solid-liquid separation layer, a fermenting tank, a marsh gas film, a water pressure device, wherein the main fermentation tank is connected with the fermenting tank, solid-liquid separating layer is set on the main body of fermentation tank and fermentation tank, a feed port and a biogas residue discharging opening are respectively connected with the main fermentation pool, a water pressure device is set on the fermentation tank, fermentation tank and biogas liquid discharge is connected with the flow layer covering the main fermentation tank and fermentation tank, the water pressure device is composed of a small hole, a pressure tank, a water pressure pipe on the main fermentation tank and fermentation tank, a marsh gas, the utility model is capable of processing rural residents life garbage and human manure, rural household garbage solves the environment pollution and the marsh gas pool gas is low.
NOVELTY - Spheroidal glass steel is horizontal ellipsoid with the marsh gas tank, the tank is made of glass steel, the top part of the ellipsoid is provided with skylight, the skylight is provided with a gas guide pipe. Using fermentation principle to generate marsh gas, which not only change waste into valuable stuff, but also is convenient for the user to use, management, transportation, high production efficiency, biogas, biogas residue as cultivation and planting of the raw material.
NOVELTY - A kind of device for generating synthesized gas by biomass, device for generating synthesized gas comprises a combustion furnace, a cracking furnace, a burning furnace wall of the furnace is set on at least one part of cracking furnace or burning furnace and containing a common part furnace wall, a burning furnace, a cracking furnace is relatively independent, in the gas pipe, vent-pipe, an ignition device are connected with the combustion furnace, a cracking furnace is provided with a feeding port, and a sealing gate, a gas collecting pipe of the feed port, gas collecting pipe, the first end of the cracking furnace. The advantages of the utility model is high in conversion rate, does not generate tar, dioxin and other harmful gas, high temperature, anaerod, device for preparing fermentable reducing sugar from biomass synthesis gas.
NOVELTY - This utility model claims a kind of by using urban domestic garbage and coal producing regenerated coal production system, comprising a storage bin, a magnetic separator, a primary crusher, a high speed rotating machine, a crusher, a high speed rotating machine, and environment protection hot-blast stove, a garbage storage bin, an additive storage bin, a coal slurry storage bin and a forming machine, the storage bin, a magnetic separator, a primary crusher, a high speed rotating machine, a crusher, a high speed rotating machine, and environment protection hot-blast stove and a garbage storage bin through the transmission device are connected with the garbage storage bin, the additive storage bin and a coal storage bin are connected with the forming machine. This utility model can reduce the pollution to the environment, changing waste into valuable, using coal with cracking furnace for household garbage in the coal mine production, coal as adhesive, and has a certain heat value of garbage particles are formed, the product is easy to burn, it is not easy to break, and wide application range, the utility model is new product can be used in the fields of production and life, it can form scale and industrialization.
NOVELTY - Preparation of 3-fluorophthalic anhydride crystal comprises reacting 3-chlorophthalic anhydride and fluorinating agent under nitrogen protection in four-necked flask, monitoring reaction process using gas chromatography, terminating reaction when conversion rate is more than 98%; pouring into ice water, stirring uniformly precipitated solid, filtering, washing using ice water, vacuum drying to obtain crude 3-fluorophthalic anhydride; and washing crude product with aromatic hydrocarbon and long chain alkane, filtering and drying in vacuum at 159-161 degrees C.    USE - Method for preparing 3-fluorophthalic anhydride crystal (claimed).    ADVANTAGE - The method is environment-friendly. It ensures high efficiency, high product purity and high yield.
NOVELTY - Preparation of 1,2-bis(trimethylsilyloxy)cyclohexene comprises reacting 1,2-epoxycyclohexane and dimethyl sulfoxide in the presence of Lewis acid at 20-30 degrees C for 1.5-2 hours, reacting at 50-55 degrees C for 2-3 hours, recovering the solvent to dryness, separating out the solid material, adding into pure water and stirring, filtering, washing the filter cake with pure water, drying to obtain 2-hydroxycyclohexanone, dissolving in toluene or xylene solvent, reflux reacting with trimethylchlorosilane in the presence of an organic base, filtering, evaporating and recycling the solvent, and distilling.    USE - Preparation of 1,2-bis(trimethylsilyloxy)cyclohexene (claimed).    ADVANTAGE - The method has short process flow period, simple operation, low cost, high product selectivity, and high yield and purity and is environment-friendly and suitable for industrial mass production.    DETAILED DESCRIPTION - Preparation of 1,2-bis(trimethylsilyloxy)cyclohexene comprises reacting 1,2-epoxycyclohexane and dimethyl sulfoxide at 1:2.5-2.6 mol ratio in the presence of Lewis acid at 20-30 degrees C for 1.5-2 hours, reacting at 50-55 degrees C for 2-3 hours, recovering the solvent to dryness, separating out the solid material, adding into pure water and stirring, filtering, washing the filter cake with pure water, drying to obtain 2-hydroxycyclohexanone, dissolving in toluene or xylene solvent, reflux reacting with trimethylchlorosilane in the presence of an organic base for 4-6 hours, where the mol ratio of 2-hydroxycyclohexanone and trimethylchlorosilane is 1:2.0-2.1, filtering to remove the reaction product, evaporating and recycling the solvent, and distilling to obtain the product.
NOVELTY - Method for preparing bioethanol, involves (a) saccharifying algae of family Hydrodictyaceae to obtain a saccharified solution containing monosacharides, and (b) culturing microorganisms using the saccharified solution as a carbon source.    USE - The method is useful for preparing bioethanol which is useful as transport fuel or material for producing various chemical products (to contribute to the production of petroleum alternative chemical material).    ADVANTAGE - The method does not use edible resources such as corn and wheat, and hence there is no steep rise in food prices and no ethical problems when the industrial demand of biomass increases. Stable supply of resources is possible, and chemical material can be produced at a low cost due to easy saccharification.
NOVELTY - A process of electrolysis comprising a cathode and an anode containing a catalyst, involves: immersing both the cathode and anode in an electrolyte, where the electrolyte at least partly inhibits further oxidation of a product formed at the anode.    USE - In electrolysis for electrolytic generation of hydrogen peroxide, electrolytic generation of radicals for hydrogen peroxide formation, for water oxidation and water splitting (claimed).    ADVANTAGE - The process improves efficiency and yield and has lower environmental impact compared to analogous processes of the prior art; and capable of forming hydrogen peroxide or hydrogen that can consume energy from a renewable source.
NOVELTY - Accelerating and/or enhancing degradation of an antibiotic that may be present in a carrier material (such as an organic waste), comprises providing the carrier material to an anaerobic digestion (AD) reactor, and optionally maintaining the rate of biogas production substantially steady during the AD process.    USE - The method is useful for accelerating and/or enhancing degradation of an antibiotic present in a carrier material (biowaste material or WDGS), where the antibiotic is a sulfonamide antibacterial agent that includes a sulfonamide group (e.g. sulfamethazine), or a veterinary medicine (all claimed).    ADVANTAGE - The method: facilitates more than 50%, preferably 100% degradation of the antibiotic in the carrier material; and reduces biogas production rate by no more than 40%, 30%, 25% 20%, 15%, 10%, 5% or less, and methane production rate by no more than 25%, 20%, 15%, 10%, 5% or less, hence environmentally friendly and energy efficient.
NOVELTY - Method comprises converting a low molecular weight sugar to a product by mixing the low molecular weight sugar with a microorganism in a fluid medium using a jet mixer, where: the jet mixer comprises a jet-flow agitator; the vessel has an arcuate bottom surface; and a longitudinal axis of a shaft of the jet flow agitator is offset laterally from a longitudinal axis of the vessel.    USE - The method is useful for saccharifying biomass feedstock such as plant biomass, animal biomass and municipal waste biomass to produce useful products, such as fuels, energy, food, pharmaceutical products, hydrogen, alcohols (e.g. monohydric alcohols or dihydric alcohols, such as ethanol), hydrated or hydrous alcohols (e.g. n-propanol or n-butanol), hydrocarbons, and co-products (e.g. proteins, such as cellulolytic proteins (enzymes) or single cell proteins).    ADVANTAGE - The method is capable of simply, rapidly and economically saccharifying the biomass feedstock with high efficiency and low power consumption thus increasing concentration of the final product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a feedstock saccharification apparatus comprising a tank, a feedstock delivery device configured to deliver a feedstock to the tank, a feedstock processing agent delivery device configured to deliver a metered amount of a feedstock processing agent to the tank, and a jet mixer having a nozzle disposed within the tank and configured to mix the delivered biomass feedstock and saccharifying agent, where the jet mixer comprises jet-flow agitators, and each jet-flow agitator is configured to operate reversibly and pumps fluid towards the top of the vessel in a first mode, and towards the bottom of the vessel in a second mode.
NOVELTY - The fuel cell/inerting system (10) has inerting system flow selector valve that is provided with a first inlet port coupled to inerting system feed line of fuel cell system. A fuel tank flow selector valve is provided with a first inlet port coupled to fuel tank feed line of fuel cell system. The first inlet port coupled to fuel tank feed line of fuel cell system is closed when the controller is instructed to supply oxygen depleted air (ODA) to the inerting system. Inlet ports are opened when the controller is instructed to boost the mass flow to the fuel tank.    USE - Fuel cell/inerting system used in aircraft, bus, and train.    ADVANTAGE - The first inlet port coupled to fuel tank feed line of fuel cell system is closed when the controller is instructed to supply ODA to the inerting system. Inlet ports are opened when the controller is instructed to boost the mass flow to the fuel tank. Thus, the fire or explosion in aircraft tanks and cargo bays and local peripheral applications can be prevented efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of operating a fuel cell/inerting system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the input elements used for fuel cell system.    Fuel cell/inerting system (10)
NOVELTY - Preparing glycerol ether (I) and/or (Ia) comprises reacting 1,3-dioxolan-2-one compound (II) with an alcohol compound (III) in the presence of a heterogeneous acid catalyst.    USE - The method is useful for preparing (I) and/or (Ia) (claimed), which is useful in biodiesel industry, cosmetic field, detergent products, washing formulations and pharmaceutical field.    ADVANTAGE - The method is capable of simply and economically preparing (I) and/or (Ia) with high yield.    DETAILED DESCRIPTION - Preparing glycerol ether of formula (R2-CH(OH)-CH(R1)-O-R3) (I) and/or (R1-CH(OH)-CH(R2)-O-R3) (Ia) comprises reacting 1,3-dioxolan-2-one compound of formula (II) with an alcohol compound of formula (R3-OH) (III) in the presence of a heterogeneous acid catalyst.    R1 = H or linear or branched 1-15C, preferably 1-10C alkyl;    R2 = H, linear or branched 1-15C, preferably 1-10C alkyl or alcohol group of formula (-(CH2)nOH) in which n is 0-5, preferably 0-1; and    R3 = linear or branched 1-40C unsaturated alkyl or hydroxyl substituents.
NOVELTY - Treating lignocellulosic biomass, comprises providing the biomass including lignin, forming either a suspension or a first aqueous solution by suspending or dissolving a solid manganese (III) salt including manganese (III) acetate, manganese (III) trifluoroacetate, or manganese (III) triflate in an aqueous solvent, combining an aqueous solution of hydrogen peroxide with the suspension or first aqueous solution to form a second aqueous solution having a pH of less than 6, and combining the second aqueous solution with the biomass under conditions for the decomposition of the lignin.    USE - The method is useful for treating lignocellulosic biomass such as non-food agricultural waste material including wood, corn stover, plant residues and/or grain husks, preferably switchgrass (all claimed), where the lignocellulosic biomass is useful for production of biofuels, paper and a construction material.    ADVANTAGE - The method is capable of economically, easily and effectively treating the lignocellulosic biomass under ambient conditions.
NOVELTY - The system (100) has an exhaust gas sources, a feed gas conduit, a compressor (C), a primary gas separation membrane (GSM1), a primary permeate conduit, a product gas conduit, and a recycle conduit. A recycle control valve (CVa,CVb) is in fluid communication with primary permeate conduit, recycle conduit and product gas conduit, and adapted to adjust a proportion of permeate gas allowed to flow from the primary permeate conduit to recycle conduit versus product gas conduit. A controller (PLC) is adapted to control proportionate adjustment by the recycle control valve.    USE - System for recovering exhaust gas such as fast gas and slow gas. Can also be used in recovering hydrogen, neon, carbon-di-oxide, methane, nitrogen, oxygen, helium.    ADVANTAGE - Since the two stages of membrane-based gas separation is involved in system, the purity of the recovered gas in the product stream is improved and the size of the compressor is reduced. Wide range of feed flow rates of gas is achieved, while reducing capital costs. The flexibility in recovering gas is improved by using partial recycle of the permeate stream. Since the membrane separation system having fixed membrane surface area is used to treat multiple cooling towers without unacceptably high drop in either purity or recovery, the economics of gas recovery are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for recovering gas from process producing wide variation in flow rates.    System for recovering exhaust gas (100)    Compressor (C)    Control valves (CVa,CVb)    Gas separation membrane (GSM1)    Controller (PLC)
NOVELTY - The apparatus (500) has an electricity supply drive unit (60) at which electricity supply drive to a heater layer (53) is intermittently carried out and changing temperature of a gas detection layer. A gas detection unit (61) detects detection-target gas based on electrical property of the gas detection layer at time of electricity supply in the heater layer. A different gas determination unit (62) determines different gas that exists in atmosphere of the gas detection layer based on the electrical property of the gas detection layer when the heater layer is supplied with electricity.    USE - Low-power consumption type lithium ion battery drive gas detection apparatus for detecting combustible interference gas e.g. ethanol, isopropyl alcohol and methane, of a combustion apparatus. Can also be used for detecting carbon monoxide, propane and methanol.    ADVANTAGE - The different gas determination unit determines the different gas that exists in the atmosphere of the gas detection layer based on the electrical property of the gas detection layer when the heater layer is supplied with electricity, so that deterioration of a filter package is diagnosed by the determination result by the different gas determination unit, thus performing preventive maintenance of the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a thin film gas sensor used for a gas detection apparatus.'(Drawing includes non-English language text)'    Heater layer (53)    Electricity supply drive unit (60)    Gas detection unit (61)    Different gas determination unit (62)    Gas detection apparatus (500)
NOVELTY - Biogas plant comprises a first container chamber (10), a second container chamber, a separator (24) for separating biomass solid phase from biomass liquid phase from the first container chamber, and a conveyor for conveying the biomass liquid phase from the first container chamber to the second container chamber.    USE - Used as a biogas plant.    ADVANTAGE - The biogas plant: can be constructed with low cost; and ensures simple production of biogas, in which a high proportion of methane is obtained in the biogas from the used biomass at low fermentation residues.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) separator comprising a backwashing device (96) for back washing the separated biomass liquid phase; and    (2) producing biogas, comprising performing acetogenesis, and transferring biomass liquid phase during performing methanogenesis.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of the separator.    First container chamber (10)    Separator (24)    Screen (28)    Perforated sleeve (72)    Backwashing device (96)
NOVELTY - A water-treatment apparatus comprises a nitrification unit (1) which nitrifies using nitrifying bacteria, and a denitrifying unit (4) which denitrifies using denitrifying bacteria. The denitrifying unit receives supply of breeding water in a breeding tank without passing through the nitrification unit. The nitrification unit receives supply of breeding water into which the denitrifying process by the denitrifying bacteria is formed. At least one portion of breeding water into which nitrification process by using nitrifying bacteria is formed recirculates to the breeding tank.    USE - Apparatus is used for treating water from breeding tank of living organisms e.g. fish, shellfish, crustacean and amphibian.    ADVANTAGE - The water-treatment apparatus efficiently reduces flowing of water with low dissolved oxygen concentration into breeding tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic stricture of water-treatment apparatus. (Drawing includes non-English language text)    Nitrification unit (1)    Backwashing water-supply unit (2)    Decomposition unit (3)    Denitrifying unit (4)    Physical filtration unit (5)
NOVELTY - A reformed-gas supply apparatus comprises reformed-gas generator (12) which can generate reformed gas containing hydrogen at low temperature using catalyst which makes dielectric material support noble metal using source gas by applying voltage and source gas supply part which supplies source gas to reformed-gas generator. The reformed gas is introduced into the air-intake system of an internal combustion engine (1).    USE - A reformed-gas supply apparatus for internal combustion engine (claimed) of vehicles e.g. motor vehicle.    ADVANTAGE - Even when internal combustion engine is in cold condition, reformed-gas generator can produce hydrogen, internal combustion engine can be supplied, and combustion of internal combustion engine can be promoted.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a reformed-gas supply apparatus.    Internal combustion engine (1)    Combustion chamber (2)    Inlet valve (3)    Intake passage (4)    Reformed-gas generator (12)
NOVELTY - Certain disclosed pellets, briquettes, and other compacted products contain multiple components and have a composition tailored to meet specific requirements for a given application. Frequently, at least one of the components is a biomass component. The compacted biomass products can be used in various applications including power generation, animal bedding, and waste absorbent. One particular embodiment involves using compacted body or mass as a fuel supplement or fuel replacement for coal or other fossil fuel(s) in co-firing power plants. Other specific applications include bedding for various animals including fowl, horses, and rabbits. Another application comprises pelletized absorbents such as cat litter for absorbing liquid and/or solid waste products.
NOVELTY - The water treatment system has an anaerobic reactor (10) for decomposing the organic pollution in a wastewater by the action of anaerobic microorganisms. The reactor is filled with the filler for making microorganisms adhere to the inside of the reactor. A membrane activated sludge reactor (13) is provided after the anaerobic reactor, and is provided with a separation membrane for solid-liquid separation biological reactor. A portion corresponding to the amount of reclaimed water among the treated water is processed by the membrane bio-Reactor, and the remaining portion of the treated water is processed by the water sprinkling type aerobic reactor (12).    USE - Water treatment system for recycling of treated water of organic wastewater such as sewage wastewater, agricultural colony wastewater and industrial wastewater.    ADVANTAGE - The anaerobic reactor is arranged in the front stage and the water sprinkling type aerobic reactor and membrane bio-reactor are arranged in the back stage thus the cost of the system can be reduced by combining membrane bio-reactor and the water sprinkling type aerobic reactor. The sludge disposal cost can be reduced. Since the electric power supplied to the blower of membrane bio-reactor can be reduced, the operation cost of system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the water treatment system. (Drawing includes non-English language text)    Anaerobic reactor (10)    Aerobic reactor (12)    Membrane bio-reactor (13)    Treated water pump (21)    Blower of membrane bio-reactor (22)
NOVELTY - A microorganism belonging to genus Bacillus and having ability to decompose at least one of bacterial cell wall, lipid, protein and starch, annihilating Gram negative bacteria or to grow using decomposed bacterial components as source of nutrient, is new.    USE - The microorganism belonging to genus Bacillus is useful in probiotic agent and wastewater treatment apparatus for preventing generation of excess sludge, enabling volume reduction of the excess sludge, processing oil containing wastewater or reducing oil content in wastewater and suppressing fall in flux of membrane used for performing solid-liquid separation (all claimed).    ADVANTAGE - The microorganism enables treatment of oil containing wastewater with good efficiency within shorter period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) probiotic composition comprising the above-mentioned microorganism;    (2) method for performing volume reduction of excess sludge in wastewater treatment, involves adding the above-mentioned microorganism individually or as mixture of 2 or more types of the microorganisms to the to-be-processed water in wastewater treatment plant;    (3) method for suppressing fall in flux of membrane used in wastewater treatment method for performing solid-liquid separation, involves allowing the above-mentioned microorganism to act on solid-liquid separation membrane individually or in mixture of 2 or more types; and    (4) wastewater treatment apparatus comprises inlet pipe for allowing flow of to-be-processed water to processing tank, aeration pipe for aerating the to-be-processed water, discharge pipe for discharging treated or processed water from the wastewater treatment apparatus in wastewater treatment plant and input device for introducing the above-mentioned composition into the wastewater treatment plant.
NOVELTY - Method for controlling microbial reactions in a benthic soil, involves burying a first electrode in an anaerobic soil in a benthic region, setting up a second electrode in water and controlling the first electrode to a redox potential, at which a definite microbial reaction in the soil is inhibited or promoted, by a potential controller that is connected between the electrodes.    USE - The method and system are useful for controlling microbial reactions in benthic soil (claimed) and improving the quality of water under the soil.    ADVANTAGE - The method suppresses generation of greenhouse gases e.g. methane and nitrous oxide stably and efficiently, thus reduced the influence of global warming and eliminates deposition of hazardous substance in the soil due to microorganism reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microorganisms reaction control system.
NOVELTY - Separating lignin from original black liquor (BL(IN)) having a first pH value, involves a first precipitation stage (PR) where an acidifier charge is added to the BL(IN) in order to decrease the pH value of the BL(IN) to a second pH level initiating precipitation of lignin where the second pH level is above pH of 7 and below 11.5, followed by a separation phase (FP1) where the precipitated lignin is separated as a lignin cake from the remaining liquid phase of the acidified BL(IN).    USE - The method is useful for separating lignin from BL(IN) having first pH value (claimed).    ADVANTAGE - Lignin germ particles are added to the BL(IN) in the first precipitation stage, preferably between two phases in the precipitation stage, in order to increase lignin particle growth on such lignin germ particles instead of spontaneous nucleation of lignin particles in the BL(IN). Thus, this will result in improved filterability in subsequent dewatering and lignin cake formation and hence an increased lignin yield.    DETAILED DESCRIPTION - Separating lignin from original black liquor (BL(IN)) having a first pH value, involves a first precipitation stage (PR) where an acidifier charge is added to the BL(IN) in order to decrease the pH value of the BL(IN) to a second pH level initiating precipitation of lignin where the second pH level is above pH of 7 and below 11.5, followed by a separation phase (FP1) where the precipitated lignin is separated as a lignin cake from the remaining liquid phase of the acidified BL(IN), where lignin germ particles are added to the BL(IN) in the first precipitation stage in order to increase lignin particle growth on such lignin germ particles instead of spontaneous nucleation of lignin particles in the BL(IN).
NOVELTY - Method for increasing lipid levels in cell population, involves contacting algal or yeast cell population with at least one compound provided in table 1 of patent specification in an amount sufficient to increase lipid levels in the cell population, where at least one compound does not inhibit fatty acid metabolism.    USE - The method is useful for increasing lipid levels in cell population which is used for producing biofuel (all claimed).    ADVANTAGE - The method enables to increase lipid levels in cell population cost-effectively with excellent sustainability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing saturated or monounsaturated triacylglycerols in a cell population, which involves contacting an algal or yeast cell population with at least one compound provided in table 1 of patent specification in an amount sufficient to induce production of one or more saturated or monounsaturated triacylglycerols in the cell population.
NOVELTY - Storing solar energy captured by a parabolic concentrating solar collector comprises using the solar energy collected by the solar collector for heating a tank containing a solution of inorganic salts including ferrous ion (Fe2+) and potassium ion (K+); and supplying the tanks for anaerobic fermentation of biomass containing Clostridium acetobutylicum and sources of carbohydrates, in order to obtain ethanol, butanol and acetone.    USE - The method is used for storing solar energy captured by a parabolic concentrating solar collector (claimed).    ADVANTAGE - The method above can be carried out on an industrial scale, is environment-friendly and provides high production yields.    DETAILED DESCRIPTION - Storing solar energy captured by a parabolic concentrating solar collector comprises (a) using the solar energy collected by the solar collector for heating a tank containing a solution of inorganic salts including Fe2+ and K+; (b) supplying the tanks for anaerobic fermentation of biomass containing C. acetobutylicum and sources of carbohydrates, in order to obtain ethanol, butanol and acetone; (c) continuously extracting the solvents and hydrogen gas (H2) resulting from the fermentation process to respective storage tanks; and (d) mixing the obtained solvent or other alcohol fuels to obtain high-octane industrial fuel mixtures with a high energy capacity.
NOVELTY - Product is obtained by treating protein materials and using an acid hydrolysis of the protein material in a single step by adding reaction product of sulfuric acid, urea and water. Degradation of urea nitrogen is controlled by forming monocarbamide dihydrogen sulfate including amino product, nitrogen, organic matter, micronutrients, phosphorus, potassium, calcium, magnesium and other biostimulants, such as seaweed extract, fulvic acid and humic acid extracts or extract of amino acids from another source.    USE - Product used as fertilizer or additive for fertilizer formulation (claimed).    ADVANTAGE - The product ensures synergistic effect.    DETAILED DESCRIPTION - The product contains 2-30% of amino acid, 2-30% of nitrogen, 5-50% of organic matter, 2-15% of calcium, 0.5-10% of boron and 0.5-10% of zinc.
NOVELTY - Method for preparing compost using weed, involves mixing weed with agricultural waste to obtain weed mixture, and cultivating the weed mixture to obtain a compost.    USE - The method is useful for preparing compost (claimed) which is used for cleaning industrial contaminants or pollutants, and for preparing chemicals. The method is used for industrial production of agricultural compost.    ADVANTAGE - The method prepares compost with fine grain size and high ripeness degree, in large quantities, maintains microorganisms in compost, is cost-effective, and consumes less time. The compost is highly nutritious, and user-friendly, and has high fertilizer retentivity, high utility value and soil improvement ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost, which is prepared by the above-mentioned method.
NOVELTY - Preparing 2-(4-methanesulfonyl-phenyl)-1-(6-methyl-pyridin-3-yl)-ethanone (I) or its salt comprises reacting 1-(6-methyl-pyridin-3-yl)-ethanone (II) with a halogenated methanesulfonyl-benzene compound (III) in the presence of a catalyst, a ligand and a base, where: the catalyst is a palladium catalyst complex; the ligand is an organophosphoric compound, which is 4,5-bis-(diphenylphosphino)-9,9-dimethylxanthene; and the base excludes potassium phosphate in an amount of 3 equivalents.    USE - (I) is useful as a key intermediate in the preparation of etoricoxib, which is a cyclooxygenase-2 inhibitor. Etoricoxib is useful for treating chronic pain, rheumatoid arthritis and osteoarthritis.    ADVANTAGE - The process provides (I) in good yield using easily available raw materials and without consuming large number of synthetic steps and using toxic chemicals such as sodium or potassium cyanide, hence economical and ecofriendly.    DETAILED DESCRIPTION - Preparing 2-(4-methanesulfonyl-phenyl)-1-(6-methyl-pyridin-3-yl)-ethanone (I) or its salt comprises reacting 1-(6-methyl-pyridin-3-yl)-ethanone (II) with a halogenated methanesulfonyl-benzene compound of formula (III) in the presence of a catalyst, a ligand and a base, where: the catalyst is a palladium catalyst complex; the ligand is an organophosphoric compound, which is 4,5-bis-(diphenylphosphino)-9,9-dimethylxantene; and the base excludes potassium phosphate in an amount of 3 equivalents.    X = halo, preferably Br.
NOVELTY - A sewage-gas electric-power generation system consists of a sewage-gas booster (2) which increases the pressure of sewage gas containing methane and carbon dioxide as main component, a separation column (3) connected to the booster, for separating the pressurized sewage gas into methane and carbon dioxide, and an electric-power generating apparatus (10) which produces electric power using the separated carbon dioxide.    USE - Sewage-gas electric-power generation system (claimed).    ADVANTAGE - The sewage-gas electric-power generation system enables effective usage of carbon dioxide which is discharged to atmosphere, as energy source. Electric-power generation efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the sewage-gas electric-power generation system. (Drawing includes non-English language text)    Mist separator (1)    Sewage-gas booster (2)    Separation column (3)    Dehumidifier (6)    Turbine (8)    Electric-power generating apparatus (10)
NOVELTY - Asymmetric-synthesis method involves continuously pouring substrate comprising hybrid catalyst containing DNA and metal complex in a reactor, performing chemical reaction on the substrate and obtaining a product.    USE - The asymmetric-synthesis method is useful for producing target product which is used as medical agent and agrochemical product.    ADVANTAGE - The method is cost-effective, and environmentally-friendly as it does not use organic solvent, enables to synthesis target product with high yield and high enantio-selectively and solve problem of metal complex with respect to air and humidity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hybrid catalyst which comprises (a) DNA and metal complex, where the DNA comprises 12, 13, 16, 20, 24, or 31 base pair sequence (SQE ID NO: 1-11) fully defined in the specification, and the metal complex comprises copper (II) as center metal, and one or more compound chosen from 2-(1H-imidazol-2-yl)-pyridine, (1,10)phenanthroline, 5,6-dimethyl-(1,10)phenanthroline, 4,7-dichloro-(1,10) phenanthroline, 4,7-dichloro-3,8-dimethyl-(1,10)phenanthroline, 2H-2,7,8-triaza-cyclopenta(I)phenanthrene, 1,4,8,9-tetraaza-triphenylene, 5-eth-(Z)-yildeneamino-4-vinyl-1,3,3a,9b-tetrahydro-imidazo(4,5-f)quinolin-2-one, and 4,5,9,14-tetraaza-benzo(b)triphenylene as a ligand, or (b) DNA and metal complex, where the DNA is the above-mentioned DNA, and the metal complex comprises copper (II) as a center metal, and one or more compound chosen from 5,6-dimethyl-(1,10)phenanthroline, 4,7-dichloro-(1,10) phenanthroline, 4,7-dichloro-3,8-dimethyl-(1,10)phenanthroline, 2H-2,7,8-triaza-cyclopenta(I)phenanthrene, and 1,4,8,9-tetraaza-triphenylene as a ligand.
NOVELTY - Manufacture of bio-oil involves thermally decomposing plant-derived biomass in presence of calcium carbonate as catalyst and heating medium.    USE - Manufacture of bio-oil (claimed).    ADVANTAGE - The bio-oil with reduced oxygen content is manufactured economically and with high yield.
NOVELTY - The system has pumps (7) that are provided to pump the positive and negative electrolytes from the compartments to the storage tanks (14,15). A catalytic bed (11) oxidatively forms the chemical species from the positive electrolyte, and regenerates the positive electrolyte for reuse in a redox flow battery. Another catalytic bed reduces the protons from the negative electrolyte into molecular hydrogen gas, and regenerates the negative electrolyte for reuse in the redox flow battery. The valves are provided to direct the electrolytes between different components.    USE - Redox flow battery system for electrical energy storage and hydrogen production.    ADVANTAGE - The necessity to provide the specific geographical siting, or extensive maintenance for the redox flow battery is prevented. Since the cross-diffusion of the cations through the membrane does not affect the cycle current efficiency, the service life of the redox flow battery is enhanced. The solubility and stability of the redox species are improved. The manufacturing cost of the redox flow battery system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the redox flow battery system.    Power source (4)    Load (5)    Pump (7)    Catalytic bed (11)    Storage tanks (14,15)
NOVELTY - Invention relates to a method of making fuel briquettes from biomass, involving heat treatment of biomass at temperature of 200-500 degrees C without access to air, preparing binding substance obtained by dissolving dextrin in a pyrolysis condensate in ratio of 1:(5-20), mixing the binder with a carbon residue ground to particle size of 2 mm, moulding a fuel briquette from the obtained mixture and drying said briquette at room temperature for 2-5 days. The obtained briquettes have low combustion heat, improved mechanical strength and resistance to compression.    USE - Oil and gas industry.    ADVANTAGE - Use of the disclosed method widens the range of solid fuel, the raw material base for making briquettes and reduces technological expenses on making briquettes.1 cl, 1 dwg, 1 tbl, 6 ex
NOVELTY - The method involves performing physical-chemical transformation through superadiabatic gasification. The collected municipal waste (1) is discharged in an area suitable for selection of equipment (2) for separating recyclable oversized material (3), where the resulting material is homogenized to less than 50 mm in a mill disintegrator and then briquetted in dimensions of 50-100 mm to feed into a reactor (7). The obtained material is processed by conveyor (9) or bucket elevator and then discharged into silo (10) located above the reactor.    USE - Method for transforming urban municipal waste into usable and clean products.    ADVANTAGE - The method simply transforms municipal waste without generating high percentage of nitrogen oxides in flue gases as well as fly ash with low environmental impact, and greatly induces formation of pollutants, dust, sulfur oxides, nitrogen, hydrogen chloride and hazardous polyaromatic hydrocarbons, polychlorinated dibenzodioxins and dibenzofuran.    DETAILED DESCRIPTION - The silo is connected with a feeder screw (13) that integrates with the valve-pendulum (14), where the pendulum valve is actuated by sensors which are located in cylinder balancing (15) to maintain operating levels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representative diagram of the method for disposal of municipal waste.    Municipal waste (1)    Equipment (2)    Oversized material (3)    Reactor (7)    Conveyor (9)    Silo (10)    Feeder screw (13)    Valve-pendulum (14)    Cylinder balancing (15)
NOVELTY - The biomass energy enhancer is provided to increase energy content of biomass intended to be used as clean fuel without moisture. A series of device is designed for measuring electromagnetic radiation, where electromagnetic oscillation is caused only resonance of water molecules without hydrocarbons and fatty acids. The heat is generated by magnetrons distributed in all modules for each hexagonal cavity.    USE - Biomass energy enhancer.    ADVANTAGE - The biomass energy enhancer is provided to increase energy content of biomass intended to be used as clean fuel without moisture, and thus provides a high utility to process solid biofuels, lowers humidity inside plant or organic biomass, increases internal energy content, and transforms biomass into clean fuel for replacing fossil modalities.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water to be vaporized and a molecular twist.
NOVELTY - Briquettes production involves collecting and selecting raw materials, which is ground by using binders. The obtained material is washed, compressed, heating and stored. The sheets are subjected to grinding process by rotating equipment.    USE - Method for producing briquettes by using leaves as raw material.    ADVANTAGE - The method simply produces briquettes with increases performance in a cost-effective and eco-friendly manner using leaves.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for producing briquettes from leaves of trees. (Drawing includes non-English language text).
NOVELTY - A substrate compound containing atom group comprising oxygen or sulfur is reacted with a diamine compound (I) at 120 degrees C or less and the atom group is removed under neutral condition to obtain compound containing amino and/or hydroxyl group.    USE - Method of producing compound containing amino and/or hydroxyl group used in pharmaceuticals.    ADVANTAGE - Since the reaction is carried out under mild conditions, the reaction is applicable to substrate compound with different functional groups other than the atom group. The reaction is carried out using inexpensive raw material, and advances efficiently under solvent-free conditions.    DETAILED DESCRIPTION - A substrate compound containing atom group comprising oxygen or sulfur is reacted with a diamine compound of formula: H2N-A-NH2 (I) at 120 degrees C or less and the atom group is removed under neutral condition to obtain compound containing amino and/or hydroxyl group.    A=optionally 1-6C alkyl, alkylamine optionally containing 1 or 2 N.    (i) When A does not exist, the compound (I) is hydrazine.
NOVELTY - The system has a thermal medium exchanging heat generated in a fuel cell (10) between a fuel cell row switching section (11) and a circulating pipe (30) and exchanging geothermal heat energy between the circulating pipe and a ground heat exchanger (20). A load (60) performs a heating process by the thermal medium of a heat pump heat exchanger (40). The heat pump heat exchanger cools another thermal medium of another circulating pipe (50). A pair of valves controls heat exchanging process between the former circulating pipe and the fuel cell row switching section.    USE - Hybrid air conditioning system.    ADVANTAGE - The system performs cooling and heating process by one facility. The system has improved heating efficiency, and is environment-friendly and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hybrid air conditioning system.'(Drawing includes non-English language text)'    Fuel cell (10)    Fuel cell row switching section (11)    Ground heat exchanger (20)    Circulating pipes (30, 50)    Heat pump heat exchanger (40)    Load (60)
NOVELTY - The method involves providing agricultural products i.e. corn silage, in a substrate. The agricultural products are transferred to pellets and volumetric load fermenting tanks. Methane gas is passed into a dryer to generate electrical energy that is used for a micronization process.    USE - Method for producing fuel from biomass.    ADVANTAGE - The method enables quickly micronizing biomass in drying process under industrial conditions and minimizing passage of methane into environment for preventing air pollution.
NOVELTY - A breeding field sewage treatment system, comprising a flow cell, a flow cell, the flow cell, the flow cell and the fifth flow cell, the flow cell provided with two adjacent of the flowing pool are is provided with a sewage inlet and a sewage outlet, the flow of sewage inlet pool is a sewage outlet of the flowing pool, sewage inlet of the fifth flow cell is provided with a grid, the lower part of the grid on the other side wall is provided with a water outlet, the water outlet is connected with the marsh gas tank. This utility model has simple structure, reasonable design, the sewage flow cell cultivation field discharged from the fourth after diluting, the impurity and solid substance in the sewage is filtered by the grid sewage filter is directly discharged marsh gas tank fermenting marsh gas, which solves the production of farm, domestic energy.
NOVELTY - This utility model is a kind of a renewable energy source agricultural and animal husbandry organic ecological resource recycling system. The system is composed of the solar battery assembly is connected by cable and an inverter, the inverter is connected with the solar water pump, solar energy water pump by cable river, reservoir and farmland by . Inverter passes through cable respectively connected with rural power grid, refrigerator and food. The farmland respectively connected with a raw material particle fuel granulator, village and dung collecting tank. Connection method of solar heat concentrator heat preservation hot water tank through circulating pipe, an air source heat pump and a dung collecting tank. Animal husbandry farm dung collecting connected to heating tank by the pipeline and the pump, an anaerobic fermenting tank, a desulfurizing gas-water separator, an air storage tank, a marsh gas generator, the overflow sedimentation tank, solid-liquid separator, solid organic fertilizer production workshop, liquid organic pesticide organic liquid fertilizer production workshop. Farmland and stock-raising field separately connected with cooling base and organic food. This utility model is a renewable energy source circular can finally realize the agriculture, animal husbandry pollution " zero release ", which completely solves the problem of serious agricultural non-point source pollution.
NOVELTY - The equipment comprises a gasification furnace (1), a removable door (2), gas inlet duct (3), heat exchanger (4), a liquid centrifugal pump (5), gas outlet duct (6), exhaust unit (7), double combustion box (8), plumbing unit (9) and chimney (10).    USE - Equipment for gasification of waste tires with gas comes from biomass combustion.    ADVANTAGE - The equipment comprises a gasification furnace, a removable door, gas inlet duct, heat exchanger, a liquid centrifugal pump, gas outlet duct, exhaust unit, double combustion box, plumbing unit and chimney, and thus the equipment is simple and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for gasification of waste tires with gas comes from biomass combustion.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an equipment.    Gasification furnace (1)    Removable door (2)    Gas inlet duct (3)    Heat exchanger (4)    Liquid centrifugal pump (5)    Gas outlet duct (6)    Exhaust unit (7)    Double combustion box (8)    Plumbing unit (9)    Chimney (10)
NOVELTY - The power supply apparatus has a battery management system (110) connected between fuel cell system (100) and grid (200). The battery management system discharges electricity produced in fuel cell system to the grid under the control of a power control unit (150). The power control unit is provided for controlling a discharge power supply unit according to electric power consumption pattern of user.    USE - Power supply apparatus of electric power system.    ADVANTAGE - The electricity of the fuel cell system can be supplied to assumption in consideration of power use pattern of the consumer. The function of the uninterruptible power supply system can be realized by supplying the emergency power source to the assumption in occurrence of blackout through battery management system. The generation of malfunction in load can be prevented, and the size and capacity of the battery can be reduced. The waste heat generated in the fuel cell is supplied to the battery management system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the power supply apparatus. (Drawing includes non-English language text)    Fuel cell system (100)    Battery management system (110)    Power control unit (150)    Grid (200)
NOVELTY - The hybrid anaerobic reactor includes two sections, a fixed bed, and fluidized bed to perform inverse process for removing organic material present in various types of effluents and agro-industrial waste.    USE - Hybrid anaerobic reactor for obtaining methane-rich biogas.    ADVANTAGE - The hybrid anaerobic reactor achieves high efficiency to remove organic waste in a single reactor, and saves space, energy and time.
NOVELTY - The method involves mixing mature compost and organic fraction of municipal solid waste under certain conditions in order to accelerate speed of hydrolysis and anaerobic biodegradation of residue.    USE - Method for pre-treatment of biological organic waste by anaerobic biodegradation process for recovery of biogas.
NOVELTY - The cylinder hydraulic machine comprises hydraulic pump for providing pressure, and hydraulic cylinders for increasing force of compaction by using a hydraulic accumulator.    USE - Cylinder hydraulic machine for producing pellets from sawdust.    ADVANTAGE - The cylinder hydraulic machine provides pellets with increased density of 2.900-4.973 kg/m3 and heat capacity of 3.483-7.029 Kcal /Kg.
NOVELTY - Use of catalyst system is claimed for catalyzing transesterification reactions for preparing fatty acid alkyl esters used as biodiesel component. The catalyst is selected from alkali metal alkanolates or alkaline earth metal in one or multiple organic solvents.    USE - Used for performing catalysis of transesterification reactions for preparing fatty acid alkyl esters used as a biodiesel component (all claimed).    ADVANTAGE - The catalyst system provides an important substitute of fossil diesel in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fatty acid alkyl esters, which involves performing transesterification of mono-, di- or triglycerides in presence of a catalyst system in monovalent alcohol.
NOVELTY - The device has a mini hydrogen generator and a wiring harness with wires, fuse and relay which are hooked with a tubing and accessories. An electrolyzer uses alkaline electrolyte to split distilled water into hydrogen and oxygen components. Oxy-hydrogen gas which is a mixture of hydrogen and oxygen is produced. A gas vent hole (2) is provided in each electrolyzer plate. Spacers are cut out of 3mm thick PVC sheet. The electrolyzer is equipped with a bubbler to prevent backfires. Electrolyzer is filled with vinegar to neutralize residual sodium hydroxide vapors.    USE - Device for construction and working of eco-friendly hybrid hydrogen system for vehicle e.g. scooter. Can also be used in moped, bikes, land mowers and generators.    ADVANTAGE - A cost effective, easy to construct, install and maintain hybrid hydrogen system can be achieved. The pollution can be reduced and the mileage of the vehicle can be increased by using distill water. The combustion rate of fuel is enhanced. The horse power of the engine can be enhanced. The life and performance of the engine can be improved.The smooth and quiet engine operation can be performed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for construction and working of eco-friendly hybrid hydrogen system.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the electrolyzer.    Gas vent hole (2)    Electrolyte level (4)    PVC end plate (5)    Stainless steel electrode (6)    PVC spacer rings (7)
NOVELTY - This utility model claims a refuse derived fuel manufacturing system, comprising a gasification furnace, a cracking furnace for household garbage carbonization furnace, extruding forming machine and a gas purifying and separating device, air outlet outputting the utility new-type gasification furnace consumption a combustible garbage gasification furnace is 400 degrees centigrade to -600 degrees centigrade high temperature combustible gas supply cracking furnace for household garbage carbonization furnace, a cracking furnace for household garbage carbonization gasification furnace of high temperature combustion gas to a combustion drying processor for kitchen litter, and the combustible garbage pyrolysis and carbonization, and then extruding forming machine caused by the manufacture to refuse derived fuel RDF, RDF fuel of the utility model is free of organic matter and it is convenient to transport and storage, the heat value is high, and the harmful gas generated by combustion is greatly reduced, it can be directly used for gasification furnace for gasification to generate combustion gases, the cracking furnace for household garbage carbonization furnace also generates a large amount of combustible gas, a combustible gas enters a gas purifying and separating device to obtain the clean fuel gas and oil, the utility model, with the combustible garbage generate cleaning gas, crude oil and solid fuel RDF, and the energy is saved.
NOVELTY - A kind of full automatic burner of biomass fuel granulating machine, this utility model relates to biomass fuel processing mechanical technology field, it is a full automatic burner of biomass fuel granulator comprising screening drying device, processing device, a packing device and a power device, screening and drying device, processing device and packaging device are connected with the power device is connected with the screen drying device, processing device and packaging device. This utility model adopts four device is composed of a work flow line, reasonable layout and convenient using three-stage separator, completely. A electronic scale weighing side edge the packaging method, saves time and labour, it is convenient and fast. This utility model uses automatic control, the operation control to only one person is capable of finishing, efficiency is high. Control circuit advanced structure, high reliability, energy-saving, strong practicability.
NOVELTY - This utility model claims a kind of synthetic air and so on. reclaiming and purifying device solves the problem that the current device is the purified synthesis air with liquid. A synthetic ammonia is provided with the air feeding port on the lower part of the ammonia absorbing tube bodies (1) (2), is provided with a soft water inlet (4) on the upper part is provided with a synthetic ammonia air outlet (5), the ammonia absorbing tube body (1), a soft water inlet (4) of the ammonia absorbing cylinder (1) on the inner side wall in a downward direction at intervals is provided with a tray (3), one side of the tray (3) and the ammonia absorbing cylinder (1) is fixedly connected with the side wall of the other side of the tray (3) of the ammonia absorbing tube body (1) is provided with the inner side wall of the water channel (9), water channel (9) is in S shape is provided with a bubble cap are evenly distributed on the tray (3), (6), is provided with a vent hole between the adjacent of the cover (6) (7). Greatly improves the cleaning quality of synthetic air.
NOVELTY - Acephate diastereoisomers are new.    USE - New acephate diastereoisomers is used as insecticide (claimed).    ADVANTAGE - The acephate diastereoisomers are manufactured efficiently and economically with excellent biological activity. The energy consumption and waste water discharge during manufacture of acephate diastereoisomers are reduced by 80% or more and 95% or more, respectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of acephate diastereoisomers.
NOVELTY - Generating biogas by using cornstalk through dry fermentation, comprises: (1) cutting the cornstalk into small segments; (2) adding an equal quantity of water into the cornstalk, and soaking; (3) adding a composite microbial inoculant and an ammonium bicarbonate solution; (4) piling up the cornstalk, punching, covering, and leaving seams at the top part; (5) maintaining the stack retting till a layer of white hypha can be seen on the stack; and (6) adding inoculum and carrying out anaerobic fermentation.    USE - The method is useful for generating biogas (claimed).    ADVANTAGE - The method for generating the biogas is long in lasting time, high in biogas generation rate, low in sewage treatment expense and low in sulfur content, and can be directly used by a biogas engine without gas washing.    DETAILED DESCRIPTION - Generating biogas by using cornstalk through dry fermentation, comprises: (1) cutting the cornstalk into small segments with length of 2-6 cm; (2) adding an equal quantity of water into the cornstalk, and soaking for 15-24 hours; (3) adding a composite microbial inoculant and an ammonium bicarbonate solution, so as to enable the moisture content of the cornstalk to be 60-80%; (4) piling up the cornstalk, punching, covering the surrounding parts and top part of the stack by using a film or cornstalk, and leaving seams at the top part; (5) subjecting the stack to a temperature of 40-60 degrees C, maintaining the stack retting for 80-120 hours till a layer of white hypha can be seen on the stack; and (6) adding inoculum and carrying out anaerobic fermentation of the cornstalk in normal temperature of 25 degrees C.
NOVELTY - Treating of tomato (Lycopersicon esculentum) plants to control vascular wilt caused by Fusarium sp. comprises applying Piper betle leaf extract.    USE - The method is useful for treating tomato plants to control vascular wilt caused by Fusarium sp.. The ability of Piper betle leaf extract to treat vascular wilt caused by Fusarium oxysporum was tested on tomato plant seedlings. The result shows that the pathogenicity was found to be 11 plus minus 3.2% after 21 days treatment with Piper betle leaf extract at 2%.    ADVANTAGE - The method: controls the deadly vascular wilt of tomato plants caused by Fusarium sp, thus replaces/reduces the use of commercial chemical fungicides; utilizes 1-0.25 wt/wt.% of extracted product to effectively control the disease in seedlings and through seeds respectively; utilizes Piper betle leaf extract, which is stable, can be applied directly to soil and to the seeds, is easy to prepare and handle, can be stored at 4 degrees C without losing its properties, which is essential for its bulk production, and require easily available chemicals for processing viz. chloroform and dimethyl sulfoxide; and is environmentally-friendly and non toxic method for controlling the disease.
NOVELTY - The method involves mounting a rotating shaft on the electrolytic cell. The electrolytic cell is rotated, so as to generate ultra-gravity centrifugal force. The direct electrolytic current is applied between the cathode (3) and anode (2), so as to generate oxygen and hydrogen. The current density is controlled, such that the current density is set within the range of 500-1000A/m2.    USE - Water electrolysis hydrogen preparing method.    ADVANTAGE - The chlorine-alkali electrolysis device can be strengthened so as to produce hydrogen and chlorine. The power consumption of the hydrogen preparing device can be reduced. The production efficiency of the device can be improved. The electrochemical reaction rate and the product gas/liquid separation efficiency can be enhanced. The voltage of an electrolytic tank can be reduced. The electrolytic current density can be improved, while improving the electrolytic efficiency and the production rate of the device. The ultra-gravity can be changed easily and effectively by controlling the rotating speed of rotary electrolytic cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the water electrolysis hydrogen preparing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis hydrogen preparing device.    Rotary tube (1)    Anode (2)    Cathode (3)    Diaphragm plate (4)    Electrolyte (5)
NOVELTY - The apparatus comprises a noncatalytic reactor adapted for methanation, by supplying activation energy, through sparc or plasma ignition to generate synthetic natural gas from a source gas, a power supply unit (102), an electric energy control unit, a source gas mixing injector (103) that is installed at the reactor, a swirl generator installed inside the gas mixing injector, a cooling device (117) connected to the reactor, and a system (112) for sensing temperature at a center and surface of the reactor.    USE - The apparatus for producing synthetic natural gas such as carbon monoxide, carbon dioxide and hydrogen using sparc or plasma ignition (claimed), where the natural gas is useful as fuel for power generation and in vehicle.    ADVANTAGE - The synthetic natural gas has high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a synthetic natural gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a synthetic natural gas producing device.    Power supply (102)    gas mixing injector (103)    Pressure control valve (105)    Flow meter (106)    Temperature sensing system (112)    Cooling device. (117)
NOVELTY - Method involves bringing a methanol-containing stream into contact with water, separating the propane fraction from the water-methanol solution, removing methanol in form of its aqueous solution, fortifying the aqueous methanol solution via rectification, characterised by that the methanol-containing stream is brought into contact with water by mixing. Water consumption is determined by the following condition: 3.Qmet.less than Qwater less than 0.2.Qmet., where Qmet. is the amount of methanol from the propane fraction per hour, m3/h; Qwater is the amount of water fed for washing, m3/h. After separation from the water-methanol phase fed for fortification, the propane fraction is fed into a column for azeotropic rectification. A water-methanol-propane azeotrope-forming mixture in vapour form is output from the top part of the column, compressed, condensed and then fed for mixing with water, and a purified and dried propane fraction containing a residual amount of methanol and water is then output from the bottom part of the column. The propane fraction fed for purification and drying is also directly fed for mixing with water or is fed together with the propane fraction after separation from the water-methanol phase for azeotropic rectification.    USE - Chemistry.    ADVANTAGE - Use of the present method enables to reduce specific energy consumption in the drying and purification processes when realising the method. 8 cl, 8 ex, 8 tbl, 2 dwg
NOVELTY - This utility model claims a combustion energy-saving furnace with biomass straw gasification furnace of the stirring rod, a crank, a fixed block and a stirring paddle, the crank is connected with the fixing block, the fixing block is connected with the stirring paddle, the diameter of the fixed block is covered outside the heat insulating cotton, the one used for combustion energy-saving furnace with biomass straw gasification furnace of the stirring rod, the crank is covered heat insulating cotton of the stirring rod can effectively avoid the crank temperature is too high, so as to avoid the potential safety hazard, improves the safety of production is the diameter of the stirring paddle, the rocker. The heat insulating cotton is covered sand skid-proof jacket, is convenient for operator to stirring operation, to produce at the same time improve the production security of humanization.
NOVELTY - This utility model claims a kind of biomass catalytic gasification furnace, comprising a shell body is installed on the inner part of the high temperature burning chamber biomass gasification conversion chamber, the catalytic biomass gasification material feeding auger system, biomass coal powder feeding system and material feeding biomass gasification system of straw fast thermal-cracking conversion chamber and the outside of the shell, wherein the biomass gasification conversion chamber and catalytic cracking conversion chamber is connected by the gas pipeline, the biomass gasification conversion chamber and catalytic cracking conversion chamber connected with a biomass gasification conversion chamber and biomass gasification material feeding system with high temperature combustion chamber, the biomass gasification material feeding auger system, a high temperature combustion chamber by a combustion material inlet pipe and biomass pulverized coal feeding system. This utility model has compact structure, the smoke is recycled, little heat loss, high energy utilization rate, the operation process of biomass gasification and gas is not mixed in the air nitrogen and other inert gas gasification efficiency is high, the heat value is high.
NOVELTY - This utility model claims a kind of combustion energy-saving furnace with biomass straw gasification furnace, comprising a furnace body, a hopper, a stirring device, a gas-guide layer, a cooling layer and water layer, the top of the furnace body is provided with a hopper, the stirring device comprises a motor, a sieve plate and a transmission gear, the furnace body is provided with a sieve plate, the sieve plate is a round sieve plate, the sieve plate uniformly distributed with mesh, the periphery of the sieve plate is provided with a gear ring, the motor is connected with the transmission gear, the wheel tooth of the transmission gear and the gear of the gear ring. The combustion energy-saving furnace with biomass straw gasification furnace, it can smoothly realize combustion energy-saving furnace with biomass straw gasification generated gas, and raw material feeding device for straw automatic feeding, does not need the operation and improves the production efficiency and ensures the production safety. Provided with stirring device for stirring the straw, the more straw can contact with air for combustion and gasification at the same time, so that the straw is generated by burning of the dust dropped off from the mesh of the sieve plate, which avoids combustion ash the straw combustion and gasification effect.
NOVELTY - This utility model claims a combustion energy-saving furnace with biomass straw gasification of stirring device, comprising a motor, a transmission gear, a sieve plate and a sieve plate is a round sieve plate, the sieve plate uniformly distributed with mesh, the periphery of the sieve plate is provided with a gear ring, the motor is connected with the transmission gear, the wheel tooth of the transmission gear and the gear engaged with the gear ring, the one used for combustion energy-saving furnace with biomass straw gasification of the stirring device, has simple and reasonable structure design, solves the problem that the combustion energy-saving furnace with biomass straw gasification in the gasification furnace in the high temperature is not convenient to stir the straw, and can make the position of the straw so that the straw more contact with air for combustion and gasification, at the same time, the combustion energy-saving furnace with biomass straw forming fuel ash falling to the gasification furnace from the mesh of the sieve plate, it can avoid combustion ash influencing the production benefit of the combustion energy-saving furnace with biomass straw gasification combustion and gasification, the gasification furnace.
NOVELTY - This utility model claims a combustion energy-saving furnace with biomass straw gasification furnace is a sealing device, comprising a sealing water channel and at least more than one air outlet connecting pipe, the first end of the connecting pipe is connected with the gasification furnace, and the other end of the connecting pipe is set at the bottom of the sealing channel, the sealing channel is set on the side of the gasification furnace wall, the furnace sealing channel is an annular sealing channel, a sealing channel around the side wall of the gasification furnace is provided with a furnace wall, the one used for combustion energy-saving furnace with biomass straw gasification furnace, a gasification furnace capable of combusting the straw for an effective seal to prevent gas leakage, ensure smooth the collected gas. At the same time, the pressure increase, gasification furnace or reduced, and can carry out proper adjustment of the pressure in the gasification furnace, the pressure in the gasification furnace in the reasonable range, which avoids the change of pressure in the gasification furnace so as to excessive damage to the gasification furnace, the service life of the gasification furnace.
NOVELTY - This utility model claims a combustion energy-saving furnace with biomass straw gasification furnace structure of industrial furnace, comprising a furnace body, the furnace body is surrounded with gas-guide layer, the gas-guide layer and the furnace body, outside the gas-guide layer is circumferentially provided with a cooling layer, the water cooling layer is water channel, the water cooling layer is circumferentially provided with a adjusting layer, the water layer is water channel, the one used for combustion energy-saving furnace with biomass straw gasification furnace is a furnace, specifically a water cooling layer and the water layer to adjust the gasification furnace temperature, the heat of the gasification furnace in turn outwardly so as to adjust the gasification furnace. One is used for combustion energy-saving furnace with biomass straw gasification furnace structure of industrial furnace can effectively adjust temperature, and the production cost is controlled at a lower level, which is good for increasing the production efficiency. A water cooling layer and a adjusting layer are provided with a pump for regulating the water quantity in the water cooling layer and the water layer so as to adjust the temperature in the cooling effect is connected with the gasification furnace of the gasification furnace.
NOVELTY - Preparation of chicken manure organic fertilizer comprises placing chicken manure into fermenting tank, adding yeast strain, covering with plastic film, fermenting for 15-20 days, drying and crushing.    USE - Method for preparing chicken manure organic fertilizer (claimed) used for promoting activity and permeability of soil, loosening soil compaction, promoting water retention, sterilizing and repelling soil insects, preventing and treating continuous cropping disease, and increasing product quality and production efficiency.
NOVELTY - Production of tobacco stems bioorganic fertilizer comprises mixing 30-70 wt.% tobacco stems, 20-50 wt.% additive, 5-15 wt.% conditioner and 1-5 wt.% microorganism bacterium, aerobic composting, stacking and adjusting compost carbon/nitrogen ratio to 25-35/1, water content to 50-65 wt.%, pH to 5-8.5 and stack height to 1-1.5 m, crushing, sieving and packaging. The microorganism is Bacillus subtilis, Bacillus megaterium, thermophilic Acremonium hansfordii, Aspergillus and/or Trichoderma reesei.    USE - Method for producing tobacco stems bioorganic fertilizer (claimed) used for improving soil structure.    ADVANTAGE - The method increases production efficiency and reduces pollution.
NOVELTY - The device has a big frame which is provided in a device main portion. A frame (7), a driving shaft (8), a connecting shaft (9), a driven shaft (10), a walking wheel (12) and a walking power unit are connected wit each other. A driving shaft is connected with the walking power unit, and driven shaft is connected by a connecting shaft. The side portions of the frame are provided with the three driven shafts, and driving shaft and the driven shaft are provided with walking wheels.    USE - Traveling device of groove type turner for use with organic fertilizer production machinery equipment used in organic fertilizer production industry.    ADVANTAGE - The operation of the traveling device can be ensured, as the center of gravity is low. The safety of the operator can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the traveling device.    Frame (7)    Driving shaft (8)    Connecting shaft (9)    Walking wheel (12)
NOVELTY - Natural plant fertilizer comprises 40-60 pts. wt. lacquer tree fruit, 7.5-10 pts. wt. soapberry fruit, 12.5-20 pts. wt. wild jujube fruit, 30-60 pts. wt. Paulownia, 20-40 pts. wt. phosphorus fertilizer, and 95-180 pts. wt. or 4000-4500 pts. wt. animal manure.    USE - Natural plant fertilizer used for improving crop growth.    ADVANTAGE - The fertilizer has no toxic and side effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of natural plant fertilizer comprising taking lacquer tree fruit, crushing, adding water, boiling for 20 minutes, transferring in fermenting tank; taking soapberry fruit, crushing, transferring in fermenting tank; crushing wild jujube fruit, placing in fermenting tank; crushing dried vegetable, transferring in fermenting tank, crushing Paulownia, transferring in fermenting tank; adding phosphorus fertilizer in fermenting tank; and adding animal manure and 4000-4500 pts. wt. water and soaking for 15-30 days.
NOVELTY - A slow release composite fertilizer comprises taking 20-40 pts. wt. urea, 7-20 pts. wt. ammonium sulfate, 10-35 pts. wt. potassium sulfate, 25-30 pts. wt. mixed fertilizer, 0.1-0.5 pt. wt. zinc-iron-molybdenum additives, 7-10 pts. wt. granulating agent and balance water.    USE - Slow release composite fertilizer used for soybean cultivation (claimed).    ADVANTAGE - The fertilizer has high utilization rate, improves yield and quality with environment-friendly preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of slow release composite fertilizer comprising melting urea, adding ammonium sulfate and potassium sulfate, standing, adding apatite powder with 100 mesh fineness, diammonium phosphate and magnesium phosphate, mixing uniformly, adding remaining components, standing, adding stearic acid coating, heating, cooling, drying at 50-80 degrees C, adding talcum powder and modified zeolite powder, mixing, grinding into 120 mesh and screening.
NOVELTY - Extraction of 99% rebaudioside A from Stevia comprises mixing methanol and water to prepare 75-100% solvent; mixing low-purity stevioside and solvent at 1:3-1:10 mass ratio by hybrid plasmid; stirring, standing for 2-6 hours; stirring mixture at less than 30 degrees C for 6-10 hours; centrifuging or filtering using filter with greater than 500 mesh pore size; washing separated solid with 95-100% methanol solution for 2-4 times at 30 minutes/washing; centrifuging or filtering using filter with greater than 500 mesh pore size; and drying or spray-drying separated solid.    USE - Method for extracting 99% rebaudioside A from Stevia (claimed).    ADVANTAGE - The method is simple. It has low device requirement and low energy consumption. It ensures high yield and stable purity.
NOVELTY - Soil improvement agent comprises 100-150 pts. wt. bentonite, 3-5 pts. wt. synergistic agent, 5-10 pts. wt. water, 20-35 pts. wt. corn straw, and 10-35 pts. wt. biocontrol bacteria.    USE - Soil improvement agent used for preventing and killing pests, and preventing and treating diseases of greenhouse vegetables (claimed).    ADVANTAGE - The preparation of soil improvement agent is simple, has low manufacturing cost, high efficiency, no toxicity, no environment pollution and no public hazard, is provided with antibacterial test, promotes quick composting, prolongs life service, improves soil and plant water retention capacity and increases soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of soil, comprising dry crushing low grade bentonite, purifying, separation impurities and montmorillonite to obtain 600-800 mesh high purity bentonite powder with more than 80% montmorillonite content, mixing corn straw, crushing to 600-800 mesh, fully dissolving synergistic agent in water, spraying on bentonite-corn straw mixture, stirring for 3-5 days, sterilizing, putting in sterile containers to obtain base material, spraying biocontrol bacteria, uniformly stirring, placing at 20-30 degrees C environment, growing for 20-30 hours, embedding, fixing, granulating to 5-10 mm diameter with 10-15 mm length cylindrical particle, and drying to a water content of 4-7%.
NOVELTY - The method involves collecting triglyceride containing oil to dehydrate. Oil filled in a fixed bed reactor. Pressure is 20 to 80bar. Temperature is 200 to 500 degree Celsius. Oil is reacted with hydrogen to directly generate biological diesel oil, water, propane, methane, carbon dioxide and carbon monoxide gas-liquid mixture. A catalyst is a load type cobalt catalyst or cobalt-nickel alloy catalyst. Gas-liquid mixture is separated into a liquid phase product and a gas phase product in a gas-liquid separating device.    USE - Biodiesel producing method for a triglyceride.    ADVANTAGE - The method enables avoiding the generation of environment pollution with simple technical process, clean and environment-friendly, and low energy consumption. The method enables increasing fuel demand with better economic and social benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biodiesel producing method. '(Drawing includes non-English language text)'
NOVELTY - The furnace has a feeding device connected with an air cylinder body. A base end is installed with a gasification agent air inlet device that is connected with a cylindrical furnace body. Two ends of a kiln with the cylindrical furnace body are provided with a rotary kiln sealing device. A discharging device is connected with a slag conveying device. A lower end of the kiln furnace is provided with a smoke inlet tube. A high end of the kiln is provided with a kiln cylinder outlet flue. A tailings burner nozzle of a burner is connected to the kiln of a kiln smoke inlet.    USE - Combustion material recycling switch composite furnace.    ADVANTAGE - The furnace provides stable gasification process. The furnace has small lower waste bearing upper layer garbage air outlet pressure. The furnace has rapid reaction, garbage drying efficiency and production efficiency, and is stable and high in efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a combustion material recycling switch composite furnace.
NOVELTY - The device has two sleeves (2, 8) connected with a cold water replenishing pipe (4) and an outer wall of a cyclone dust collector (6). Upper and lower parts of two steam outlets (1, 7) are connected with the sleeves. An inner wall is welded with two fins (3, 9). Each upper part of each steam outlet is connected to a spiral feeder machine (14) and a lower end of a jacket (13). The lower end of the jacket is provided with a water outlet (12).    USE - Dust collecting pre-heating fuel device for a fluidization bed biomass gasification furnace.    ADVANTAGE - The device is simple and compact in structure and convenient to manufacture and assemble. The device effectively heats to-be-used fuel so as to achieve better waste heat recycling effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a dust collecting pre-heating fuel device.    Steam outlets (1,7)    Sleeves (2,8)    Fins (3,9)    Cold water replenishing pipe (4)    Cyclone dust collector (6)    Water outlet (12)    Jacket (13)    Spiral feeder machine (14)
NOVELTY - The furnace has a gasification agent air inlet device connected with a cylindrical furnace body that is provided with a sealing device. A lower end of the cylindrical furnace body is provided with a slag discharging device. A discharging device is connected with a slag conveying device. The conveying device is connected with the slag. A lower end of a kiln furnace is provided with a smoke inlet tube. A high end of the kiln is provided with a kiln cylinder outlet flue. A tailing burner nozzle of a burner is connected to the kiln of a kiln smoke inlet.    USE - Plastic resources continuous gasification cracking multi-effect furnace.    ADVANTAGE - The furnace has complete processing.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a plastic resources continuous gasification cracking multi-effect furnace.
NOVELTY - This utility model claims a kind of straw nutritional fermenting transforming agent particle, comprising agent layer, a protective film, a starch layer, the agent layer is provided with a layer of protective film and the protective film is set with starch layer. This utility model is the one can be used as a kind of crop straw firewood transform is made of high quality animal feed and organic fertilizer to replace a large amount of complete feed, improve the breeding benefit and fermented feed time is short, only in 5-8 hours, 15-30 hours to complete fermentation and can be directly used, the transforming agent into the straw mixture to be fermented according to ratio, the time for more than 3 days is capable of complete fermentation, it can be directly used for greenhouse and field fertilizing, the straw, the food of livestock and poultry are capable of feeding, promoting digestion and absorption, long, a fat, meat fresh.
NOVELTY - Method of restoring, roasting, purifying, and extracting manganese and iron involves adding manganese slag and coal gangue slag to rotary kiln, carrying out high-temperature roasting under negative pressure, introducing gases to multi-pipe dedusting and tail gas treatment system, carrying out scavenging processes of ball-milling, and carrying out primary low-intensity magnetic separation process, secondary high-intensity magnetic separation process and tertiary high-intensity magnetic separation process on the material.    USE - Method of restoring, roasting, purifying, and extracting manganese and iron used for manufacturing ammonium sulfate as agricultural fertilizer (claimed), and used for building material.    ADVANTAGE - The manganese and iron are environmentally-friendly manufactured with reduced impurities and reduced energy consumption, by simple process.    DETAILED DESCRIPTION - Method of restoring, roasting, purifying, and extracting manganese and iron involves adding manganese slag and coal gangue slag into a rotary kiln, carrying out high-temperature roasting under high-temperature environment inside the rotary kiln and negative pressure of -0.012 to -0.019, such that sulfur, ammonia and nitrogen compounds are decomposed into gaseous state, introducing the gases into a multi-pipe dedusting and tail gas treatment system in which smoke is removed, carrying out scavenging processes of ball-milling, and carrying out primary low-intensity magnetic separation process, secondary high-intensity magnetic separation process and tertiary high-intensity magnetic separation process on the material which is restored by high temperature of the rotary kiln to obtain an iron product, a manganese product and ultra-fine quartz powder. The content of coal gangue slag is 5-10%.
NOVELTY - Preparation of hydrogen evolution cathode material involves surface-treating active metal, performing constant temperature treatment on a prepared precursor reaction solution of cathode active material at -20 degrees C to 0 degrees C, placing the surface-treated active metal in the precursor reaction solution, plating the active metal at -20 degrees C to 0 degrees C, removing active metal, washing and blow-drying.    USE - Low temperature preparation of hydrogen evolution cathode material (claimed).    ADVANTAGE - The cathode material having improved hydrogen evolution property is economically prepared.
NOVELTY - Synthesizing DL-menthol and its stereoisomers comprises (i) carrying out catalytic hydrogenation of compounds containing at least one double bond, an oxygen atom substituted at 3-position, and having a menthane carbon skeleton e.g. thymol, DL-menthol and/or its stereoisomers using complex Raney nickel catalyst; and (ii) carrying out vacuum distillation in a packed tower with a number of theoretical plates of 60-100 to obtain DL-menthol, DL-neomenthol and DL-iso-menthol, where the reaction is carried out under pressure of 0.1-3.5 MPa and temperature of 50-200 degrees C.    USE - The method is useful for synthesizing DL-menthol and its stereoisomers (claimed).    ADVANTAGE - The method: does not use water or an organic solvent, and ensures the reutilization of catalyst; rarely produces hydroxy byproducts and hence prevents the generation of hydrocarbons which are not used repeatedly; is carried out under mild operating conditions low pressure and temperature, and does not require reaction equipment; reduces the cost, is safe and environmentally friendly; and has thymol conversion rate of 99.99% and produces yield of more than 99%.
NOVELTY - An oxygen tube belongs to medical goods field, so as to protect environment and save resource. The technical solution comprises a cylinder body, a hydrogen and oxygen pipe, an inner cylinder for storing a proper amount of water, is set with the electrode. By using said structure, when using, through the electrode, and decomposing water, a hydrogen collecting hydrogen gas is oxygen and hydrogen, oxygen pipe, it can save the hydrogen used for the other. So it can heat preservation obtain good oxygen, protecting environment, saving resource and saves cost.
NOVELTY - An enzyme biological fuel cell electrode preparation method involves utilizing carbon paper as an electrode base plate, and sodium alginate/carbon nanotube/chitosan composite immobilized enzyme.    USE - Method for manufacturing enzyme biological fuel cell electrode that is utilized for manufacturing double-room enzyme biological fuel cell (claimed).    ADVANTAGE - The method enables manufacturing enzyme biological fuel cell electrode with better biological compatibility and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a double-room enzyme biological fuel cell comprising anode and cathode.
NOVELTY - The cell has a lead wire leading electric energy generated in a fuel cell for external electrical appliances. One end of an outlet pipe is connected with an upper cover plate of the fuel cell. A middle piece of the outlet pipe is connected with a speed regulating valve. An outlet of a liquid storage tank is placed inside a sealing ring after the sealing ring is connected with an upper cover plate of the fuel cell. The outlet of the liquid storage tank is connected with a runner inlet on the upper cover plate of the fuel cell through the sealing ring.    USE - Self-driven non-membrane type micro-fluid fuel cell.    ADVANTAGE - The cell improves energy net output of the fuel cell by 10 % and utilization efficiency and reduces manufacturing, installation and operation costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a Self-driven non-membrane type micro-fluid fuel cell.
NOVELTY - Nutrient repairing agent comprises solid module repairing agent comprises 40-60 pts. wt. active humic acid, 1-3 pts. wt. bonding agent, 10-30 pts. wt. water retention agent, 1.5 pts. wt. nitrogen fertilizer, 1.2 pts. wt. phosphate fertilizers, 0.3 pts. wt. potash fertilizers, and 1-5 pts. wt. fly ash; or 30-60 pts. wt. active humic acid, 1-30 pts. wt. cellulose, 1-5 pts. wt. film-forming agent, 10-30 pts. wt. microbial strains, 0.7 pts. wt. nitrogenous fertilizer, 0.5 pts. wt. phosphate fertilizers, and 0.1 pts. wt. potash fertilizers.    USE - Nutrient repairing agent used for desertified soil restoration (claimed).    ADVANTAGE - The repair agent has fixing and water retention effects which can be optimized by adjusting the raw material proportions according to different regions and levels of desertification of soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of solid mold repair agent comprising pulverizing active humic acid, adding proportioned raw materials, mixing, subjecting to plasma chemical reaction for 1-2 minutes, compression molding, and low temperature drying at 70-80 degrees C; and    (2) preparation of liquid coating repair agent comprising pulverizing active humic acid, adding proportioned raw materials, mixing, subjecting to plasma chemical reaction for 1-2 minutes, screening, and low temperature drying at 70-80 degrees C.
NOVELTY - The method involves performing hydrogenation and deoxygenation to obtain alkane under the usage of plant oil and/or animal fat, based on hydrogenation isomerization. The alkane and hydrogen are combined with the hydrogenation isomerization catalyst in the hydro-refining condition to obtain the jet fuel. The hydrogenation isomerization catalyst contains carrier and metal active component with silicon, phosphorus and aluminum molecular sieve. A metal active component contains a group of metal.    USE - Method for producing jet fuel.    ADVANTAGE - The alkane and hydrogen are combined with the hydrogenation isomerization catalyst in the hydro-refining condition to produce the jet fuel in a stable manner.
NOVELTY - A cephalosporin C acylase mutant having specific amino acid sequence, or a sequence by replacing, deleting or adding at least one amino acid and having the same function of the sequence derived from the amino acid sequence, is new.    USE - For preparing 7-aminocephalosporanic acid (claimed).    ADVANTAGE - The mutant has high conversion rate i.e. 99%. The process has high yield i.e. 96%; and is environment-friendly.    DETAILED DESCRIPTION - A cephalosporin C acylase mutant having amino acid sequence containing 707 amino acids (SEQ ID NO: 4), as given in the specification, or a sequence by replacing, deleting or adding at least one amino acid and having the same function of the (SEQ ID NO: 4) derived from the amino acid sequence, is new. INDEPENDENT CLAIMS are included for the following:    (1) new cephalosporin C acylase mutant encoding gene having nucleotide sequence containing 2325 nucleotide base pairs (SEQ ID NO: 3);    (2) carrier comprising the gene;    (3) new vector comprising the gene; and    (4) preparation of the cephalosporin C acylase mutant.
NOVELTY - The machine has a fixed bed gasification furnace (4) with a gas outlet (8) set on top of a feeding hopper (1) of a furnace body. Bottom of the furnace body is formed with a gasification agent inlet. The gasification agent inlet is connected with an air outlet on the furnace body along vertical direction. The gas outlet is inclined upwards with an inertial dust separator (11) of a settling chamber (10). The settling chamber is connected with the gas outlet, and the combustion device is connected with a heat-using device. The device and the settling chamber are connected with each other.    USE - Biomass press block gasification combustion machine.    ADVANTAGE - The machine improves biomass fuel gasification efficiency, and reduces energy loss during gasification process of biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass press block gasification combustion machine.    Feeding hopper (1)    Fixed bed gasification furnace (4)    Gas outlet (8)    Settling chamber (10)    Inertial dust separator (11)
NOVELTY - The device has a tank body provided with a bottom end opening and a lower side that is provided with an air outlet and an air inlet. The tank body is arranged vertical to a spray thrower. A water supply branch pipe includes an end passing through an upper cover. The spray thrower is connected with the water supply pipe. A water pump includes a water outlet end that is connected with a water supply pipe, and a water inlet end connected with the water tank.    USE - Biomass fuel gas purifying device for an internal combustion engine.    ADVANTAGE - The device is simple in structure with better purifying effect and can be manufactured in an inexpensive manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass fuel gas purifying device.
NOVELTY - Bonsai Osmanthus fragrans cultivation disc matrix comprises organic material and mineral material at volume ratio of 9:1-3:7. The mineral material comprises perlite and/or vermiculite. The organic material is vermicompost, peat or harmless completely fermented manure. The peat has water content of not greater than 25 wt.%. The organic matter is present at not less than 60 wt.%.    USE - Bonsai Osmanthus fragrans cultivation disc matrix.    ADVANTAGE - The cultivation matrix can quickly cultivate the bonsai Osmanthus fragrans at cuttage of 40 days and cuttage rooting rate of 80-90%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of the disc matrix in bonsai Osmanthus fragrans cultivation, comprising soaking 2-3 cm cuttage seedling base in 50-200 mg/L rooting promoting agent for 2 hours and then inserting into the disc matrix at depth of 2/3 of the length of branches, keeping temperature at 20-30 degrees C and relative humidity at not less than 70% for 60 days, transplanting to big container, and spraying seedling leaf surface with fertilizer once every 10 days. The root promoting agent comprises green growth regulator (GGR), 6-benzyladenine (6-BA) and indolebutyric acid (IBA).
NOVELTY - Doubling maize haploid is carried out by treating corn haploid with herbicide to obtain corn diploid. The herbicide comprises amiprophos-methyl, metolachlor or trifluralin.    USE - Method for doubling maize haploid (claimed).    ADVANTAGE - The method is simple to perform, has small pollution to the environment, low toxicity, low and easily degradable residue, and high efficiency. The total doubling rate can reach to more than 27.9%, and the seed soaking processing rate is more than 17.9%, while rate of emergence is lower than that of colchicine. Further, the method is suitable for large-scale breeding of corn haploid.
NOVELTY - A thermostatic atomizing auxiliary agent comprises 0.5-40 wt.% surface active agent, 0.5-10 wt.% flame retardant, and balance vegetable oil or its ester.    USE - Thermostatic atomizing auxiliary agent used in pesticide preparation or foliar fertilizer preparation (claimed).    ADVANTAGE - The auxiliary agent has synergistic effect and is safe to use by hot mist diffusion and using low drift and ultra-low volume spraying machine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using thermostatic atomizing auxiliary agent, comprising directly adding the auxiliary agent into pesticide or foliar fertilizer, or mixing with aqueous solution of agrochemical and fertilizer preparation.
NOVELTY - A double-layer reactor for producing hydrogen agent, wherein it is a double-layer structure, comprising a reaction container and used for collecting outer cover for hydrogen, outer cover are fixed together through the inner container, the top of the reactor and the reactor top cover and sealing, bottom of the reactor is set with outer cover O-shaped ring, inner end, outer cover is set with a sealing pad in the outer cover and the liner end part sealing part, is set with the waterproof ventilating film on the outer side inner container side wall is inclined for 1-30 degrees to the same direction. A reactor for preparing hydrogen agent and water to prepare high pure hydrogen, using water-proof ventilating film at outer side of layer, only allow penetrating hydrogen, water vapour is condensed into water collected in the inner and outer interlayer, so as to not enter the fuel cell, which improves the safety.
NOVELTY - This utility model claims a water source heat pump and sludge digestion integrated system is provided with a sludge gravity concentration tank, a water pump, a water source heat pump machine set, water heating device, a sludge digestion tank and biogas generator, the secondary treatment water pump is connected with the water inlet, the water outlet is connected with the filter and the water source heat pump machine set, a hot water outlet and a mud-water heat exchanger of the heat pump machine set is connected with the sludge gravity concentration tank and a sludge sewage treatment device, the inlet of the heat exchanger outlet and water, the sludge and the sludge digestion tank after being heated, marsh gas outlet of the sludge digestion tank by the desulfurizing tower, an air storage cabinet and marsh gas supercharger with the gas supply pipe of the marsh gas generator, marsh gas generator heat cement recovery device of residual-heat water heating device is a hot water inlet. This utility model is suitable for sewage treatment plant in water, heat and energy comprehensive utilization, which greatly improves the energy saving and emission reduction and sludge treatment effect, energy-saving and environment-friendly effect is very obvious.
NOVELTY - This utility model claims a kind of acetaminophen refined processing device. The processing device comprises a crystallizing tank is connected with outlet, feeding and stirring jar capable of advancing the material produced from the crystallizing tank with the feeding tank is connected with the lower discharging centrifuge; charging device is set on the lower discharging centrifuge to lower part, wherein the lower discharging centrifuge for centrifuging the unloading assistant device for bulk material to the loading device is connected with the charging device, drying the material from the feeding device of the vibration fluidized bed, and is connected with the vibration fluidized bed, crushing the material introduced by the vibration of the vibration fluidized bed. This utility model is a processing device for realizing the continuous production and clean production, and avoids the cross pollution, but also reduces the labour intensity of the worker, saves labour, and improves the batch of the product, reduces the test cost.
NOVELTY - This utility model claims a kind of using triamine tail gas joint of urea, wherein the triamine tail gas input pipe and a dimethyl liquid tube junction of pump input and in turn introduce methylamine condenser II, methylamine condenser I, methylamine; methylamine one end of which is connected to a first pump inlet pipe, one end of which is connected to the first steam heater heat utilization section, then orderly connected with a cooler II, a cooler I, a sucking tower, a sucking tower discharging methylamine to go no the first pump inlet pipe. A desalted water tube through hot water circulating pump are orderly connected with methylamine condenser I, methylamine condenser II, methylamine condenser II are respectively connected to the hot water circulating pump and a condensing liquid. The character is: the triamine tail gas with the dimethyl liquid manifold primary urea device to prepare methylamine recovery into urea-segment system, uses the original urea device joint urea, recovery of carbon dioxide and ammonia in triamine tail gas, protects the environment, but also increase the urea production and has obvious economic benefit.
NOVELTY - A kind of laboratory with biological carbon carbonization furnace, comprising a feeding tank, heating steel pipe, a resistance wire, a temperature sensor, a shell and a cover, wherein the feeding tank is a hollow steel structure of spring power assembly and upper end is opened and the bottom is sealed, heating steel pipe is an opening at the upper end the lower end of the cylindrical structure, a feeding tank is inserted into the heating steel pipe, heating layer is arranged outside the heating steel pipe, heating layer is a heating resistance wire is wound with insulating porcelain bead, a heating layer is covered heat insulating layer, is provided with a temperature sensor and the heating layer and the heat insulating layer, and the cover is provided with an air outlet channel, the cover is fixed with the shell. This utility model has the advantages of preparing process is reliable and safe, efficiency is high, the cost is low, it saves energy, it can meet the laboratory research of the bio-char.
NOVELTY - Gasification system is a kind of woody biomass energy, comprising a pyrolysis device, pyrolysis device is connected with the condensing device, the condensing device is connected with the gas collecting device. This utility model has simple structure, convenient operation and small construction of the gasification system, free addressing is flexible, the natural environment of dependence. Raw material source is wide, it not only reduces the environment pollution, but also can produce useful energy, supply people daily life.
NOVELTY - This utility model claims a biomass gasification system, comprising a multi-section fixed bed biomass gasification furnace, the multi-section fixed bed biomass gasification furnace comprises a vertical furnace body provided with a furnace body is located at the bottom of conical hopper-shaped tail ash section and at least two gas section on the tail ash section, the at least two gas generating section vertically arranged and connected end to end, the tail ash section and is located between the gas section of the fire grate is set at the bottom side of each gas section are provided with a fuel gas outlet, a gas outlet is connected with a gas branch pipelines, a plurality of fuel gas branch pipeline connected to a gas main pipe, tail section of the ash outlet is set at the bottom, the side part of the tail ash. is provided with an air inlet, wherein the upper part of the gas section of the top side or top end is provided with a fuel inlet. This utility model has compact structure of the gasification furnace of biomass raw material water adaptability is high, breaks through the normal gasification furnace of strict requirement of a part, the produced gas properties can control can be adjusted to adapt to different users need a biomass fuel gas, because suitable for multi-section gas production process, the gasification efficiency is higher than normal gasification furnace.
NOVELTY - This utility model claims a self-drying type biomass gasification system, comprising a self-drying type fixed bed biomass gasification furnace, wherein the drying type fixed bed biomass gasification furnace comprises a vertical set with the furnace body, the furnace body is located at the bottom of a conical hopper-shaped tail ash section and a reaction section on the tail ash section, tail ash section and reaction section is provided with a fire grate, the side part of the bottom of the section is provided with a tail ash outlet, the tail ash is equipped with an air inlet, and the reaction period is on the side surface of upper part or top end is provided with a fuel inlet, the self-drying type fixed bed biomass gasification furnace further comprises a feeding device and a blanking pipe, falling pipe is inserted into the fuel inlet, the top end is closed, the side part of the blanking pipe of the blanking pipe is provided with a feeding port, the tail end of the feeding device; blanking pipe of the side part or top is further provided with a circulating gas outlet, said circulating gas outlet is connected with a gas return pipe, the side part of the tail ash section is provided with a reflux inlet, and the other one end of the gas return pipe is connected to the reflux inlet of tail ash.
NOVELTY - This utility model claims a kind of automatic ash discharging biomass gasification furnace, the air outlet hole, a wind pipe, a nozzle, a filter barrel, a barrel cover, a sealing groove, the gas circulating groove, ash discharging plug board, ash discharging box chute, ash discharging box, a bracket, a blower; The upper end of the material barrel with a barrel cover, a sealing groove and the barrel cover are connected, the gas circulating slot is located on the air outlet hole, an air filter located on one end is fixed with the material barrel, and the other end of the blower, wind pipe is connected with the centre of the lower part and discharging the filter inserted plate is connected with the ash box is fixed on the bracket, a dust box with ash discharging plug plate, wherein two sides of the ash discharging box is connected with the sliding groove. It has scientific and reasonable design, convenient and quick operation, no pollution, strong safety, complete combustion, stable and durable, it is substituted by the biomass is the ideal product of the gasification furnace as raw material.
NOVELTY - Furnace before the utility model claims a multi-level furnace front feeding device for biomass gasification furnace, the side wall of the biomass gasification furnace is provided with a material inlet, a multi-level feeding device at least comprises the first level feeding device, a feeding device, a first level feeding device comprises a feeding port on the front part, and the tail end of the discharging port, the first level feeding device, feeding device arranged up and down, feeding port of the last stage of the feeding device of the first level feeding device is directly connected, or by a one-stage or multiple-stage feeding port of a feeding device with the last feeding device in a first stage and last stage feeding device and feeding device is indirectly connected with the first level feeding device and the tail end of each of the middle feeding device is provided with a closed box, a first stage feeding device and the discharging port of each a middle material conveying device is connected with the feeding port connected with the feed region and in the next feeding device, the discharging port of the final feeding device is connected to the material inlet of the biomass gasification furnace.
NOVELTY - A Bacillus subtilis PGPR-802 deposited as CGMCC No. 6048, is new.    USE - The B.subtilis is useful in microbial fertilizer used for apple and tomato (all claimed).    ADVANTAGE - The microbial fertilizer increases yield of tomato by 10.4% and yield of apple by 7.3%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial fertilizer comprising 10% B.subtilis fermented bacterial liquid, 40% humic acid, and 50% activated sludge powder; (2) B.subtilis fermented bacterial liquid obtained by culturing B.subtilis at 35 degrees C in medium comprising 0.5% peptone, 0.5% yeast, 2% glucose, 1% corn steep liquor and 0.2% sodium chloride and adjusting pH to 7.5 to produce spores; (3) method for preparing the microbial fertilizer, which involves uniformly mixing and stirring humic acid with activated sludge in a weight ratio of 4:5, subjecting the mixture to disk granulation, spraying the B.subtilis fermented bacterial liquid into the granules, and drying the granules at lower than 70 degrees C.
NOVELTY - The reactor has tank cover (3) that is connected with a reaction tank (1) to form a sealing cavity (15). The reaction tank is provided with three-phase separator (5). The reaction tank is connected with the inner wall of a bracket (6), and grip is installed on the bracket on an inclined plane array unit (7). The inclined plane array unit is parallely connected with the inclined plate and horizontal reaction tank. Adjacent inclined plates are reserved through inclined plane array unit on lower surface of inclined flow passage, and array unit is comprised of sloping plate.    USE - Sewage reactor such as upflow anaerobic sludge blanket (UASB) for bio-waste water treatment.    ADVANTAGE - The reactor is featured with simple structure, and settlement effect of sludge can be improved. The scale production can be facilitated, and the transportation and mounting can be easily achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage reactor.    Reaction tank (1)    Tank cover (3)    Sealing cavity (5)    Bracket (6)    Inclined plate array unit (7)    Sealing cavity (15)
NOVELTY - A Bacillus licheniformis BL-1 strain having cellulase activity and having phosphorus and potassium dissolving function deposited under preservation number CCTCC No. 2012457, is new.    USE - In probiotic composition for preparation of ethanol fuel from industry waste active sludge; and for preparing organic fertilizer for forest or landscape nursery (claimed).    ADVANTAGE - The Bacillus licheniformis strain has high cellulase activity; provides good phosphorus and potassium dissolving function; avoids the environment pollution; provides simple processing technique; has low cost; and is good for ecological protection and agriculture sustainable development.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a probiotic composition in dry powder form comprising yeast, Bacillus subtilis, Bacillus licheniformis BL-1, Bacillus megaterium, Bacillus mucilaginosus and Azotobacter chroococcum in ratio of 10:1:2:1:1:10.
NOVELTY - This utility model claims a kind of sewage processing biological the wire strengthening device, comprising a microorganism culture tank is provided with a water outlet and a drain valve, a microorganism culture tank is provided with a , and the microorganism culture tank is further provided with a through microorganism culture tank wall of the pH meter and the temperature sensor in the microorganism culture tank is provided with an aeration device, the aeration device is connected with a fan through a pipeline, the fan is connected with an air filtering and heating sterilizer, an electric control device is an aeration device, a fan and an air filtering and heating for providing electric energy. The advantages of this utility model lie in: the microorganism feeding technology, the microorganism adding technology can realize the wire to avoid later remediation of microorganism and capable of adding a propagation of high density, so that microbial action time extend the adaptive period, fast effect, no need the continuous complete.
NOVELTY - This utility model claims a secondary anaerobic fermentation for restaurant and kitchen rubbish device, comprising a heating tank, the first-stage anaerobic reaction tank and two-stage anaerobic reaction tank, the anaerobic reaction tank and the air outlet of the two-stage anaerobic reaction tank are connected with a marsh gas collecting tank, the outlet of the two-stage anaerobic reaction tank is connected with a slag collecting tank, and the first-stage anaerobic reaction tank is connected with the two-stage anaerobic reaction tank is provided with a cooling tank and cooling water tank, cooling tank and the cold water tank are connected with each other, the inlet of the cooling tank is connected with the first-stage anaerobic reaction tank, the outlet of the cooling tank is connected with the inlet of two-stage anaerobic reaction tank, the cooling tank is provided with a hot water outlet, the hot water outlet is on the lower part of the cooling tank. This utility model adopts said structure, wherein the kitchen garbage treatment process, it can make the kitchen garbage decomposing is more complete, marsh gas generating rate is higher.
NOVELTY - Wettable powder comprises 1-4 wt.% cypermethrin, 0.2-0.8 wt.% emamectin benzoate, 0.5-5 wt.% wetting agent, 1-5 wt.% dispersing agent, 0.5-5 wt.% synergistic agent and filler (make up to 100 wt.%).    USE - The wettable powder is useful for preventing and treating pests.    ADVANTAGE - The wettable powder has simple preparation process, strong synergistic effect and low production cost, reduces environmental pollution, exhibits good effect under a very low dosage, does not harm beneficial insects in the process of preventing and controlling pests, enlarges the insecticidal spectrum, reduces the human and animal toxicity, and is convenient and safe to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the wettable powder, comprising crushing cypermethrin, emamectin benzoate, wetting agent, dispersing agent, synergistic agent and filler into 80-200 meshes, and uniformly mixing and stirring to obtain the wettable powder.
NOVELTY - A method for processing pig farm waste water of double-cylinder type microbial fuel cell experiment platform, comprising a cation exchange membrane and graphite carbon felt, a load R, carbon fibre protofilament cylinder outer wall of the magnetic stirrer, distributor, aerator, an anode chamber, a cathode chamber, an aeration pipe, a calomel electrode, a rubber plug, a power clamp, carbon fibre strand, a data collector, a notebook computer. A battery of pig farm waste water organic removing rate can reach the traditional anaerobic technique organic removing the higher level, at the same time, it can reduce the reactor cost and improves the power generating efficiency.
NOVELTY - Preparing anti-moisture coating of capsule comprises taking traditional Chinese medicine dry extract and silymarin flavonoids, setting slurry mixing, granulating knife at low speed and then sieving through 60 meshes sieve and then mixing for 15 minutes, spraying the mixed material in a drying granulating machine and then preheating, spraying the coating liquid, spraying into a coating liquid and then granulating and then drying, and tidying the coated granules and then filling.    USE - The method is useful for preparing anti-moisture coating of capsule, which is useful for calming liver (claimed).    ADVANTAGE - The method allows preparation of the anti-moisture coating of capsule with improved stable quality and yield in eco-friendly manner.    DETAILED DESCRIPTION - Preparing anti-moisture coating of capsule comprises taking 220 g of traditional Chinese medicine dry extract and 30 g of silymarin flavonoid, setting slurry mixing at low speed for 20 minutes, granulating knife at low speed and then sieving through 60 meshes sieve and then mixing for 15 minutes, spraying the mixed material in a drying granulating machine and then preheating for 5 minutes, spraying the coating liquid at a flow rate of 35-5 ml/minutes, spraying into a coating liquid (1.5-2%) and then granulating at main air passage temperature to 80-70 degrees C and auxiliary air channel temperature to 70 degrees C, controlling the temperature to 40-45 degrees C, a firstly atomization pressure of 0.15-0.20 MPa and secondarily atomization pressure of 0.4-0.45 MPa and a spray gun of 40 Hz and then drying for 2-30 minutes, and tidying the coated granules having an average grain diameter of 16 meshes and then filling.
NOVELTY - A butadiene tail gas hydrogenation device comprises hydrogenation reactor (13), gas-liquid separating tank (15), absorption tower (11), compressor (12), condenser, compressor discharge tank (14), tower line pipe combination and hydrogenation reactor inlet.    USE - Butadiene tail gas hydrogenation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of butadiene tail gas hydrogenation device.    Absorption tower (11)    Compressor (12)    Hydrogenation reactor (13)    Compressor discharge tank (14)    Gas-liquid separating tank (15)
NOVELTY - Hydrogenation device comprises hydrogenation reactor and product tank. The hydrogenation reactor comprises diluting tank, compressor, condenser and gas-liquid separating tank. The diluting tank is sequentially connecting with compressor, condenser and gas-liquid separating tank which is connected with the hydrogenation reactor. The hydrogenation reactor is connected with the product tank outlet pipeline which is divided into hydrogenation reactor inlet, diluting tank and reactor outlet.    USE - Hydrogenation device is used for hydrogenation method (claimed).    ADVANTAGE - The hydrogenation method is carried out using hydrogenation device with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogenation method, which involves using hydrogenation device in which tail gas is diluted, compressing, condensing and subjecting resultant product to hydrogenation reactor.
NOVELTY - Preparing vermiculite-containing nickel-based catalyst, comprises (a) preparing nickel containing solution and impregnating for 6-24 hours, (b) drying the impregnated solution at a temperature of 80-120 degrees C, and calcining the solution at 400-1000 degrees C for 2-10 hours, and then (c) reducing a mixed gas of hydrogen gas and nitrogen gas at 300-800 degrees C.    USE - The method is useful for preparing vermiculite-containing nickel-based catalyst, which is useful for catalytically reforming for preparing natural gas or methane (claimed).    ADVANTAGE - The method is suitable for large scale production, and provides nickel-based catalyst with high catalytic activity and good stability.
NOVELTY - A semiconductor photocatalyst comprises cadmium selenide (I).    USE - Semiconductor photocatalyst is used for photocatalytic reforming of biomass and its derivative for preparing hydrogen (all claimed).    ADVANTAGE - The high-activity semiconductor photocatalyst is economical. The hydrogen is efficiently and economically preparation using the semiconductor photocatalyst by simple method, without performing calcination and without using co-catalysts e.g. platinum and rhodium, and with improved catalytic efficiency.    DETAILED DESCRIPTION - A semiconductor photocatalyst comprises cadmium selenide of formula: CdAxSe (I).    A=cobalt, nickel or iron;and    x=0.02-1.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of semiconductor photocatalyst, which involves adding water-soluble cadmium selenide quantum dot in reactor, then, adding cobalt, nickel or iron salt or complex solution into the reactor to obtain mixed solution (A), adding aqueous solution of biomass or its derivative to mixed solution (A) to obtain solution (B), adjusting pH of mixed solution (B) to 3-10 to obtain mixed solution (C), placing solution (C) in inert gas or vacuum atmosphere, and processing using ultraviolet light and/or visible light;    (2) system used for preparing hydrogen by photocatalytic reforming of biomass and its derivative using semiconductor photocatalyst, which contains aqueous solution of biomass and its derivatives, water-soluble cadmium selenide quantum dot, and cobalt, nickel or iron salt or complex solution. The pH of the system is 3-10. In the system, photocatalysis is carried out under ultraviolet light and/or visible light; and    (3) method of photochemical catalysis reforming of biomass and its derivative for preparing hydrogen using semiconductor photocatalyst.
NOVELTY - Aluminum powder and nickel powder are mixed, to obtain mixture. The mixture is cold-pressed to form compact. The compact is heated under vacuum at 1x 102 Pa to 1x 103 Pa, heated at 350-500 degrees C for 60-90 minutes, the temperature is raised to 700-950 degrees C for 30-120 minutes and cooled to room temperature to obtain electrode material. Nickel powder and aluminum powder has particle diameter of 1-15 mu m. The content of nickel powder and aluminum powder with respect to total content of nickel powder and aluminum powder is 80-95 wt.%, and 5-20 wt.%, respectively.    USE - Preparation of electrode material used for electrolyzing water for producing hydrogen.    ADVANTAGE - The method economically provides electrode material having uniform pore size distribution, high surface area, high activity, catalytic efficiency, and durability, by a simple process.
NOVELTY - A two-stage solid-liquid bi-phase anaerobic fermentation circulation system for producing marsh gas comprises first stage reactor (1), a buffer tank (2) and second stage reactor (3). The buffer tank is set on a one side of the first and second stage reactor. The buffer tank and second stage reactor is provided with marsh gas outlet (15). The first stage reactor is further provided with a mechanical stirrer (6). The second stage reactor is provided with an active sludge bed (12).    USE - As two-stage solid-liquid bi-phase anaerobic fermentation circulation system for producing marsh gas (claimed).    ADVANTAGE - The present system has simple structure; is easy to operate; has low cost; produces marsh gas with high yield; and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing marsh gas by using the two-stage solid-liquid bi-phase anaerobic fermentation circulation system involving adding organic waste into the first stage reactor and second stage reactor, mixing it, subjecting to fermentation process to produce marsh gas, carrying solid-liquid separation, then using the liquid obtained into the second stage reactor as the raw material gas; circulating the liquid phase in the whole system, and solid phase into the corresponding reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of two-stage solid-liquid bi-phase anaerobic fermentation circulation system for producing marsh gas.    First stage reactor (1)    Buffer tank (2)    Second stage reactor (3)    Mechanical stirrer (6)    Active sludge bed (12)    Marsh gas outlet (15)
NOVELTY - Removal of ammonia-nitrogen from ammonia-nitrogen-containing water involves adding high-efficient powdered ammonia-nitrogen adsorbent which is high-grade powdered modified zeolite using self-measuring device according to ammonia-nitrogen content, mixing powdered ammonia-nitrogen adsorbent with water containing ammonia-nitrogen, fully stirring, absorbing heavy metal ion in obtained aqueous ammonia-nitrogen, rapidly precipitating, depositing saturated ammonia-nitrogen adsorbent, discharging, dehydrating obtained filter cake, pressing and drying into powder using drying device.    USE - Removal of ammonia-nitrogen from ammonia-nitrogen-containing water (claimed).    ADVANTAGE - The ammonia-nitrogen is economically removed by environmentally-friendly method, with reduced energy consumption.    DETAILED DESCRIPTION - Removal of ammonia-nitrogen from ammonia-nitrogen-containing water involves adding high-efficient powdered ammonia-nitrogen adsorbent which is high-grade powdered modified zeolite using self-measuring device according to ammonia-nitrogen content, mixing powdered ammonia-nitrogen adsorbent with water containing ammonia-nitrogen, fully stirring using stirring device, absorbing heavy metal ion in obtained aqueous ammonia-nitrogen, rapidly precipitating, depositing saturated ammonia-nitrogen adsorbent, discharging deposited saturated ammonia-nitrogen adsorbent, dehydrating obtained filter cake, pressing using pressing device and drying into powder using drying device.
NOVELTY - A controllable inner and outer double-circulating anaerobic reactor comprises water inlet pipe; primary reaction zone; three phase separator; secondary reaction area; water outlet pipe; gas-liquid separator; exhaust pipe; and lifting pipe set on first grade lift pipe of circulating reflux pump.    USE - A controllable inner and outer double-circulating anaerobic reactor.    ADVANTAGE - The reactor has improved adaptability, separation effect of biogas and sludge, and reaction efficiency and production.    DETAILED DESCRIPTION - A controllable inner and outer double-circulating anaerobic reactor comprises water inlet pipe; primary reaction zone, three-phase separator; secondary reaction area; water outlet pipe; gas-liquid separator; exhaust pipe; and lifting pipe set on first grade lift pipe of circulating reflux pump, and is provided with gas-liquid separator divided into two areas, e.g. first level three phase separator of lifting tube and second level three phase separator of lifting pipe which is separating chamber. The gas-liquid of two regions in gas-liquid separator is connected with external reflux pipe and with first grade lift pipe provided with a control circulating reflux pump, and sludge falling edge in first reaction region connected with first grade lift pipe corresponding to the gas-liquid separator.
NOVELTY - Preparation of fertilizer comprises soaking waste vegetable, fruit, chicken manure, egg shell, waste meat and bone in water, putting in jar, embedding pit, adding water, spraying Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate), sealing, fermenting and adding water to supernatant.    USE - Preparation of fertilizer used for home flowers.    ADVANTAGE - The fertilizer has easy preparation, convenient use and low cost.
NOVELTY - Preparation of microbial organic fertilizer comprises inoculating hyacinth residue organic fertilizer and composite microbial agents with water at ratio of 1:0.1-0.2, respectively.    USE - Preparation of microbial organic fertilizer.    ADVANTAGE - The fertilizer has low cost, convenient use, non-toxic, harmless and environment-friendly; improves continuous cropping, nourishes physical and chemical properties of soil through microorganism activity, thus, improving stress resistance of plant and reducing diseases and insect pests.
NOVELTY - A sugarcane organic compound fertilizer is prepared by following components: 10-15 wt.% of organic potassium solution, 3-7 wt.% of organic acid calcium chloride solution, 2-5 wt.% of zinc salt of organic acid solution, and 5-10 wt.% of organic acid as salt solution.    USE - As sugarcane organic compound fertilizer (claimed).    ADVANTAGE - The sugarcane organic compound fertilizer can provide comprehensive nutrition for crops, and high fertilizer effect; is safe and convenient; improves yield; and improves the quality of the high-quality fertilizer, which is suitable for area of sugar cane planting.
NOVELTY - Preparation of organic fertilizer comprises taking natural red soil, 150 pts. wt. straw powder, 100 pts. wt. green waste, 50 pts. wt. plant ash and 10 pts. wt. pig manure, crushing, mixing, stirring, piling, turning over every 5-7 consecutive days for 15 days, carrying out fermentation for 90 days, decomposing, adding 5.6% nitrogen, 1.3% phosphorus pentoxide and 1.8% potassium oxide and adjusting pH value of 7.5.    USE - Preparation of organic fertilizer.    ADVANTAGE - The method has simple technique and convenient manufacturing; inhibits plant diseases and insect pests and improves soil environment with pH value that is good for the growth of crops.
NOVELTY - Manufacture of organic fertilizer comprises stacking fresh livestock manure in loose bulk stacked fertilizer field with process air.    USE - Manufacture of organic fertilizer.    ADVANTAGE - The fertilizer reduces nitrogen loss.
NOVELTY - Utilization of crop straw resource comprises taking crop straw of 10-25 cm long, adding livestock excrement, mixing uniformly, adding water, controlling water content to 40-70%, adding 1-5 pts. wt. urea or 2-10 pts. wt. ammonium sulfate, stirring uniformly, stacking, adding water, keeping humidity at 40-60%, covering with plastic thin film, turning stack every 4-6 days for 8-12 days, inoculating edible fungi strain, stacking residue and edible fungi dreg uniformly, adding 15-45% livestock excrement, stirring, mixing uniformly and stacking for 5-8 days.    USE - Utilization of crop straw resource used for crop development of ecological agriculture (claimed).    ADVANTAGE - The method produces high quality organic fertilizer with no environmental pollution and improved soil fertility.
NOVELTY - Preparation of organic selenium-rich compound fertilizer comprises taking vinegar residue dreg, adding yeast, fermenting, balancing acid, adding additive and adding sodium selenite.    USE - Method for preparing organic selenium-rich compound fertilizer for improving soil quality (claimed).
NOVELTY - Recycling of vinegar residue comprises fermenting vinegar residue, adjusting pH, adding corn core and rice bran to obtain oyster mushroom culture medium, taking waste oyster mushroom culture medium, fermenting and adding urea, potassium sulfate, diammonium phosphate and other inorganic fertilizer to produce tea fertilizer.    USE - The vinegar residue is used for producing oyster mushroom culture medium and tea, green vegetable and fruit tree fertilizer (all claimed).    ADVANTAGE - The environment-friendly method reduces production cost and improves production efficiency.
NOVELTY - A green organic crop micro fertilizer comprises 1.5-2 wt.% biochemical fulvic acid, 20-25 wt.% potassium, 8-10 wt.% organic matter, 0.3-0.5 wt.% sodium humate/potassium humate and 0.3 wt.% carbendazim.    USE - As green organic crop micro fertilizer (claimed).    ADVANTAGE - The microbial inoculums can promote plant growth and improves the utilization ratio of fertilizer and inducing plant to generate adversity and anti-diseases ability to target pore size production. The method uses efficient biocontrol Trichoderma as strain, and cheap raw materials including straw powder, and bran as raw materials. The Trichoderma conidium preparation, which is produced through fermentation under aseptic condition which is approximate to good manufacturing practice (GMP), is used as a soil microbial agent and can be applied to controlling various plant soil-borne diseases. The method requires a tight loose cross-stacking method, which not only can reduce the time to maturity of organic fertilizer, but also can reduce the nitrogen loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing green organic crop micro fertilizer involving taking wheat bran as raw material, adding ammonium sulfate and water, sterilizing at high temperature and high pressure, inoculating with a liquid strain, changing into a bacterial solid fermentation starting tank and subjecting to thick-layer ventilation fermentation to prepare Trichoderma conidium fermentation culture, drying Trichoderma conidium fermentation culture, crushing, and adding conidium protecting agent to obtain the product.
NOVELTY - Complex-controlled long-acting slow release organic and inorganic biological fertilizer comprises 24-28 pts. wt. urea, 6-8 pts. wt. monoammonium phosphate, 6-8 pts. wt. potassium sulfate, 55-65 pts. wt. fermented chicken manure fertilizer, 7-9 pts. wt. carbon powder, 1.8-2.2 pts. wt. calcium superphosphate, 0.8-1.2 pts. wt. bentonite, and 1 pt. wt. solid microbial inoculum.    USE - Complex-controlled long-acting slow release organic and inorganic biological fertilizer.    DETAILED DESCRIPTION - Complex-controlled long-acting slow release organic and inorganic biological fertilizer comprises 24-28 pts. wt. urea, 6-8 pts. wt. monoammonium phosphate, 6-8 pts. wt. potassium sulfate, 55-65 pts. wt. fermented chicken manure fertilizer, 7-9 pts. wt. carbon powder, 1.8-2.2 pts. wt. calcium superphosphate, 0.8-1.2 pts. wt. bentonite, and 1 pt. wt. solid microbial inoculum. It is prepared by respectively crushing the raw materials, mixing and stirring urea, monoammonium phosphate, potassium sulfate, and charcoal powder, sieving to obtain particles having particle size of 1.5-2.5 mm, re-crushing the unqualified materials, adding 40% calcium superphosphate and 40% bentonite with water, fully stirring to form a slurry, uniformly spray coating the qualified particles with the slurry, mixing with fermented chicken manure fertilizer, granulating, sieving to obtain particles having particle size of 2.5-3.5 mm, uniformly mixing the qualified particles with solid microbial inoculum, spray coating with slurry prepared from 60% calcium superphosphate, 60% bentonite, and water, drying the granules, and rolling in hot air at 60-80 degrees C, where water content is less than 8%.
NOVELTY - Liquid fertilizer comprises 2-4% chitosan and urea-water solution.    USE - Liquid fertilizer used for promoting the growth speed of plant, maintaining crop nutrient balance, and reducing diseases and insect pests.
NOVELTY - Production of organic-inorganic compound fertilizer, involves: adding a crude fiber of organic matter raw material to production process to produce a large amount of crude fiber containing organic-inorganic compound fertilizer.    USE - For production of organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The fertilizer containing inorganic nutrient (nitrogen, phosphorus, potassium), high content of organic nutrient, large amount of crude fiber, and a beneficial microorganism, effectively improves the fertilizer utilization ratio; improves the quality of agricultural products; improves soil structure; and enhances soil water preserving fertility and crop stress resistance.    DETAILED DESCRIPTION - Production of organic-inorganic compound fertilizer: involves: adding a crude fiber of organic matter raw material to production process to produce a large amount of crude fiber containing organic-inorganic compound fertilizer. The crop straw, bran powder and organic raw material crude fiber by biological fermentation method, is made into biological organic fertilizer with a high concentration of nitrogen, phosphorus and potassium raw materials, and through a series of enzymatic catalysis reaction, to produce organic-inorganic compound fertilizer with high concentration of nutrients and contains a large amount of crude fiber. The fertilizer contains inorganic nutrient (nitrogen, phosphorus, potassium) and high content of organic nutrient, coarse fiber (30%), and beneficial microorganism.
NOVELTY - Extraction of methane from biogas comprises purifying biogas by removing hydrogen sulfide and water vapor; putting purified gas to separation chamber, cooling to temperature prior to methane melting point, and condensing; and heating to temperature 1.15 times the methane melting point to evaporate methane, extracting methane at high temperature, and collecting in methane cylinders.    USE - Method for extracting methane from biogas (claimed).    ADVANTAGE - The method improves methane purity, without consuming additional energy.
NOVELTY - A substituted piperazine-1-carbodithioic acid 1-benzyl-1H-(1,2,3)triazol-4-ylmethyl ester compound, is new.    USE - For preparing anti-gastric cancer, breast cancer, esophageal cancer and prostate cancer medicines (claimed).    ADVANTAGE - The preparation method is simple, efficient, green and environment-friendly. The compound has excellent anti-tumor activity on many types of tumor cells; and can be used as candidate for further development or lead compound, which is applied to prepare the anti-cancer medicine.    DETAILED DESCRIPTION - A substituted piperazine-1-carbodithioic acid 1-benzyl-1H-(1,2,3)triazol-4-ylmethyl ester compound of formula (I), is new.    R1=1-5C alkyl, methoxy, F, Cl, Br or trifluoromethyl;    R2=H or methyl;    R3=1-6C alkyl or benzyl.    In R1 1-5C alkyl, methoxy, F, Cl, Br or trifluoromethyl are mono substituted and F or Cl are polysubstituted. An INDEPENDENT CLAIM is included for preparation of the compound (I).
NOVELTY - Preparation of dihydroquercetin involves processing rutin by heating in high temperature, cooling, filtering, washing by water and drying; heating, refluxing with ethanol, adding activated carbon to decolor, drying, filtering, concentrating filtrate, crystallizing and centrifuging; refining with alcohol, introducing hydrogen in palladium-carbon catalyst, adding zinc powder and sodium borohydride, crystallizing, centrifuging and drying; neutralizing, filtering, fermenting, decompressing and concentrating.    USE - Method of preparing dihydroquercetin (claimed).    ADVANTAGE - The method realizes waste acid recycling and reusing of wastewater, avoids environmental pollution and improves additional value of technology with green and environment-friendly procedure..    DETAILED DESCRIPTION - Preparation of dihydroquercetin comprises:    (A) processing rutin by heating in high temperature, cooling, filtering, washing by water and drying;    (B) heating, refluxing with ethanol, adding activated carbon to decolor, drying, filtering, concentrating filtrate, crystallizing and centrifuging;    (C) refining with alcohol, introducing hydrogen in palladium-carbon catalyst, adding zinc powder and sodium borohydride, adding activated carbon to decolor, filtering, decompressing, concentrating, cooling, crystallizing, centrifuging and drying;    (D) neutralizing, filtering, fermenting, decompressing, concentrating, crystallizing, centrifuging and drying to obtain crude product of rhamnose; and    (E) dissolving rhamnose crude product, adding activated carbon to decolor, filtering, decompressing, concentrating, crystallizing and drying.
NOVELTY - Synthesizing esomeprazole sodium, comprises (a) preparing 5-methoxy-2-(4-methoxy-3,5-dimethyl-2-pyridyl) methylthio-1H-benzimidazole and then dissolving in toluene, (b) adding D-(-)-diethyl tartrate, water, titanium isopropylate and diisopropylamine and then stirring at constant temperature to form chiral catalysis system, dropwisely adding cumyl hydroperoxide with a mass concentration of 80% to perform chiral oxidization reaction and adding sodium hydroxide to obtain esomeprazole sodium crude product, and (c) purifying the esomeprazole sodium crude product.    USE - The method is useful for synthesizing esomeprazole sodium (claimed).    ADVANTAGE - The method is capable of simply, rapidly and economically synthesizing the esomeprazole sodium with high purity and without toxicity and pollution, and is suitable for industrial production.
NOVELTY - Extraction of paeoniflorin and albiflorin comprises selecting plant raw material containing paeoniflorin and albiflorin, extracting for 2-3 times with 70% ethanol solution, concentrating extract, drying concentrate to obtain crude extract; passing extract in macroporous adsorption resin, washing with clean water to remove impurity, eluting with 10-40% ethanol solution, concentrating eluent, drying; and performing high speed countercurrent chromatography with mixed solution of n-butanol-ethyl acetate-water at 4:4:5 volume ratio, collecting paeoniflorin or albiflorin, concentrating and drying.    USE - Method for extracting paeoniflorin and albiflorin (claimed).    ADVANTAGE - The method is simple, environment-friendly, fast and efficient. It has low processing cost and low energy consumption. The extract has 89-98% purity.    DETAILED DESCRIPTION - Extraction of paeoniflorin and albiflorin comprises selecting plant raw material containing paeoniflorin and albiflorin, extracting for 2-3 times with 70% ethanol solution, concentrating extract, drying concentrate to obtain crude extract; passing extract in macroporous adsorption resin, washing with clean water to remove impurity, eluting with 10-40% ethanol solution, concentrating eluent, drying; and performing high speed countercurrent chromatography with mixed solution of n-butanol, ethyl acetate and water at 4:4:5 volume ratio, collecting paeoniflorin or albiflorin, concentrating and drying. The macroporous adsorption resin is non-polar or weak-polar macroporous adsorbent resin.
NOVELTY - Fuel comprises 90-99.5 wt.% of dimethyl ether, 0.5-10 wt.% of methanol, and 500 parts per million (ppm) of antiwear additive.    USE - The fuel is useful for dimethyl ether engine.    ADVANTAGE - The fuel is inexpensive, and has high purity.
NOVELTY - Biodiesel oil is refined by filtering waste oil in filtering device having impermeable sand filler material.    USE - Refining of biodiesel oil (claimed).    ADVANTAGE - The method solves the problem about complex process and high cost of biodiesel.
NOVELTY - A strain amplification culture method to produce glutamic acid involves carrying out amplification culturing from primary seed tank to secondary seed tank.    USE - In strain amplification culture method for producing glutamic acid (claimed).    ADVANTAGE - The method reduces the manual operation; reduces the mixed fungi pollution and contamination; reduces the labor quantity; and has great application value in biological fermentation technology field.
NOVELTY - Producing biodiesel, vitamin E, and sterol involves adding deodorized distillate and anhydrous methanol into the reaction kettle, then adding Novozymes lipase 435 (RTM: lipase) and immobilized lipase PS as catalyst for methyl esterification reaction, after reacting, washing, separating the oil phase from kettle, cooling, filtering and separating to obtain filter liquid, dehydrating, degassing and performing distillation to obtain biodiesel and vitamin E; and after oil phase separation and centrifugal filtering, crystallizing the obtained filter cake to obtain high purity sterol.    USE - For producing biodiesel, vitamin E, and sterol (claimed).    ADVANTAGE - The method performs esterification and transesterification reaction at the same time; has simplifies the process flow, shortens the reaction time, reduced loss rate of vitamin; reduces 50% organic solvent utilization; and greatly reduces production cost.
NOVELTY - Fermenting monosodium glutamate comprises fermenting a culture medium including corn steep liquor, glucose, disodium hydrogen phosphate, magnesium sulfate and potassium chloride, removing the fermented corn steep liquor in the medium, adding disodium hydrogen phosphate water into a fermentation tank and heating and sterilizing the tank, keeping the temperature for a certain time by a first level heat, mixing extracts to the material in the fermentation tank, and finally adjusting the fermentation temperature of the material for inoculating and fermenting process.    USE - The continuous and actual sterilization combined disinfection method is useful for fermenting monosodium glutamate (claimed).    ADVANTAGE - The method does not require sterilization of the heat exchanger frequently so as to avoid pollution and to reduce steam consumption and cooling water consumption.    DETAILED DESCRIPTION - Fermenting monosodium glutamate comprises fermenting a culture medium including corn steep liquor, glucose, disodium hydrogen phosphate, magnesium sulfate and potassium chloride, removing the fermented corn steep liquor in the culture medium by carrying out enzymolysis, adding disodium hydrogen phosphate water into the fermentation tank, heating the tank for a certain time, sterilizing the tank and adding water to it, decontaminating the tank by raising the temperature, keeping the temperature for a certain time by a first level heat exchanger for heating a heat exchange material and by a secondary heat exchanger to reduce the heat by cooling water so as to reduce the material temperature, mixing extracts to the material in the fermentation tank so as to obtain the fermented material, and finally adjusting the fermentation temperature of the material for inoculating and fermenting process.
NOVELTY - Fermentation of monosodium glutamate by using condensed water recycling method involves: taking water and fermentation culture medium comprising molasses, corn steep liquor, disodium hydrogen phosphate, magnesium sulfate and potassium chloride into the mixing tank, stirring and mixing uniformly, sterilizing for 30 minutes into the fermentation tank at 118-125 degrees C, transferring this mixture into a fermentation tank, and fermenting at 33-37 degrees C for 32 hours, after fermenting, concentrating the mixture at 70-72 degrees C, vacuum evaporating and then extracting glutamic acid.    USE - For fermentation of monosodium glutamate (claimed).    ADVANTAGE - Compared with the existing technology, the present method saves the water, energy and raw material; can be widely applied to chemical and food industry; has very good popularization and application value; reduces the steam in the fermentation process; protects the environment; saves sewage treatment cost; and is simple and easy to realize.    DETAILED DESCRIPTION - Fermentation of monosodium glutamate by using condensed water recycling method involves: taking water and fermentation culture medium comprising 1.8-2.7% of molasses, 0.6-5% of corn steep liquor, 1.2-3.6% of disodium hydrogen phosphate (Na2HPO4), 0.2-0.8% of magnesium sulfate (MgSO4) and 1.2-3% of potassium chloride (KCl) into the mixing tank, stirring and mixing uniformly, sterilizing for 30 minutes into the fermentation tank at 118-125 degrees C, transferring this mixture into a fermentation tank, and fermenting at 33-37 degrees C for 32 hours, after fermenting, concentrating the mixture at 70-72 degrees C, vacuum evaporating by using vacuum pressure of 0.8-0.9 Mpa and then extracting glutamic acid.
NOVELTY - Comprehensive utilization of lignocellulose biomass, involves (a) performing acid hydrolysis of the biomass, and separating pentose solution and acid hydrolysis residues, (b) processing the acid hydrolysis residues using alkaline solution to extract alkaline lignin, (c) performing enzymatic hydrolysis of the alkaline hydrolysis residues using cellulase to obtain glucose solution and enzymatic hydrolysis residues, and (d) returning the enzymatic hydrolysis residues to step (b) for alkaline solution processing, and cycling the steps to further extract lignin.    USE - The method is useful for utilizing lignocellulosic biomass (claimed).    ADVANTAGE - The method enables to improve the conversion rate of cellulose enzymatic hydrolysis and realizes comprehensive resource utilization of lignocellulose biomass.    DETAILED DESCRIPTION - Comprehensive utilization of lignocellulose biomass, involves (a) performing acid hydrolysis of the lignocellulose biomass, and separating pentose solution and acid hydrolysis residues, (b) (i) dissolving the acid hydrolysis residues obtained in step (a), using alkaline solution, (ii) filtering and washing the treated alkaline hydrolysis liquid and residue, and (iii) separating and concentrating the alkaline lignin, (c) performing enzymatic hydrolysis of the alkaline hydrolysis residues using cellulase to obtain a glucose solution and enzymatic hydrolysis residues, (d) returning the obtained enzymatic hydrolysis residues to step (b) for alkaline solution processing, or combining the enzymatic hydrolysis residues with another acid hydrolysis residues and performing alkaline solution processing in step (b), then orderly performing steps (c) and (d), and cycling the steps to further extract lignin and to perform enzymatic hydrolysis of the cellulose.
NOVELTY - Utilizing lignocellulose biomass comprises processing lignocellulose biomass by an alkaline solution to dissolve lignin in the alkaline solution, and then filtering and washing to obtain alkaline hydrolysis slag and liquid, separating the obtained liquid by a membrane device and concentrating to obtain alkali lignin solution, performing acid hydrolysis and residue hydrolysis to obtain pentose solution and acid hydrolysis residue, performing enzymatic hydrolysis of the acid hydrolysis residues by cellulose to produce ethanol.    USE - The method is useful for utilizing lignocellulose biomass (claimed).    ADVANTAGE - The method reduces resource utilization of lignocellulose biomass.
NOVELTY - Lignocellulose biomass is subjected to n-stage acid hydrolysis. Freshly prepared acid solution is added in initial stage reaction kettle, and final pentose solution obtained by hydrolysis is discharged from n-stage reaction kettle. Final acid hydrolysis residues are discharged from initial stage reaction kettle, such that concentration of acid solution decreases from initial stage to nth stage by 10-40% of concentration of initial stage acid solution. Acid hydrolysis residues are treated using alkaline solution, and subjected to enzymatic hydrolysis using cellulase.    USE - Usage of lignocellulose biomass (claimed).    DETAILED DESCRIPTION - Lignocellulose biomass is subjected to n-stage acid hydrolysis in reaction kettles which are connected end to end, in which one of the reaction kettle is designed as initial stage reaction kettle and a final reaction kettle is designed as an n-stage reaction kettle. Freshly prepared acid solution is added in initial stage reaction kettle, and final pentose solution obtained by hydrolysis is discharged from n-stage reaction kettle. Final acid hydrolysis residues obtained by acid hydrolysis are discharged from initial stage reaction kettle, and new materials are loaded on the initial stage reaction kettle, such that concentration of acid solutions decrease gradually from the initial stage to the nth stage by 10-40% of the concentration of initial stage acid solution, where n is 2 or more. Acid hydrolysis residues are treated using an alkaline solution, so that alkaline lignin is extracted. Alkaline hydrolysis residues obtained by alkaline hydrolysis treatment, is subjected to enzymatic hydrolysis using cellulase, so that solution with glucose as main component is obtained.
NOVELTY - Utilizing lignocellulose biomass comprises performing acid hydrolysis of a lignocellulose biomass, separating it to obtain a pentose solution and acid hydrolysis residues, performing enzymatic hydrolysis of the acid hydrolysis residues by cellulose to obtain a glucose solution and enzymatic hydrolysis residues, where the cellulose is obtained by culturing a strain of Penicillium with a preservation number of CCTCC NO: M 2011195, and then processing the enzymatic hydrolysis residues produced by an alkaline solution so as to extract lignin from the enzymatic hydrolysis residues.    USE - The comprehensive method is useful for utilizing lignocellulose biomass (claimed).    ADVANTAGE - The method reduces resource utilization of lignocellulose biomass.
NOVELTY - Comprehensive utilization method of lignocellulosic biomass involves carrying out acid hydrolysis to lignocellulosic biomass, obtaining pentose solution and acid hydrolysis residue, subjecting enzymolysis to acid hydrolysis residue using cellulase, obtaining glucose solution and enzymolysis residue, processing enzymolysis residue with alkali solution, returning hydrolysis residue, carrying out enzymolysis treatment, and performing lignin degradation. Enzymolysis residue is processed, obtaining alkaline hydrolysis liquid and residue, and concentrating.    USE - Comprehensive utilization method of lignocellulosic biomass (claimed).    DETAILED DESCRIPTION - Comprehensive utilization method of lignocellulosic biomass involves carrying out acid hydrolysis to lignocellulosic biomass, obtaining pentose solution and acid hydrolysis residue, subjecting enzymolysis to acid hydrolysis residue using cellulase, obtaining glucose solution and enzymolysis residue, processing enzymolysis residue with alkali solution, returning hydrolysis residue, carrying out enzymolysis treatment with new acid hydrolysis residue, extracting, and performing lignin degradation. The enzymolysis residue is processed by dissolving alkali solution to lignin, filtering, washing, obtaining alkaline hydrolysis liquid and residue, separating and concentrating.
NOVELTY - Comprehensive utilization of lignocellulosic biomass, comprises performing acid hydrolysis to lignocellulosic biomass to obtain pentose solution and acid hydrolysis residue, enzymolyzing the obtained acid hydrolysis residue using cellulase, processing the resulting enzymolyzing residue using alkaline solution, performing enzymolysis process of resulting alkaline hydrolysis residue or combining the alkaline hydrolysis residue with acid hydrolysis residue to perform enzymolysis process, repeating the process, circulating, extracting lignin and performing cellulose hydrolysis.    USE - The method is useful for comprehensive utilization of lignocellulosic biomass (claimed).    ADVANTAGE - The method achieves maximum resource utilization of lignocellulosic biomass.    DETAILED DESCRIPTION - Comprehensive utilization of lignocellulosic biomass, comprises: (a) performing acid hydrolysis to lignocellulosic biomass to obtain pentose solution and acid hydrolysis residue, (b) using cellulase to carry out enzymolysis of the acid hydrolysis residue obtained in step (a) to obtain glucose solution and enzymolysis residue, (c) processing enzymolysis residue obtained in the step (b) with an alkaline solution, extracting lignin to obtain alkaline hydrolysis residue, and (d) refluxing the alkaline hydrolysis residue back to the step (b) to perform enzymolysis process or combining the alkaline hydrolysis residue with the acid hydrolysis residue to perform enzymolysis treatment, and then performing the steps (c) and (d), and circulating, and extracting lignin and performing cellulose hydrolysis.
NOVELTY - Utilizing lignocellulosic biomass comprises performing N-stage hydrolysis on lignocellulose biomass, performing enzymatic hydrolysis on the acid hydrolysis residues by cellulose so that a glucose solution and enzymatic hydrolysis residues are obtained, treating the enzymatic hydrolysis residues with an alkali solution so that lignin in the enzymatic hydrolysis residues is extracted, returning the alkali hydrolysis residues obtained by alkali hydrolysis treatment to the enzymatic hydrolysis, and extracting the lignin and performing cellulose enzymatic hydrolysis.    USE - The method is useful for utilizing lignocellulosic biomass (claimed).    ADVANTAGE - The method enables reducing utilization of resources for realizing lignocellulose biomass production.    DETAILED DESCRIPTION - Utilizing lignocellulosic biomass comprises performing N-stage hydrolysis on lignocellulose biomass, where a reduced range of concentration of an acid solution from a first-stage to an N stage is 10-40% that of the first-stage acid solution, and N is an integer greater than or equal to 2, performing enzymatic hydrolysis on the acid hydrolysis residues by cellulose so that a glucose solution and enzymatic hydrolysis residues are obtained, treating the enzymatic hydrolysis residues with an alkali solution so that lignin in the enzymatic hydrolysis residues is extracted and alkali hydrolysis residues are obtained, returning the alkali hydrolysis residues obtained by alkali hydrolysis treatment to the enzymatic hydrolysis after the enzymatic hydrolysis residue treatment step is finished so as to perform enzymatic hydrolysis or firstly mixing the alkali hydrolysis residues with fresh acid hydrolysis residues and then carrying out the enzymatic hydrolysis to perform alkali hydrolysis treatment process successively, and finally repeating the above process, and further extracting the lignin and performing cellulose enzymatic hydrolysis.
NOVELTY - Lignocellulose biomass is subjected to n-stage acid hydrolysis in reaction kettles. Freshly prepared acid solution is added to initial stage reaction kettle, and final pentose solution obtained by hydrolysis is discharged from n-stage reaction kettle. Final acid hydrolysis residues are discharged from initial stage reaction kettle, and new materials are loaded on initial stage reaction kettle. Acid hydrolysis residues are treated using alkali solution, and enzymatic hydrolysis is carried out using cellulase, so that solution with glucose as main component is obtained.    USE - Usage of lignocellulose biomass (claimed).    DETAILED DESCRIPTION - Lignocellulose biomass is subjected to n-stage acid hydrolysis in reaction kettles which are connected end to end, in which one of the reaction kettle is designed as initial stage reaction kettle and a final reaction kettle is designed as an n-stage reaction kettle. Freshly prepared acid solution is added in initial stage reaction kettle, and final pentose solution obtained by hydrolysis is discharged from n-stage reaction kettle. Final acid hydrolysis residues obtained by acid hydrolysis are discharged from initial stage reaction kettle, and new materials are loaded on the initial stage reaction kettle. The primary stage hydrolysis reaction time is 1-4 hours. The subsequent hydrolysis reaction time is reduced by 0.25-1.5 hours stage by stage, where n is 2 or more. Acid hydrolysis residues are treated using an alkali solution, so that alkali lignin is extracted. Alkali hydrolysis residues obtained by alkali hydrolysis treatment, is subjected to enzymatic hydrolysis using cellulase, so that solution with glucose as main component is obtained.
NOVELTY - Utilizing lignocellulosic biomass comprises performing N-grade acid hydrolysis of lignocellulosic biomass in a reaction kettle, adding the acid solution into a first acid hydrolysis reaction kettle, and then adding water to a second grade acid hydrolysis reaction kettle, and then adding water in a third level hydrolyzing reaction kettle, carrying out a hydrolysis reaction for circulating the lignocellulosic biomass, carrying out acid enzymolysis reaction to obtain glucose solution and enzymolysis residue using a cellulose, and carrying out residue enzymolysis process to extract alkali lignin.    USE - The method is useful for utilizing lignocellulosic biomass (claimed).    ADVANTAGE - The method enables reducing the usage of lignocellulosic biomass sources.    DETAILED DESCRIPTION - Utilizing lignocellulosic biomass comprises performing N-grade acid hydrolysis of lignocellulosic biomass in a reaction kettle,adding the prepared acid solution into a first acid hydrolysis reaction kettle, and then adding water to a second grade acid hydrolysis reaction kettle, adjusting acid concentration of the reaction kettle, and then adding water in a third level hydrolyzing reaction kettle, where concentration of the acid hydrolysis solution in the reaction kettle is N-1, discharging a pentose solution in a first level hydrolyzing reaction kettle to prepare an acid hydrolysis residue, carrying out a hydrolysis reaction for circulating the lignocellulosic biomass, where reduced range of concentration of the acid solution from a first-stage to an N-stage is 10-40% that of the first-stage acid solution, and N is an integer greater than or equal to 2, carrying out acid enzymolysis reaction to obtain glucose solution and enzymolysis residue using a cellulose, and carrying out residue enzymolysis process to extract alkali lignin in the enzymolysis residue.
NOVELTY - Supercritical extraction of rotenone comprises crushing rotenone plant tissue to obtain powder, adding powder and extracting liquid at a mass ratio of 0.5-1.5:6 in extraction tank for extraction at 50-55 degrees C and stirring for 1-2 hours; adding extracting liquid to heating tank at 62-68?0C; evaporating chloroform in condensation tank and returning cooling liquid into the extraction tank and repeat extracting powder; repeating second and third step 1-4 times; and recovering liquid in the heating tank.    USE - Method for supercritical extraction of rotenone (claimed).    ADVANTAGE - The method recycles chloroform to solve problems in soil compaction, decreasing fertility, serious environmental problems and large influence on non target organisms; has high extraction rate of rotenone and environment-friendly.
NOVELTY - The straw marsh gas fermentation device comprises a fermentation tank body, a double-layered thermal insulation layer, a multi-point top part feeding pipe, a fermentation liquid, and a solar water heater heat collection system. The multi-point top part feeding pipe comprises a vacuum pump, a heat insulating air pressure feeding tank. The fermentation liquid is passed to the fermentation tank through a top part of a feeding pipe. The solar water heater heat collection system comprises a circulating water tank, and fermentation raw material heating pipe.    USE - Used as straw marsh gas fermentation device.    ADVANTAGE - The straw marsh gas fermentation device has high working efficiency, utilization rate and yield and less energy consumption, and is inexpensive.    DETAILED DESCRIPTION - The straw marsh gas fermentation device comprises a fermentation tank body, a double-layered thermal insulation layer, a multi-point top part feeding pipe, a fermentation liquid, and a solar water heater heat collection system. The multi-point top part feeding pipe comprises a vacuum pump, a heat insulating air pressure feeding tank. The fermentation liquid is passed to the fermentation tank through a top part of a feeding pipe. The solar water heater heat collection system comprises a circulating water tank, fermentation raw material heating pipe, auxiliary solar energy heat pump. The double-layered thermal insulation layer in a fermentation tank and a polyurethane foaming insulating layer are provided with an air isolation layer.
NOVELTY - Cultivating sea Chlorella comprises uniformly mixing a sludge and then standing for 1 hour, taking precipitate from the sludge, adding sea water in the sludge precipitate in volume ratio of 1:10, centrifuging the mixed solution at 600 revolutions per minute for 3 hours, and collecting the supernate and then sterilizing at 121 degrees C.    USE - The method is useful for cultivating sea Chlorella for feed industry.
NOVELTY - Preparing cellulosic ethanol by using steam-exploded straw material involves: a) crushing straw material by a mechanical device in the blasting container (1); b) maintaining a pressure to 1.2-4 Mpa for 10-120 minutes; c) opening the blasting container, and separating the material; d) passing the organic molecules separated from material obtained in the step c) into a pressure-reducing cabinet; e) passing the liquid obtained in step d) into a condenser (3); f) subjecting to sewage treatment process; g) passing tail gas obtained in step e) to absorbing tower (4).    USE - For preparing cellulosic ethanol by using steam-exploded straw material (claimed).    ADVANTAGE - The present method can full use of heat energy of vehicle exhaust gas; and is easy to popularize and use.    DETAILED DESCRIPTION - Preparing cellulosic ethanol by using steam-exploded straw material involves: a) crushing straw material by a mechanical device in the blasting container (1); b) maintaining a pressure to 1.2-4 Mpa for 10-120 minutes; c) opening the blasting container, and separating the material; d) passing the organic molecules separated from material obtained in the step c) into a pressure-reducing cabinet; e) passing the liquid obtained in step d) into a condenser (3); f) subjecting to sewage treatment process; g) passing tail gas obtained in step e) to absorbing tower (4), where harmful substance in tail gas is absorbed by reduction of the gas by the water in the absorption tower.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a method for preparing cellulosic ethanol by using steam-exploded straw material.    Blasting container (1)    Decompression chamber (2)    Condenser (3)    Absorbing tower (4)    Belt conveyor (5)
NOVELTY - Making silicon-rich composite biological fertilizer by using fermentation culture of Bacillus mucilaginosus and Bacillus circulans involves: culturing Bacillus mucilaginosus and Bacillus circulans in culture medium, where the culture medium comprises corn dregs lixivium, bran lixivium, soybean flour, glucose, dipotassium hydrogen phosphate, magnesium sulfate, ammonium sulfate, calcium carbonate, iron(III) chloride, yeast extract, ash, and distilled water; adding thermal power plant slag and fly ash; passing into decomposing furnace; and then fermenting.    USE - For preparing silicon-rich composite biological fertilizer used for plant growth (claimed), where the plant is wheat, maize, sorghum, cucumber, watermelon and white gourd.    ADVANTAGE - The silicon-rich composite biological fertilizer obtained by the present method can effectively supplement silicon and potassium element to plant; and also has good economic and social benefit.    DETAILED DESCRIPTION - Preparing silicon-rich composite biological fertilizer by using fermentation culture of Bacillus mucilaginosus and Bacillus circulans involves: culturing Bacillus mucilaginosus and Bacillus circulans in culture medium, where the culture medium comprises 10% corn dregs lixivium, 10% bran lixivium, 0.6% soybean flour, 0.2% glucose, 0.2% dipotassium hydrogen phosphate (K2HPO4), 1.5% magnesium sulfate (MgSO4), 0.5% ammonium sulfate ((NH4)2SO4), 1% calcium carbonate (CaCO3), 0.2% iron(III) chloride (FeCl3), 0.4% yeast extract, ash (1-2%), and balanced to 100% distilled water; adding thermal power plant slag and fly ash; passing into decomposing furnace; and then subjecting to fermentation process at a following conditions: controlling the pH value at 7.2-7.5, controlling air flow of 10-20 m3/minutes for 34-38 hours, and controlling the temperature of 36-38 degrees C.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of process for preparing silicon-rich composite biological fertilizer.
NOVELTY - This utility model claims a kind of biological bacteria fertilizer automatic producing device, comprising a central controller, a drying process unit central controller is respectively connected with the loading mechanism for feeding raw material, mixing and crushing the raw materials to a stirrer, a fermentation tank strain inoculating fermentation, solid fertilizer is a separate processing unit for processing liquid bacterial manure is electrically connected, wherein a, a stirrer and the fermentation tank are connected in turn, and the drying process unit and separating process unit is respectively connected with the fermentation tank; The beneficial effects of the utility model are as, low cost, green and environment-friendly.
NOVELTY - This utility model is a kind of belt dangerous waste gasification furnace for plasma torch heating system, the dangerous waste gasification furnace comprises gasification furnace body (1), a gasification furnace body lining of refractory material layer (2) is set on the top of the gasification furnace feeding port (3) is set on the upper part of the furnace body is gasification furnace side of the gas outlet (4), a gasification furnace body is set on the lower side of the oxidant gas inlet (5), a gasification furnace body is set on the lower side of the plasma torch (6), and the gasification furnace body bottom side of slag and metal outlet (7). This utility model claims a dangerous waste gasification furnace is novel and special, scientific and reasonable structure, can realize a renewable resource raw material and use of enlarging and method, better support biomass power generation and biomass chemical project as conditions, promotes the development of green energy, dangerous waste gasification discharge piping system of coke oven is oven capable of collecting and utilizing, as a heat value of the fuel gas or chemical raw material gas.
NOVELTY - This utility model is a kind of biomass-doped garbage gasification furnace for plasma torch heating system, the gasification furnace comprises gasification furnace body (1), a gasification furnace body lining of refractory material layer (2) is set on the top of the gasification furnace feeding port (3) is set on the upper part of the furnace body is gasification furnace side of the gas outlet (4), a gasification furnace body is set on the lower side of the oxidant gas inlet (5), a gasification furnace body is set on the lower side of the plasma torch (6), a gasification furnace body is set on the bottom side of the slag outlet (7). This utility model claims a biomass-doped garbage gasification furnace is novel and special, scientific and reasonable structure, can realize a renewable resource raw material and use of enlarging and method, better support biomass power generation and biomass chemical project as conditions, promotes the development of green energy of biomass mixed garbage gasification discharge piping system of coke oven is oven capable of collecting and utilizing, as a heat value of the fuel gas or chemical raw material gas.
NOVELTY - This utility model claims a kind of new-type multifunctional biomass gasification furnace. A outer water cavity (1), the water pipe (2), smoke chamber 3, the inner layer water cavity (4), a water inlet pipe (5), a gasification cavity (6), a water outlet pipe 7, a water inlet pipe (5) and the outer layer water cavity (1) is connected with the water pipe (2) is connected with the outer layer water cavity (1) and the inner water cavity 4, smoke cavity (3) is located between the outer water cavity (1) and the inner water cavity 4 and 6 is connected with the gasification chamber. Replace prior art through use of a cavity of the water pipe, which greatly increases the contact area of the water area and the gasification cavity and greatly improves the water hot water outlet and the water outlet temperature, at the same time, effectively reduces the oxidation rate of material gasification chamber, and improves the service life of the biomass gasification furnace. In addition, the increase of the whole cavity, which can fully cooling a combustion gas, compared with the existing technology, reduces the outer wall temperature of the biomass gasification furnace, which effectively improves the use safety of the biomass gasification furnace.
NOVELTY - The utility model claims a biomass gasification furnace taking carbon auxiliary device, the device is composed of a guide pipe (1), the isolated carbon rod 2, 3 is composed of a stop valve, the guide pipe 1 one end is fixed on the furnace body (4), and the other end is connected with the stop valve (3) are connected together, the carbon separating rod (2) capable of passing through the guide tube 1 and check valve 3. When taking carbon powder, firstly opening stop valve 3, to the carbon separating rod (2) from the stop valve (3) is inserted into the guide pipe 1 is not completely combustion of biomass fuel block above the carbon separating rod (2), a carbon outlet from the hollow carbon powder, it can effectively ensure the carbon powder and biomass fuel fully separated from said valve seat. This kind of auxiliary device, simple operation, taking carbon effect is good.
NOVELTY - This utility model claims a marsh gas generating device, comprising an anaerobic reactor and the pure marsh gas power generation system, an anaerobic reactor through the exhaust pipe and the pure marsh gas power generation system, the pure marsh gas power generation system is connected to the electric appliance by the power transmission line, wherein the anaerobic reactor and the pure marsh gas power generation system and the exhaust pipe are connected in turn for generating marsh gas anaerobic reactor for purifying and compressing of the gas-water separator, a desulfurizing tower, a condenser and a pressurizing storage tank, and the pure marsh gas power generation system and electric appliance for controlling electric power output control unit of the pure marsh gas power generation system power output. By improving the purity and concentration of marsh gas, at the same time, the electric power output control unit controls pure marsh gas power generation system for generating high efficient work, so as to ensure full combustion of marsh gas, reduce discharge of greenhouse gas generating efficiency is high, environment-friendly and energy-saving.
NOVELTY - This utility model claims a kind of underground biomass partner process of corollary equipment, comprising at least one kind of microorganism filler of the submersible vessel, the submersible container for microorganism nutrient supply of nutrient tank, diving the container surface to form the surface of the bottom of tank is provided with a diving pump, the surface is drilled in the diving pump is connected with a long thin pipe is connected to the bottom of the container is submerged, and long thin tube close to the submersible vessel is provided with several holes of long thin long thin pipe part extending a pipe outside the submersible vessel, the lower branch pipe is connected with an aeration device. This utility model can provide a specific, efficient and stable organic matter in the sewage and provides efficient and stable sewage treatment in the application of the sewer system.
NOVELTY - This utility model claims a method for ecological circulation mechanism of wastewater/sewage treatment system, comprising a equipment for preparing pure natural fiber biomaterial, is provided with a water storage space, and a plurality of organic compound and a suspended substance in sewage source device is guided to the water storage space, and introduced into the water as proper proportion to a water purifying water device, the water storage space is provided with a light source to form the first cultivating algae, and provided with a plurality of conversion part in the water storage space, the water storage space in the water algae and conversion part and so on together is composed of wastewater/sewage processing system is used for removing the organic compound and suspended substance in the water storage space and so on pollution source, therefore, the peculiar smell and pollution material can effectively improve water source device is in the form of an aqueous regeneration as resource recycling, not only can achieve the purpose of waste/sewage treatment, and it can reduce the large energy consumption, but also has sustainablly and environment-friendly.
NOVELTY - The utility model claims a kitchen garbage recycling automatic processing machine, comprising a crushing device, a pressing device, an oil-water separating device and a biochemical processing device and a kitchen garbage automatic processing machine using a crushing device, a pressing device, an oil-water separating device and a biochemical treatment device to form an integrated device, the oil-water mixture to separate, at the same time, the sewage after being processed by sewage treatment to reach the discharge standard can be directly on the oil-water separating device, the utility model is a device integrated design and adding microbial inoculum in the biochemical treatment device, can greatly shorten the composting time of the kitchen garbage solid residue, improve the processing efficiency, the device has small volume, convenient use, good treatment effect, it has good market popularization value.
NOVELTY - This utility model claims a fermentation device for kitchen garbage, comprising a fermentation tank, a stirrer, a heater and a temperature automatic control system, wherein the fermentation tank is provided with a feeding port, adding enzyme and an air outlet port, wherein the fermentation tank is provided with a temperature sensor, the temperature sensor is connected with the heater and a temperature automatic control system is connected with the heater is installed in the fermentation tank, the stirrer comprises a driver and a stirring propeller, a stirring screw propeller is extended and set with the fermentation tank of the driver rotating the fermentation tank. The fermentation device by reasonably arranging the driver and cover and automatic temperature control system, so that the device in the process of operation, low noise, and can obtain stable rotating speed of the stirring and heating temperature, so as to effectively control the stable fermentation conditions has reached the best fermentation treatment effect, improves the processing efficiency of the kitchen garbage.
NOVELTY - A method for producing organic compound fertilizer by test device, comprising a fan, a reaction chamber, a bottle a, dryer, bottle, hydrogen sulphide alarm, a bottle b and sulphur dioxide alarm and which are connected in series via a pipeline, a fan, a reaction chamber, a drier, a hydrogen sulphide alarm and a sulphur dioxide outlet pipeline of the alarm are respectively provided with a valve, the reaction chamber is a sealed box body, the inner chamber is fixed with a horizontal silo. type stirrer, a bottle filled with a dilute sulfuric acid, a drier is spherical drying tube containing calcium oxide, bottle filled with concentrated sulphuric acid, a bottle B is equipped with ammonium hydrogen carbonate solution. The advantages of the utility model are as follows: the device uses the biological fermentation and chemical method, using waste straw, livestock manure, ammonium bicarbonate, sulphuric acid and calcium oxide as raw material, producing the rich in nitrogen and sulphur mineral nutrition and high-efficient organic fertilizer of organic matter, at the same time avoids the generation of ozone in the composting process, improves fertilizer effect, at the same time, avoids the secondary pollution.
NOVELTY - This utility model claims a kind of human hole and the fermentation tank is provided with a manhole. The human hole comprises a base, the base is cylindrical, the base used is connected to the fermentation tank, a sealing head, a lower sealing head is a lower end enclosure at one side of the opening end is pivoted on the large bottom of the base, the lower end enclosure around the horizontal pivot shaft to rotate. According to this utility model the human hole, the lower seal head is pivoted on the bottom of the base, the end enclosure is pivoted around a horizontal rotation. The setting such as the operator into the fermentation tank for cleaning and maintenance and creates condition, improves the cleaning efficiency of the fermentation tank, improving the cleaning effect of the fermentation tank so as to improve the production efficiency and the product quality.
NOVELTY - This invention claims a kind of stirring system, comprising a marsh gas tank, stirrer, floating platform, a rotating resistance tester and a controller, wherein the stirrer is set in the marsh gas tank, floating platform comprises a sliding rail on the inner wall of the marsh gas tank and capable of sliding along the slide rail, and a floating on the supporting platform of the marsh liquid surface in the marsh gas tank, rotating resistance tester is mounted on the supporting platform, which is used for detecting a characteristic resistance value floating number of the biogas liquid surface in the marsh gas tank, the first controller is respectively connected with the stirrer, rotating resistance tester is connected with the resistance value for the rotational resistance tester to a preset resistance threshold value, and when the resistance value is greater than a preset resistance threshold value signal and stirring to the stirrer. When the system by detecting the resistance of the surface can be the gas condition of the marsh gas tank is a floating surface of the stirrer to stir, controlling the floating the gas.
NOVELTY - A kind of dry method and wet method for combining ferment producing marsh gas reaction device, comprising a feeding port, a discharging port and the air outlet of the dry fermentation tank, wherein the dry fermentation tank body on the outer wall of the tank body is provided with an insulating layer, and the insulating layer is coated on the outer surface of the solar energy heat absorbing material, dry fermentation tank is connected with the air outlet and the wet marsh gas tank, marsh gas tank is connected with the biogas outlet pipe and the wet gas chamber. The utility model is common to rural biomass as raw material, fully uses the biomass in rural areas at the same time to improve the living environment of farmers. Because of dry anaerobic fermentation tank is provided with a heat preservation layer, it can ensure the normal gas, even if the wet marsh gas tank in winter cannot be gas, combined with a dry anaerobic fermentation tank also can complete normal process in cold winter, it effectively improves the traditional wet marsh gas tank in winter gas generating efficiency is low.
NOVELTY - This utility model claims a device for anaerobic reaction device for food waste treatment, comprising a reaction tank (1) and a pipeline pump (3), the upper part of the reaction tank (1) is provided with a plurality of nozzles (2), the pipeline pump (3) on the bottom of the reaction tank (1), the input port of the pipeline pump (3) is connected with the reaction tank (1) is connected with the lower part, the pipeline pump (3) is a spray head is connected with the reaction tank (1), (2). This utility model adopts said structure, wherein the kitchen garbage treatment process, it can prevent scum, for avoiding blocking reaction tank, so as to ensure the normal process of the kitchen garbage.
NOVELTY - This invention claims a kind of marsh gas pool temperature control system, the system comprising: a set in the marsh gas tank, and is used for stirring the liquid in the marsh gas tank of the stirrer, disperse arranged in different areas in the marsh gas tank, a plurality of temperature sensors for detecting the temperature value of region a biogas liquid in the marsh gas tank, and a plurality of temperature sensors, a temperature comparator for the first size of the multiple temperature sensors measure temperature values, and a comparison between any two temperature value of the difference value with the preset temperature difference, a stirrer, a temperature comparator, when used for preset temperature difference value when the difference value is more than between any two temperature value, generating a stirring and sending to the controller of the stirrer. Compared with the existing technology, the device can carry out stir according to the specific condition in the marsh gas tank, the flexibility is good, it can better control the temperature in the marsh gas tank to avoid the different areas and large temperature difference;
NOVELTY - The utility model claims a hydrogen-oxygen mixed gas generator, comprising a series combination of a plurality of electrolytic chamber of the electrolytic cell, the electrolytic cell is provided with a hydrogen and oxygen outlet total total outlet, hydrogen outlet total a total oxygen outlet are respectively connected to the hydrogen water seal jar and oxygen water seal tank, further comprising the liquid tank, the liquid tank is connected to the hydrogen water seal jar and oxygen water seal tank through pipeline, hydrogen water seal tank set a liquid outlet and a gas water seal tank by the liquid outlet pipe is connected to the electrolytic cell. This utility model is water electrolysis to obtain hydrogen and oxygen, hydrogen and oxygen by electrolysis groove are respectively washing clean the hydrogen water seal tank set and oxygen tank water, then to use, the combustion gas hydrogen and oxygen combustion-supporting gas can be separated to obtain, on one hand to avoid the tempering in the flame processing industry of potential safety hazard, but also can use two kinds of gas to realize different functions. This utility model can be used as manufacturing and generated as hydrogen and oxygen.
NOVELTY - Processing livestock manure used for production of organic biofertilizer, involves stirring the livestock manure, and filling ozone into stirred livestock manure.    USE - Processing livestock manure used for production of organic biofertilizer (claimed).    ADVANTAGE - The livestock manure is processed preferably oxidized, such that components preferably various bacteria, viruses and roundworm ova and heavy metals chosen from aluminum, mercury, chromium and arsenic being harmful to human body are removed or eliminated from the livestock/poultry manure which often get absorbed into human body when used as raw material during preparation of the high-quality organic biofertilizer.
NOVELTY - A solid composite actinomycete bacteria fertilizer comprises Streptomyces violascens (T 005=CCTCC M 2012185), Streptomyces albidoflavus (T 006=CCTCC M 2012186), Streptomyces rutgersensis (T 009=CCTCC M 2012187), Streptomyces koyangensis (T 011=CCTCC M 2012188) and 20% of Streptomyces gelaticus (T 013=CCTCC M 2012189).    USE - Solid composite actinomycete bacteria fertilizer used for improving cultivation of pseudoginseng.    ADVANTAGE - The fertilizer improves the survival rate of pseudoginseng seedlings.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid composite actinomycete bacteria fertilizer comprising adding seed culture in liquid culture medium, culturing to log phase, inoculating in solid fermentation culture medium at inoculum concentration of 10%, fermenting to maturity period and mixing uniformly, where viable bacterial count is greater than or equal to 26.8x 108 units/g.
NOVELTY - Sweet potato residue is used for preparing fertilizer. The preparation comprises pulping sweet potato residue to obtain slurry, solid-liquid separating, drying, crushing to obtain powder, mixing sweet potato residue powder and chicken manure, stirring to obtain particles, adding thermophilic aerobic fermentation bacterial strain, fermenting at 20-35 degrees C for 48-72 hours until temperature of tank is 50-60 degrees C, fermenting at 35-40 degrees C for 48-72 hours until temperature of tank is 60-70 degrees C, fermenting at 70-80 degrees C for 48-72 hours, cooling to room temperature and fermenting at 40-50 degrees C.    USE - Sweet potato residue is used for preparing fertilizer (claimed).    ADVANTAGE - The method changes waste into valuable product, thus helping in protecting the environment. The prepared fertilizer has high nutrients and trace elements such as glycoprotein, organic acid, cellulose and nucleic acid, and does not contain heavy metals. It helps in reducing soil compaction and viral diseases.    DETAILED DESCRIPTION - Sweet potato residue is used for preparing fertilizer. The preparation comprises pulping sweet potato residue to obtain slurry, solid-liquid separating, drying, crushing to obtain powder of 100-200 meshes, mixing 50-70 pts. wt. sweet potato residue powder and 30-50 pts. wt. chicken manure, stirring to obtain particles, adding thermophilic aerobic fermentation bacterial strain at particles to bacterial strain weight ratio of 8-10:1-1.2, fermenting at 20-35 degrees C for 48-72 hours until temperature of tank is 50-60 degrees C, fermenting at 35-40 degrees C for 48-72 hours until temperature of tank is 60-70 degrees C, fermenting at 70-80 degrees C for 48-72 hours, cooling to room temperature and fermenting at 40-50 degrees C.
NOVELTY - A kind of adjusting cavity is mountain water and fertilizer, comprising a cavity the upper part of body, the cavity is 60 cm long, and the width is 40 cm, the depth of the square structure according to claim 50 cm, said cavity towards inside of excavating a bottom width is wedge-shaped space 20 cm. This utility model by injecting a edible fungi material on slope digging, it not only can prevent the edible fungi waste pollution environment, but also can store mountain ground rainwater to prevent the loss of waste, at the same time, the mountain soil water condition, the farmer income, lasting fertilizer effect, economical and practical, and the inner space is large, the structure is firm, it is not easy to collapse.
NOVELTY - A microbial organic fertilizer is produced by mixing 65-70 wt.% furfural residue and 30-35 wt.% weathered coal powder to obtain mixture, adding water at 95-100 degrees C, stirring uniformly, naturally fermenting to obtain substrate, adding potash fertilizer and adhesive to substrate, adding 1-10 times inoculated composite bacteria, mixing uniformly and fermenting.    USE - Method for producing microbial organic fertilizer (claimed) used for vegetables, sunflower and corn.    ADVANTAGE - The low-cost fertilizer is environment-friendly and long-lasting, and improves fertility of soil and crop yield by 10%, where yield is increased to 10-15%.
NOVELTY - This utility model claims a kind of rotary high efficient bioreactor, comprising a tank (1), a gear motor (2), a central rotating shaft (3), and it is fixed with three vertical supporting steel plate on the central rotating shaft (3) (4), a plurality of reaction tube (5) is arranged on the supporting steel plate (4), a protective cover (6) is covered on the water tank (1), the reaction pipe (5) comprises a supporting pipe (7), and is fixed on the supporting tube (7) grid-shaped plastic rod (8). This utility model adopts cylindrical hollow three-dimensional net-like plastic rod to replace the biological rotating disk sheet, as the attached body. Because of cylindrical hollow three-dimensional net-shaped plastic rod lower disc using space is large, and the microorganism attached on the net-shaped plastic rod is more than the sewage fully contact, so compared with the existing device, the processing efficiency is high.
NOVELTY - This utility model is a kind of waste gas treatment and sewage purification of the bio-filtering tower device, comprising a bio-filtering tower, comprising a spraying device on the top of the water-gas contact layer part and a groove on its bottom, wherein it further comprises a connected with the bottom of the fluid pipeline and the sewage bio-filtering tower strengthening self-cleaning device. A sewage reinforcing self-cleaning device beside the biological filter tower, adding the microorganism and reinforced in the groove, it can fast degrade the harmful substance in the water, the harmful substance in the water is completely decomposed, so as to make the water and the cycle water recycling standard and the process through the circulating water is pumped to the spraying device of the bio-filtering tower, so as to circulate, and a little sludge only by regular mud removing is. Therefore, there is no need for water to sewage treatment plant for treatment, or new processing structure for the sewage at the same time complete the clean water to the water collecting groove, so as to greatly reduce the cost.
NOVELTY - A modified mordenite zeolite-containing isomerization catalyst comprises 0.01-5 wt.% noble metal element, 10-80 wt.% phosphorus-modified mordenite zeolite, 0.1-10 wt.% additive and 0.5-5 wt.% halogen-containing binder. The phosphorus-modified mordenite zeolite contains 0.1-10 wt.% phosphorus.    USE - A modified mordenite zeolite-containing isomerization catalyst is used in isomerization reaction of alkane containing 4-12 carbon atoms (claimed), and production of high-octane rating gasoline.    ADVANTAGE - The catalyst has high catalytic activity and selectivity.
NOVELTY - Synthesizing levocarnitine using D-(-)-tartaric acid comprises synthesizing D-(-)-dibenzyl tartrate with benzyl alcohol using boric acid as a catalyst, reducing D-(-)-dibenzyl tartrate to obtain D-(-)-2,3,4-methyl trihydroxy benzene using sodium borohydride as a catalyst, bromizing in a hydrogen bromide acetate solution to obtain D-(-)-3-hydroxy-2,4-dibromo-benzene methyl ester, performing selective debromination to obtain D-(-)-3-hydroxyl-4-bromobenzene methyl ester using palladium-carbon catalyst by introducing hydrogen, and performing ion exchange.    USE - The method is useful for synthesizing levocarnitine using D-(-)-tartaric acid (claimed).    ADVANTAGE - The method provides levocarnitine without using resolving agent and cyanide and with mild reactions in a cost-effective and environmental friendly manner.
NOVELTY - Planting iodine-enriched flower comprises drying iodine-rich sea cabbage, crushing at diameter of 6 mm, sieving to 80-100 meshes sieve, extruding by pelletizer, preparing diameter of 2-6 mm of particulate solid organic fertilizer, and cultivating iodine-enriched vegetable.    USE - Method for planting iodine-enriched flower (claimed).
NOVELTY - The utility model claims a firewood waste gas automatic generator furnace, comprising a furnace body, a feeding system, a gas reaction purifying gas system, an automatic ignition system, oxygen supplying and compressing oxygen cycle balancing system and an automatic control system, the furnace body comprises a main furnace body and furnace body, the gas reaction purifying gas system comprises a high temperature gas reactor, an air guide pipe, an air return pipe, a fuel gas purifying gas stove and gas leading-out pipe, the oxygen supplying and compressing oxygen cycle balancing system comprises high temperature resistant nozzle, main oxygen supplying pipe, a pressurizing oxygen supply pipeline, a blower and pressurized oxygen cycle. This utility model is a firewood waste gas automatic generator furnace, provided with low cost, easy to operate, easy to characteristics of maintenance, long service life, fast gas production, gas flow, gas purity, high thermal value, no smoke, no smell, no waste water, no tar, safe and environment-friendly, efficient and energy-saving, dry and wet material thickness is not limited, civil and industrial are capable of large range and so on.
NOVELTY - Nano microbial organic and inorganic fertilizer comprises 5-40 pts. wt. layered silicate, 0.1-0.25 pts. wt. Bacillus megaterium, 0.1-0.25 pts. wt. B.mucilaginosus, 0.1-0.25 pts. wt. B.subtilis and 235-510 pts. wt. base fertilizer containing nitrogen, potassium and phosphorus element, where the nitrogen, potassium and phosphorus element are 6-18% of total weight of the base fertilizer.    USE - As nano microbial organic and inorganic fertilizer (claimed).    ADVANTAGE - The fertilizer provides nutrition required by crops and is environment-friendly as it decomposes nitrogen, potassium and phosphorus fertilizers adsorbed and fixed in the soil thereby avoiding soil damage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the fertilizer which involves (a) culturing B.megaterium and B.mucilaginosus strains and obtaining spores, (b) adding and mixing nitrogen, potassium and phosphorus elements and crushing to obtain base fertilizer and (c) adding layered silicate to the base fertilizer obtained in step (b) and spores obtained in step (a), mixing the mixture, granulating and drying granules.
NOVELTY - This utility model claims a kind of synthesis gas methanation flow transformation period operation reaction device, belonging to the field of coal chemical industry. The reaction device comprises a reactor unit and a heat exchange device, wherein the reactor unit is divided into three layers of a packed bed catalytic reactor, six through a disconnecting valve with a connecting pipe, the heat exchange device comprises a raw material pre-heating heat exchanger and a heat recovery heat exchanger, the said heat recovery heat exchanger is connected with a raw material pre-heating heat exchanger by the pipeline so as to product gas with waste heat to the raw material gas preheating, in practice according to the need, also can be the three reactor units connected to a combination so as to improve the content of methane in the product gas and improve the stability of the whole process. This utility model of device performance is stable, the equipment investment and operation cost is low, and it can prolong the service life of the catalyst.
NOVELTY - Garage type straw batch fermentation device, a use of the first, the second, the third, the fourth, the fifth yeast on together at the same time a gas, but also can work independently, in designing a plurality of biogas liquid spray head, increase yield of marsh gas. Using seal for anaerobic base, at the same time, adding proper amount of anaerobic bacteria and other living garbage and so on to realize the biogas production. Convenient user, high production efficiency, simple structure, strong adaptability. A production unit for farmers, waste utilization, it can protect environment and economy.
NOVELTY - This utility model claims a kind of kitchen garbage anaerobic digestion tank shell breaking device, the liquid level height parallel position is provided with a stirring paddle of the tank on the vertical axis of the stirrer, the inner end of the overflow pipe is provided with a loudspeaker; The upper part of the anaerobic digestion tank is provided with a circulating spraying pipe, the inner end of the circular spraying pipe alignment horn discharge opening, the outer end of the circulating spraying pipe is connected with the circulating pump. The scum layer and by continuously rotating the stirrer and a circulating spraying pipe for spraying, the liquid level position crust and a scum layer, crushing discharged from the horn discharge opening overflow. Can effectively crushing big blocks the shell to prevent the solid impurity blocking the discharge port.
NOVELTY - Method of preparing biomass sandy soil improving agent, involves soaking wooden meal, adding horse dung (10-15%), mixing uniformly, adding beneficial decomposing organisms and preparing mixed bacterial liquid, diluting the bacterial liquid for 3-4 times, spraying the bacterial liquid on the raw material, stirring and mixing uniformly, continuously inoculating for at least 5 weeks, providing enough oxygen and humidity of 70-80%, then inoculating earthworm, standing for 72-96 hours, and obtaining biomass sandy soil modifying agent.    USE - The method is useful for preparing biomass sandy soil improving agent.    ADVANTAGE - The method is simple, cost-effective and easy to perform. The agent improves nutritional content and retains water capacity of sandy soil.
NOVELTY - Producing organic fertilizer with plant charcoal and bamboo vinegar, involves preparing plant charcoal, preparing bamboo vinegar, proportioning primary raw materials, carrying out vacuum pressurizing treatment and extrusion pelleting, stirring uniformly, where the primary raw materials are plant charcoal, bamboo vinegar and crystallized mother liquor containing abamectin, vacuum-pressurizing, adding crystallized mother liquor into the tank, pressurizing and treating for 15-30 minutes, and extruding-prilling the product.    USE - The method is useful for producing organic fertilizer with plant charcoal and bamboo vinegar (claimed).    ADVANTAGE - The total nutrient and sum of organic matter mass fraction of the organic fertilizer prepared with plant charcoal and bamboo vinegar are improved.    DETAILED DESCRIPTION - Method for producing organic fertilizer with plant charcoal and bamboo vinegar, involves preparing plant charcoal, preparing bamboo vinegar, proportioning primary raw materials, carrying out vacuum-pressurizing treatment and extrusion pelleting, stirring uniformly, where the primary raw materials are 40-60 pts. wt. plant charcoal, 15-25 pts. wt. bamboo vinegar and 20-30 pts. wt. crystallized mother liquor containing 10-20% abamectin, vacuum-pressurizing by filling the raw materials into a vacuum pressurizing tank, vacuumizing till the vacuity is -0.015 to -0.025 MPa, preparing 3-10 pts. wt. crystallized mother liquor into the tank, pressurizing till the pressure is 0.1-0.8 MPa and treating for 15-30 minutes, and extruding-prilling the product.
NOVELTY - Extraction of caffeine comprises drying tea, crushing, sieving to 40-80 meshes to obtain tea powder, mixing tea powder and 60-95% ethanol at weight ratio of 1:2-16, putting mixed solution into bottle, putting in microwave oven at microwave radiation, and setting power of microwave oven to 0.1-0.35 kW; and after 1-15 minutes, taking out bottle, cooling, filtering, concentrating in vacuum, adding 5 g neutralizing precipitator and sublimator, evaporating solvent at 160-195 degrees C water bath, sublimating for 2-5 times, and obtaining caffeine.    USE - Method for extracting caffeine (claimed).    ADVANTAGE - The method has short reaction, high extracting efficiency, high product purity and no toxicity, and is simple, easy, safe and convenient, environment-friendly and low in energy consumption.
NOVELTY - Extraction of sugar crystal xylose comprises diluting xylose mother liquor to 45-60% mass concentration, passing at 35-80 degrees C through cross-flow type membrane, ultrafiltering liquid, collecting into ultra-filtration liquid tank, and discoloring; and carrying-out ion exchange treatment, inoculating yeast to ferment, fermenting liquid, centrifugally separating yeast, passing through cross-flow treating domestic sewage by multilevel biomembrane filtration, processing xylose ultrafiltration, discoloring, processing ion exchange, evaporating, and crystallizing to obtain xylose.    USE - Method of extraction of sugar crystal xylose (claimed).    ADVANTAGE - The method is simple, has low cost, high separation precision, good separation effect, high product yield, greatly reduces steam in production process, saves energy and reduces consumption, and is suitable for industrial production.    DETAILED DESCRIPTION - Extraction of sugar crystal xylose comprises diluting xylose mother liquor to 45-60% mass concentration, passing at 35-80 degrees C through cross-flow type membrane, with membrane aperture of 1000 Da to 1 mu m ultrafiltration membrane, ultrafiltering liquid, collecting into ultra-filtration liquid tank, and discoloring; carrying-out ion exchange treatment, respectively collecting constituent of xylose, glucose and galactose, sterilizing and inoculating yeast to ferment, fermenting liquid, centrifugally separating yeast, fermenting clear liquid, passing through cross-flow treating domestic sewage by multilevel biomembrane filtration, and obtaining ultrafiltration clean liquid; and processing xylose ultrafiltration, discoloring, processing ion exchange, evaporating, and crystallizing to obtain xylose.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the extraction of sugar crystal xylose.
NOVELTY - Bio-fuel pellet comprises a mixture formed of a first ingredient including combustible organic material, and a second ingredient including alginate, where the first and second ingredients are combined together and the resulting mixture is shaped to form a cylindrical pellet, and the second ingredient functions as a retention agent to maintain the size and shape of the cylindrical pellet.    USE - Used as bio-fuel pellet.    ADVANTAGE - The pellet: is of high quality (resilience and appearance); utilizes retention agent that is free of starch for retaining the ingredients, thus allowing greater range of available ingredient configurations and increasing conversion rate of usable animal product that leads to greater value, and reduces manufacturing cost as amount of heat and/or pressure required may be reduced or even eliminated; is produced with lower percentage of damaged and/or unusable articles due to breaking, crushing, premature disintegration; exhibits fewer fines and are more robust (e.g. more resistant to crumbling and crushing) during handling, improved application and longevity; and is biodegradable and digestible in certain applications, stable that are resistant to disintegration, moisture, rain or even placement within water, and buoyant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for forming bio-fuel pellets, comprising: mixing the first ingredient with a second ingredient; and pelletizing the combined first and second ingredients to form individual pellets.
NOVELTY - A gas separation device comprises a rapid cycle kinetic pressure swing adsorption apparatus (100) comprising an adsorbent structure. The adsorbent structure comprises a kinetic adsorbent comprising a molecular sieve with an average pore size of less than 3.9 Angstrom , preferably greater than or equal to 3.7 Angstrom . The adsorbent structure has a macroporosity of 4-18%, and macropore size of 0.001-2 microns. The adsorbent structure is a parallel passage structured adsorbent comprising a laminated adsorbent sheet. The adsorption apparatus is a rotary rapid cycle kinetic pressure swing adsorption apparatus.    USE - As a gas separation device for separating carbon dioxide from a gas mixture comprising methane and carbon dioxide (claimed).    ADVANTAGE - The present rotary pressure swing device is not only configured to perform one complete pressure swing adsorption (PSA) cycle for each rotation of the rotor, but also configured to perform a greater number of PSA cycles per rotation, such as two, three or four. Including more than one PSA cycle per rotation can be advantageous for efficient product production and for other process considerations, such as to distribute pressure loads more evenly around the circumference of the device and to reduce the overall rotation speed of the device for a given PSA cycle speed.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of rotary gas separation device.    Rotary pressure swing device (100)    Rotor assembly (102)    Upper stator assembly (104)    Lower stator assembly (106)    Axle (114)    Rotor housing (119)
NOVELTY - Fire starter, which is a manufactured article fabricated from a composition comprising (a) pine straw, (b) vegetable oil, (c) one or more natural resins, and (d) an herbal component, is claimed.    USE - Used as fire starter.    ADVANTAGE - The fire starter is manufactured from renewable natural materials. The fire starter is safer to use when cooking food, green, it would emit no smoke, no petroleum byproducts, no chemicals, and would leave a minimum ash residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process to manufacture the fire starter, comprising: drying the pine straw; pulverizing the pine straw; preparing a liquid mixture or emulsion of the vegetable oil, at least one natural resin, and the herbal component; blending the liquid mixture or emulsion into the pulverized pine straw until a uniform blend is formed; weighing the blend; transferring the blend into a die; and pressing the blend in the die to compress the slurry and to form it into a desired shape.    DESCRIPTION OF DRAWING(S) - The figure shows an isometric view of the fire starter.
NOVELTY - Processing method of used coffee powder involves solubilizing used-coffee powder containing process liquid in solubilization tank (1) under anaerobic conditions, methane-fermenting solubilized liquid in a methane fermentation tank (2), supplying the liquid to centrifugation portion and separating to solid and liquid. In a solubilization tank, alkali is added from a pH-control portion (12) and pH of methane fermentation tank is adjusted. In centrifugation portion, free higher fatty acid and sludge generated by methane fermentation tank are made to transfer to liquid phase, and are removed.    USE - Processing method of used coffee powder (claimed).    ADVANTAGE - The method is carried out efficiently and economically, by recovering biogas.    DETAILED DESCRIPTION - Processing method of used coffee powder involves solubilizing used-coffee powder containing process liquid in solubilization tank under anaerobic conditions, methane-fermenting solubilized liquid in a methane fermentation tank, supplying the liquid to centrifugation portion and separating to solid and liquid. In a solubilization tank, alkali is added from a pH-control portion and pH of the methane fermentation tank is adjusted. In the centrifugation portion, free higher fatty acid and sludge generated by the methane fermentation tank are made to transfer to liquid phase, and are removed. The sludge is returned and concentration is calculated. An INDEPENDENT CLAIM is included for processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of processing method of used coffee powder using processing apparatus.    Solubilization tank (1)    Methane fermentation tank (2)    Mixing tank (10)    Heating portion (11)    PH-control portion (12)
NOVELTY - Water electrolysis apparatus has an electrolysis cell with pneumatically isolated cavities for hydrogen and oxygen, connected to a power supply unit which is electrically connected to a process parameter control system, as well as a water supply system with a reaction water reserve, having hydrogen and oxygen gas separators, and a cooling system for the hydrogen gas separator, the input hydraulic line of which is fitted with a temperature sensor. After launching the electrolysis cell, the value of electrolysis current is measured and if it is less than a given value, the supply of reaction water is cut, and once it reaches the given current value, the supply of water through the cavity for hydrogen of the electrolysis cell is resumed with a flow rate which ensures constant water temperature at the outlet of said cavity. When current drops, the supply of reaction water into the cavity for oxygen is resumed.    USE - Chemistry.    ADVANTAGE - Invention increases energy efficiency, operating speed and safety of operation of the water electrolysis apparatus, and also reduces the dependency thereof on secondary sources of energy and ambient conditions.2 cl, 2 dwg
NOVELTY - An oil extractor comprises a salt having a potassium, a manganese, a sulfur and an oxygen.    USE - As oil extractor, particularly useful for algae oil extraction. Also useful for a hydrocarbon extraction extracting a hydrocarbon from waste water produced from one of an oil-refining and a chemical engineering processes (claimed). The nanowires are used in household cleaners, and motor oil adsorption treatment.    ADVANTAGE - The oil extractor has an appearance of nanowire. The nano-extractor for algae oil is inexpensive, safe and environmentally friendly, high selective for absorbing oil. The addition of nanowire material can lower interfacial tension between oil and water, and the nanowire material can serve as adsorbent to promote the separation of oil within the solution. Additionally, since the size of nanowire material is small, thus the nanowire material can adsorb algae oil in the algae bodies, and then the algae oil is recovered by utilizing the density difference between oil and water to enhance the efficiency of oil displacement. The nanowire material in the higher polar solvent renders aggregation phenomenon, while in the lower polar solvent, shows a size distribution of less than one micron. The nanowire materials of less than one micron reduce the oil-water interfacial tension, and thus penetrating the cell membrane or cell wall of the algae.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the extractor involving: providing a solution having potassium ions, manganese ions, sulfur-containing ions and an oxygen dissolved in it; and heating the solution to obtain the extractor.
NOVELTY - The hydrogen generator system (100) includes an internal pump (150), arranged within a cartridge housing (112), which transports a liquid reactant (122) through a liquid reactant flow path (160) formed within the cartridge housing. An external pump (180), arranged outside the cartridge housing, pumps a fluid to operate the internal pump.    USE - Hydrogen generator system for fuel cell system (claimed).    ADVANTAGE - Allows depleted reactants to be easily and economically replaced, and maximizes the number of components that can be reused. Ensures excellent reliability, safety, and a simple design which promotes easy manufacture at a low cost. Is highly resistant to leaks of harmful or corrosive liquids, and is highly resistant to malfunctioning due to accumulation of solids in lines, valves and the like.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of hydrogen generator system.    Hydrogen generator system (100)    Cartridge housing (112)    Liquid reactant (122)    Internal pump (150)    Liquid reactant flow path (160)    External pump (180)
NOVELTY - A hydrogen generating apparatus (100) comprises source gas route (10) which supplies source gas to hydrodesulfurization device (20) which reduces concentration of sulfur compound present in source gas. The obtained source gas is reformed using modifier (30), to obtain hydrogen-containing-gas. A portion of obtained gas is recycled to heater (60) which heats the source gas and recycled gas and supplies resultant source gas to source gas route. A controller is provided to control the heating temperature of heater.    USE - Hydrogen generating apparatus is used for generating hydrogen-containing-gas for fuel cell system for generating electric power (all claimed).    ADVANTAGE - The hydrogen generating apparatus has suppressed degradation of hydrodesulfurization device.    DETAILED DESCRIPTION - A hydrogen generating apparatus comprises source gas route which supplies source gas to hydrodesulfurization device which reduces concentration of sulfur compound present in source gas by hydrogenation reaction. The obtained source gas is reformed using modifier, to obtain hydrogen-containing-gas. A portion of obtained gas is recycled to heater which heats the source gas and recycled gas and supplies resultant source gas to source gas route. A controller is provided to control the heating temperature of heater, such that the temperature of the source gas supplied to hydrodesulfurization device is less than dew point of source gas. 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 the schematic view of hydrogen generating apparatus.    Source gas route (10)    Hydrodesulfurization device (20)    Modifier (30)    Heater (60)    Hydrogen generating apparatus (100)
NOVELTY - The heat exchanger has a cylindrical shell (1) whose inside is supplied with thermal medium. An inside of a hollow portion (4a) is supplied with solid from an upper direction. Heat is exchanged between the solid substance and the thermal medium. The heat-exchanged solid substance is intermittently discharged by a discharging apparatus (9). The discharging apparatus is provided in a downward solid substance exit of the hollow portion. A pair of opening-and-closing portion is linearly slid to a horizontal direction.    USE - Heat exchanger for solid substance such as carbide material, used for processing facility of organic waste such as sewage sludge (all claimed) used as fuel in electric generating facility.    ADVANTAGE - The installation space required for the heat exchanger can be reduced, and the big heating-surface area of the exchanger can be ensured. Since the discharge of the solid substance can be made intermittent, the driving force required by the discharging apparatus can be reduced. Hence the generation of the damage to the components by the abrasion can be reduced, and the cost of the exchanger can be reduced. The generation of dust in the exchanger can be suppressed, and the leakage of internal gas in the exchanger can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing facility of the organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the heat exchanger.    Shell (1)    Solid substance supply port (2)    Solid substance discharge port (3)    Hollow portion (4a)    Discharging apparatus (9)
NOVELTY - Producing bioethanol from banana pseudostem by enzymatic hydrolysis, involves washing banana pseudostem with water thrice to remove the dirt and the resin and then putting the washed material in an oven at 60 degrees C for drying. The dried material is stored and treated by enzymatic hydrolysis. The material is treated with sodium hydroxide, sulfuric acid and hydrogen peroxide in magnetic stirrer at 70 degrees C. Acetic acid, hydrogen peroxide and distilled water are added to the mixture at 70 degrees C. The obtained material is filtered and washed with distilled water at pH 4-5 and then dried.    USE - Method for producing bioethanol from banana pseudostem by enzymatic hydrolysis.    ADVANTAGE - The method enables to produce bioethanol from banana pseudostem efficiently.
NOVELTY - Preparing substituted benzamide compounds (VIc) comprises (a) converting benzaldehyde compounds (IIc) to 4-((3,5-dichloro-pyridin-4-ylimino)-methyl)-benzene-1,2-diol compounds (Vc) in a one-pot reaction, and (b) oxidizing (Vc) under conditions.    USE - The process is useful for preparing (VIc) (claimed), which is useful for treating skin disorder such as dermatoses.    ADVANTAGE - The process simply and safely prepares (VIc) with high yield and without using caustic or dangerous reagents such as thionyl chloride and sodium hydride in an economically and environmentally friendly manner.    DETAILED DESCRIPTION - Preparing substituted benzamide compounds of formula (VIc) comprises (a) converting benzaldehyde compounds of formula (IIc) to 4-((3,5-dichloro-pyridin-4-ylimino)-methyl)-benzene-1,2-diol compounds of formula (Vc) in a one-pot reaction, and (b) oxidizing (Vc) under conditions.R1, R2 = 1-4C-alkyl (optionally substituted with F), H, 1-6C-alkyl, 3-7C-cycloalkyl or 3-7C-cycloalkylmethyl.    INDEPENDENT CLAIMS are included for:    (1) the compounds (Vc); and    (2) 4-dihydroxymethyl-benzene-1,2-diol compounds of formula (IIIc).    Either R4, R5 = 1-6C-alkyl or acyl; or    R4+R5 = 5-7 member cyclic ring (optionally substituted).
NOVELTY - Bioreactor for methanizing biomass according to the principle of dry fermentation, comprises: an elongated reactor vessel with a bottom on which the biomass rests, and which comprises a first end and a second end (14); a first gas-tight port arranged at the first end, for loading the reactor vessel with fresh biomass; a biogas discharge port; and a second gas-tight port arranged at the second end for discharging spent biomass from the reactor vessel.    USE - The bioreactor is useful for methanizing biomass according to the principle of dry fermentation.    ADVANTAGE - The bioreactor ensures reduced risk of contamination of the spent biomass with respect to biomass, with respect to epidemiologic hygiene and plant hygiene, and thus the spent biomass is harmless.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biogas plant comprising a number of biogas reactors for producing biogas in batch mode; and    (2) operating the bioreactor or the biogas plant, comprising (a) loading the reactor vessel with fresh biomass through the first port, (b) generating biogas by methanation of the biomass on the principle of dry fermentation in a thermophilic region, and (c) unloading the low-germ spent biomass through the second port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the bioreactor.    Side wall (6)    Second end (14)    Second retaining device (22)
NOVELTY - The microorganisms reaction tank for sludge treatment (1) has a cylindrical inner tank (3) which is arranged inside an outer tank (2). A circulation rate control device (4) is provided on the cylindrical inner tank. A cylindrical control plate (5) is provided to upper periphery of cylindrical inner tank. A raw water supply port (10) is provided in circulation path of water to be treated which circulates inside the inner tank and outer tank. A treated water discharge port (11) is provided to upper portion of outer tank.    USE - Microorganisms reaction tank for performing activated sludge treatment of waste water.    ADVANTAGE - The raw water supply port is provided in circulation path of water to be treated which circulates inside inner tank and outer tank, and treated water discharge port is provided to upper portion of outer tank. Thus, the microbial reaction tank is utilized to enable continuous anaerobic/aerobic microbial treatment to be carried out even if the reaction tank has large capacity and enable construction costs to be controlled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a wastewater treatment method containing an activated-sludge treatment process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the microorganisms reaction tank.    Microorganisms reaction tank (1)    Outer tank (2)    Cylindrical inner tank (3)    Circulation rate control device (4)    Cylindrical control plate (5)    Raw water supply port (10)    Treated water discharge port (11)
NOVELTY - The method involves supplying (AA) the generated sludge (DD) from the microorganism reaction tank (HH) to the natural water aeration adjustment tank (CC) to which the waste water (BB) before the process is supplied. The adjusted process natural water is supplied (FF) to the reaction tank after carrying out aeration adjustment of the natural water with which the sludge is mixed, so that an oxidation-reduction potential becomes a positive value in the natural water aeration adjustment tank. The discharge water (II) from the reaction tank is used (GG) as an effluent (JJ).    USE - Activated-sludge processing method for repairing waste water treatment facility installed in foodstuff manufacturing plant (all claimed) for manufacturing roll cake, used for processing sludge such as organic type coagulant and inorganic type coagulants e.g. aluminum sulfate.    ADVANTAGE - The activated-sludge processing method which does not discharge the amount of surplus sludge is obtained by establishing the microorganism reaction tank. Since the sludge storage tank and the water-removal device become unnecessary, the installation area of the waste water treatment facility can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for repair method of existing waste water treatment facility.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the activated-sludge processing process. (Drawing includes non-English language text)    Step for supplying generated sludge to natural water aeration adjustment tank (AA)    Waste water (BB)    Natural water aeration adjustment tank (CC)    Sludge (DD)    Step for supplying adjusted process natural water to reaction tank (FF)    Step for using discharge water from reaction tank as effluent (GG)    Microorganism reaction tank (HH)    Discharge water (II)    Effluent (JJ)
NOVELTY - The method involves supplying the sludge produced by processing in a pressure floatation concentration-separation tank (DD), to the microorganism reaction tank (II). The raw water separated from the pressure floatation concentration-separation tank is supplied to the dilute activated-sludge aerator (GG). The sludge and discharge water (HH) produced by processing in the microorganism reaction tank are supplied to the dilute activated-sludge aerator. The raw water separated from the dilute activated-sludge aerator is supplied to the sedimentation tank (JJ).    USE - Method for processing activated-sludge used for waste water treatment in waste water treatment facility (claimed).    ADVANTAGE - The discharge of surplus amount of sludges can be controlled by supplying the portion of sludge produced by the supply of activated-sludge aerator to the raw water aeration adjustment tank. The existing waste water treatment facility can be repaired by establishing the microorganism reaction tank. Since the activity of activated sludge is maintained at high state, the plumping of dilute activated sludge and the production of process trouble phenomenon by the foaming scum can be decreased. The cheaper sludge-disposal expense can be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for repairing the existing waste water treatment facility.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the process for processing activated-sludge. (Drawing includes non-English language text)    Pressure floatation concentration-separation tank (DD)    Dilute activated-sludge aerator (GG)    Sludge and discharge water (HH)    Microorganism reaction tank (II)    Sedimentation tank (JJ)
NOVELTY - A Rhizobium strain KB10 (KCTC 12131BP) capable of stimulating growth of Botryococcus braunii, is new.    USE - The Rhizobium strain KB10 is useful for stimulating growth of B.braunii strain which is used in mass-production of biodiesel (all claimed).    ADVANTAGE - The strain enables to increase oleic acid content up to 9 times more, which is high-quality biodiesel component, and solve contamination caused by other microorganisms during open culture process for producing biodiesel using mixed culture of the bacteria, and produce biodiesel cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for stimulating growth of B.braunii strain, involves culturing Rhizobium strain KB10 and B.braunii strain; (2) mass-production method of fatty acid, involves culturing Rhizobium strain KB10 and B.braunii strain; (3) microbe form for fatty acid and biodiesel mass productions comprising co-culture liquid of the strains as an active ingredient; and (4) method for preparing biodiesel, involves converting the produced fatty acid into biodiesel.
NOVELTY - A recombinant microorganism comprising a disrupted chromosomal nifL gene and a chromosomal nifA gene operably linked to a heterologous constitutive promoter, where the microorganism is capable of fixing atmospheric nitrogen in presence of fixed nitrogen and oxygen and does not comprise antibiotic resistance marker gene, is new.    USE - In the preparation of fertilizer composition for enhancing the fertility of the soil (claimed).    ADVANTAGE - The microorganism such as recombinant Azotobacter is capable of fixing atmospheric nitrogen in presence of fixed nitrogen and oxygen and does not comprise antibiotic resistance marker gene; increases the yield of the crop plants; reduces the degradation of soil; reduces the application of chemical nitrogenous fertilizers in agriculture; and reduces environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) new recombinant Azotobacter having Accession number MTCC 5679, where the Azotobacter is capable of fixing atmospheric nitrogen in presence of fixed nitrogen and oxygen and does not comprise antibiotic resistance marker gene; 2) new recombinant DNA molecule comprising a disrupted chromosomal nifL gene and a chromosomal nifA gene operably linked to a heterologous constitutive promoter; 3) a recombinant vector comprising the recombinant DNA molecule; 4) a process of producing the recombinant microorganism; and 5) a process of producing the recombinant Azotobacter; 6) a composition comprising the recombinant microorganism or the Azotobacter.
NOVELTY - Reducing moisture content of a flowable organic raw material e.g. wood chips or wood shavings, which has an initial moisture content, comprises: continuously feeding the raw material into a mechanical, continuous press; mechanically pressing the material in the continuous press to form a pourable intermediate material having an intermediate product moisture; and thermally drying the intermediate product moisture of the intermediate material to form a pelletizable bulk material having a processing moisture.    USE - The raw material is useful for producing pellets, foodstuffs or healthcare products, and an etheric end product (claimed).    ADVANTAGE - The method makes use of the press that is robust, less error-prone and enables processing of coarse raw materials in an easy manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing pellets from the flowable raw material having an initial moisture content, comprising processing the raw material by the above mentioned method into a pelletizable bulk material, which has a processing moisture, and pressing the pelletizable bulk material into pellets;    (2) producing foodstuffs or healthcare products from the compressed liquid obtained by the above mentioned method during mechanical pressing, comprising purifying the extruding liquid to obtain a material; and    (3) producing an etheric end product from the compressed liquid obtained by the above mentioned method during mechanical pressing, comprising extracting wood constituents e.g. oils and resins from the compressed fluid.
NOVELTY - Multiple stage fermentation process comprises: contacting a mixture of multiple sugars with one or more strains of yeast, where a first portion of the sugars is converted by the yeast according to a first fermentation process; contacting a second portion of the sugars with one or more strains of bacteria, where the second portion of the sugars are converted by the bacteria according to a second fermentation process; and contacting at least one of the first portion of the sugars and the second portion of the sugars with an enzyme, where one or more of the sugars is a substrate for the enzyme.    USE - The multiple stage fermentation process is useful for producing alcohol, preferably ethanol (all claimed), organic acids, preferably citric acid, acetic acid, itaconic acid, lactic acid and gluconic acid, ketones, preferably acetone, amino acids, preferably glutamic acid, gases, preferably hydrogen and carbon dioxide, antibiotics, preferably penicillin and tetracycline, enzymes vitamins, preferably riboflavin, B12 and beta -carotene, and hormones.    ADVANTAGE - The process produces ethanol in an economical and environmentally friendly manner.
NOVELTY - A synthesis method of polyhydroxyalkanoate using microorganism comprises a microorganism preparation step, a fermentation tank preparation step, a fermentation and culturing step, and a withdrawal step. First, the bacterial strain Ralstonia eutropha is prepared, and then a fermentation tank is prepared, in which the crude glycerol is injected. The carbon-to-nitrogen ratio in the fermentation tank is 20:1 to 150:1, and the temperature is maintained at 20 to 45 DEG C. Then the bacterial strain Ralstonia eutropha is added into the fermentation tank, mixed therein to maintain aeration and dissolved oxygen amount, and fermented for 48 to 96 hours to allow proliferation of the bacterial strain Ralstonia eutropha and synthesis of the polyhydroxyalkanoate from the crude glycerol in the bacteria. Finally the bacterial strain Ralstonia eutropha is removed, disrupted, and extracted to obtain the polyhydroxyalkanoate. In this invention, the crude glycerol, a byproduct of biodiesel, is used as the carbon source to reduce the costs, and the condition is controlled to enables microorganism to metabolize the crude glycerol and synthesize the polyhydroxyalkanoate with enhanced yield.
NOVELTY - A 9-azanoradamantane N-oxyl compound (I) is new.    USE - New 9-azanoradamantane N-oxyl compound used for organic molecule oxidation catalyst for oxidation method of alcohol e.g. primary alcohol. Uses include but are not limited to pharmaceuticals, pharmaceutical raw materials, agricultural chemicals, cosmetics, organic materials and high value-added organic compounds.    ADVANTAGE - The primary alcohol is selectively and efficiently oxidized in polyol substrate having several alcohols under environmentally-friendly conditions in a short period of time using the 9-Azanoradamantane N-oxyl compound.    DETAILED DESCRIPTION - A 9-azanoradamantane N-oxyl compound of formula (I) is new.    R1,R2=H or alkyl group, where at least one of R1 and R2 is H and the other is alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) organic molecule oxidation catalyst, which contains the 9-azanoradamantane N-oxyl compound (I); and    (2) oxidation method of alcohol, which involves oxidizing alcohol in presence of the 9-azanoradamantane N-oxyl compound (I) and synthesizing corresponding oxo component.
NOVELTY - The device has a counter-gasification reactor (R) provided with a fixed bed gasification agent, which is fed through a supply pipe, a gas pipe, a droplet separator and a gas flaring. Exhaust gas is transported form the reactor through an exhaust gas pipe (G) that is inclined relative to an outer wall of the reactor. The exhaust gas pipe is connected with a water jacket (WD) that is filled with hot water.    USE - Biomass gasification device for sewage sludge.    ADVANTAGE - The device allows free and unhindered flow of gas from gasification plant to the sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification device.'(Drawing includes non-English language text)'    Exhaust gas pipe (G)    Counter- gasification reactor (R)    Water jacket (WD)
NOVELTY - Composition comprises (for 1 ton water) 30-40 g chlorine dioxide, 2-3 g citric acid, 3.5-4.5 g nano-minerals, 2-3 g surfactant.    USE - The composition is useful for preventing scuticociliatosis in fish (claimed), which is a parasitic infection caused by scuticociliate.    ADVANTAGE - The scuticociliatosis can be treated in an environmentally friendly manner using the composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preventing scuticociliatosis in fish, comprising (a) taking chlorine dioxide, citric acid and nano-minerals, (b) mixing at least one solvent (ethanol or hydrogen peroxide) and surfactant, (c) mixing (a) and (b), and (d) bathing the cultured fish for 1-2 hours by introducing the mixed composition in water form.
NOVELTY - The catalyst has mixing portion (110) that mixes oxidizer supply gas with fuel anode exhaust gas exhausted from fuel anode of fuel cell stack. A combustion unit (130) is connected to mixing portion for heating up oxidizer supply gas within mixing gas. The combustion unit is provided to burn unreacted fuel among fuel anode exhaust gas. A promotion element (116) is provided to promote even flow of mixing gas within mixing portion so that flame generation according to mixing of oxidizer supply gas and fuel anode exhaust gas is steadily ignited.    USE - Catalytic combustor for fuel capacitor.    ADVANTAGE - The promotion element can be provided to promote the even flow of the mixing gas within the mixing portion, so that the flame generation according to the mixing of the oxidizer supply gas and fuel anode exhaust gas can be steadily ignited. The size of the combustion unit can be reduced. The problem of the transmitted adsorption generated in the entrance of the combustion unit can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view showing the catalytic combustors.    Mixing portion (110)    Inflow opening of waste gas (112)    Feed gas inlet port (114)    Combustion unit (130)
NOVELTY - Invention refers to gas industry and can be used at gas condensate fields, immediately at sites of gas preparation for transportation or at centralised sites of preparation of instable gas condensate for transportation or processing. The invention refers to the method of obtaining liquid ethane from instable gas condensate, which involves separation of gas condensate in a rectifying column into three flows, two gas ones - methane and ethane, and one liquid - deethanised condensate, ethane gas flow separation with a side shoulder of the rectifying column, which is located on the level of gaseous phase containing ethane free from methane, and further condensation of ethane flow and extraction of liquid ethane from condensed ethane flow.    USE - Oil and gas industry.    ADVANTAGE - Enlarging the range of products, improving their quality and low-temperature properties.1 ex
NOVELTY - Invention relates to catalyst for production of molecular hydrogen. Invention covers the application of organic stable electron-excess radicals as catalyst for electrochemical production of molecular hydrogen.    USE - Process engineering.    ADVANTAGE - Lower costs, application of available and harmful catalysts.2 ex
NOVELTY - This utility model claims a marsh gas heating drying machine, comprising a shell body, a shell driven by the gear box, the inner shell is provided with inclined blade causing material, above the right end is provided with a lower hopper, right middle part of the lower end is provided with a high temperature air inlet, the left upper part of the front end is provided with waste heat air outlet, a waste heat through air inlet pipe and a hot air device, the lower end of the left part is provided with a downwardly inclined discharging pipe, wherein the drying machine further comprises a marsh gas furnace, gas furnace burning warm air generated by the hot air by introducing high temperature air inlet of the dryer. This utility model use biogas produced in high warm-air heating drying material, at the same time, waste heat air outlet of the dryer and a hot air distribution device connected with the air distribution device can be set in the fermentation tank, the weight of garbage, in the tank to store high pressure emitting device and a hot air heating method, fast fermenting domestic garbage. Marsh gas so as to generated a high warm and drying waste heat can be recycled, which not only saves energy, but also reduces the environment pollution.
NOVELTY - The invention claims a high frequency and super-biomass pyrolysis without oxygen heating furnace, comprising a furnace body (1), a high frequency and super-audio heating system (2), feeding system (3), a limiting pressure sliding door device (4), a carbon discharging pipe (5), water tank (6), heat insulation and heat preservation device is composed of (7). This utility model adopts oxygen-free indirect heating method, and the whole process is a high frequency and super-heat the furnace body, which increases the temperature of the biomass destructive distillation furnace, converting it into speed (rate) and the economical efficiency of the black is capable of use as a fuel gas, oil and waste biomass carbon. This utility model is a safe and reliable, the underground water and surface water and atmospheric pollution has no pollution in the garbage organic degradable material without strict requirement, generating a combustion gas power generation, at the same time, also can be a heavy oil, carbon powder obtain benefit.
NOVELTY - This utility model claims a gasification furnace with multiple air nozzle air supply device, is connected to the upper part (8) and the lower pipe (3) is mounted on the outer insulating layer (9) and the inner heat preservation layer (10), a head pipe (2) are respectively connected with the fan (1) and the upper part (8) and the lower pipe (3), the upper part (8) and the lower pipe (3) is connected with air pipe (11) is connected with the first annular pipe on the cross wind pipe (11) (7), the second annular pipe (4) and the third annular pipe (5), the cross wind pipe (11), the first annular pipe (7), the second annular pipe (4) and the third annular pipe (5) is provided with more than 1 of the gas nozzle (6). This kind of multi-air-nozzle air supply device is suitable for wide application range, stable and uniform, which is suitable for large and medium is straw or domestic garbage gasification furnace or fuel gas-generating stove of raw fuel to the air supply, is practical and popularization value.
NOVELTY - A suction type paragraphs except tar-free straw furnace, the utility model claims an energy-saving product field, a suction type paragraphs except tar-free straw furnace, comprising a furnace body, a furnace cover, a furnace body and a furnace cover connected with tar removing device, upper part of the furnace body is provided with a sealing device, lower part of the furnace body is provided with ash door, the bottom of the furnace body is provided with a furnace gas hole, the furnace body comprises a first sleeve by a connecting pipe connected with a tar removing device is provided with a water inlet part and a tar, a gas outlet is provided with three return cooling device for removing tar in the three return cooling device, a second sleeve, a third sleeve, the first sleeve and the second sleeve and the second sleeve and the third sleeve is provided with the upper part, a first sleeve, a second sleeve, a third sleeve component is connected with the water tank, and the second sleeve is provided with a baffle plate, a first sleeve, the third sleeve is provided with an inner sleeve, wherein the inner sleeve, the first sleeve is connected with the connecting pipe, the third sleeve, the sleeve and the gas outlet is connected with the tar removing device is set at the lower part the overflow pipe, the overflow pipe is connected with the second sleeve. Beneficial effects, improve the effect of cooking, warming and reduces the environmental pollution.
NOVELTY - This utility model claims a biomass dense forming fuel automatic production line, comprising a material feeding part, a forming part, a sieve mechanism and the cooling conveyor, feeding part is composed of a belt, a roller sieve and a horizontal machine which are connected in turn, a drum screen for sieving the impurity in the material, the material and form a modulation to extrude, so as to form the finished product pressing block, forming part of which are connected in turn, at least one spiral modulator, at least one extrusion moulding machine, at least one small belt discharging machine and the finished product discharging machine is composed of a sieving finished product discharging mechanism is set on the front end of the screening mechanism for screening the biomass product pressing block; cooling conveyor to the qualified finished product pressing block; This utility model can realize continuous production, uniform feeding, discharging, bagging directly, so that the production efficiency and yield, saves a large amount of labour force, reduces the production cost and so on.
NOVELTY - This utility model claims biomass fuel block production device, belonging to the technical field of biomass fuel block automatic production device. Wherein, the mud pump is connected with the upper feeding port of the double-head dewatering machine I, a dewatering machine I is connected under the inclined belt conveyor I, the inclined lower part of the belt conveyor I is provided with a material storage box, a storage box of the lower part is provided with an inclined belt conveyer II, the other lower end of the belt conveyor II is provided with a silo conveyor I, a silo transmission mechanism I and the other end is inserted into the roller dryer, the lower discharge hole of the roller dryer is connected with the dryer cylinder, drying cylinder the other one end is connected with the dryer discharging opening, lower part drying silo discharge hole is provided with a transmission mechanism I port, upper auger conveyor I lower port of the other silo is provided with a middle transmission mechanism II. The utility model has advantages of simple structure, low cost, it does not need drying by natural cooling is not limited by the weather, the machine by dehydrating, drying and purifying biomass raw material, drying, extruding and moulding the continuous and automatic biomass fuel block.
NOVELTY - A mineral catalytic bed biomass fast pyrolyzing device comprises a feeding system, a heat carrier gas system, ore catalytic-bed pyrolyzing reactor, a gas-solid separation and carbon collecting system, condensing system and a pyrolysis tail gas processing system. Device of biomass raw material into the mineral catalytic-bed pyrolyzing reactor by feeding system, the carrier gas and heated by the hot carrier gas system enter into mineral catalytic-bed pyrolyzing reactor, the biomass raw material fast pyrolysis under the hot carrier gas and mineral bed material catalysis to produce volatile matter and coke and the carrier gas through gas-solid separation and carbon collection system to remove coke particles enter into fractional condensation system is direct spraying cooling and indirect cooling are combined with the condensed mode, the condensable part is fully condensed biological oil. Pyrolysis tail gas by pyrolysis tail gas processing system, the hot carrier gas system as auxiliary combustion burner. The device speed is fast pyrolysis, pyrolysis compare total yield of biomass oil, the oil is good, the operation cost is low.
NOVELTY - This utility model is a kind of biomass fuel gasification hot water furnace, comprising a gasification furnace, wherein the gasification furnace comprises a furnace tube, the furnace tube is provided with a hearth is connected with a jacket-type, jacket-type water tank is connected with the hearth is set in the middle of the air outlet chamber at the lower end of the furnace tube, the bottom of the jacket-type water tank are respectively connected with the air outlet chamber of the main ash outlet and an air outlet, the air outlet is connected with an air outlet pipe, a jacket type water jacket is provided with a water outlet and the water inlet is provided with a water heat exchanger on the air outlet pipe, wherein the water heater comprises a water tank, the upper part of the water tank is provided with an upper air chamber, the lower part of the water tank is provided with a gas chamber, is connected with the upper water tank is provided with a gas-guide tube and a plurality of lower air chamber. This utility model uses biomass fuel forming the flammable gas with the heat used to heat the water, so as to improve the utilization rate of the combustible gas and the waste of energy, it has simple structure, convenient use, high heat utilization more sufficient and more environment-friendly.
NOVELTY - Biogas wet desulfurization includes adding 3-10 mg/L cobalt phthalocyanine sulfonate (PDS) into a container to dissolve, adding pre-activated catalyst to form PDS-Sx catalyst system, continuously keeping the PDS concentration at 3-10 mg/L, introducing hydrogen sulfide (H2S)-rich methane into the desulfurization tower, countercurrent contacting with the desulfurization solution for chemical absorption reaction under PDS catalysis, discharging the H2S-rich liquid from the bottom of absorption tower, passing through a solution circulating groove, and conducting oxidative regeneration reaction.    USE - Wet desulfurization of biogas (claimed) useful for internal combustion engine.    ADVANTAGE - The biogas after desulfurization has H2S concentration of less than 200 mg/m3. The method achieves improved desulfurization rate and can recycle elemental sulfur.    DETAILED DESCRIPTION - Biogas wet desulfurization comprises desulfurization and oxidation regeneration. The desulfurization step comprises adding 3-10 mg/L PDS into a container to dissolve, adding pre-activated catalyst to form PDS-Sx catalyst system, continuously keeping the PDS concentration at 3-10 mg/L, introducing H2S-rich methane into the desulfurization tower, and countercurrent contacting with the desulfurization solution for chemical absorption reaction under PDS catalysis. The oxidation regeneration comprises discharging the H2S-rich liquid from the bottom of absorption tower, passing through a solution circulating groove, vacuum pumping into regeneration tank, conducting oxidative regeneration reaction, and introducing the purified biogas into gas storage cabinet through soft pipe, which is connected with a main air path.
NOVELTY - Marsh gas power generation comprises mixing crushed straw and water at a mass ratio of 1:2, adding water and inoculum, stirring and sealing for 3-7 days, inoculating in a fermentation tank, adding fresh chicken manure and water at a mass ratio of 1:1 to obtain a water content of 91-95%, discharging the mixture in a sealed anaerobic fermentation reactor at 35-50 degrees C and at a pH of 6.8-7.2, and fermenting for 12 hours to 5 days; carrying out solid-liquid separation classification; and carrying out desulfurization, and carrying out heat and power cogeneration.    USE - Method for marsh gas generation (claimed).    ADVANTAGE - The method fully utilizes all kinds of straw materials of agricultural products.
NOVELTY - The utility model claims a straw excrement mixing organic fertilizer granulator, the straw excrement mixing organic fertilizer granulator comprising a feeding hopper, and roller wheel, prilling die plate, a discharging hopper, a primary granulator hopper, a primary polishing machine hopper, a secondary granulator hopper, a secondary polishing machine hopper, a granulator motor, a secondary granulator belt transmission system, a primary granulator belt transmission system, a primary granulator motor, a speed reducer and a main motor granulator, a granulating machine is provided with a main motor, a machine part is provided with a machine case, machine case, main shaft is the output shaft of the motor is connected with the universal joint, a speed reducer and a main shaft, the upper end of the main shaft is connected with the prilling die plate, the die plate and is provided with roller wheel. The straw excrement mixing organic fertilizer granulator low manufacturing cost, high fertilizer effect, organic fertilizer particle volatile fertility can partially replace the chemical fertilizer is widely applied to agriculture production and reduces the environment pollution caused by chemical fertilizer for farmer production cost.
NOVELTY - The utility model claims a marsh gas tank, specifically to a soft inner liner of the marsh gas tank, comprising a soft liner digestion tank, a feeding port, a discharging port, an air outlet, a water pressure chamber, a tank body, a brick concrete precast cover plate, wherein the brick tank body corner use arc, one side is provided with a feeding opening, and feeding pre-embedded pipe, the other end of the first side is provided with a discharging at the bottom of the pool pre-embedded discharge pipe, the bottom of the feeding port side discharging port of the lower slope, soft liner is brick building tank body, feed inlet and feed outlet and the liquid outlet are respectively connected with inlet and outlet pipe and a liquid outlet pipe set is embedded, the air outlet of the soft liner is connected with purifier, marsh gas pump, the stove, marsh gas tank top is covered by cement precast cover plate. This utility model adopts the PVC soft type liner design, when the pressure in the tank is not enough, and it can be used methane pump outputting marsh gas, the discharge port is set on the bottom of the digestion tank discharging completely between the biogas slurry flows into the liquid outlet, is convenient for extracting PVC soft film has good air tightness, low construction cost is low.
NOVELTY - Obtaining of composition of tungsten carbide with platinum, which has increased electrocatalytic activity, temperature decrease of electrochemical synthesis of target product, as well as increase in target product synthesis speed at reduction of electric energy costs, is the technical result of the proposed invention. Electrochemical synthesis of composition of tungsten carbide with platinum involves electrolyte containing sodium chloride, potassium chloride, cesium chloride, sodium fluoroxitungstate and platinum chlorhydric acid. Electrolysis is performed in a three-electrode quartz cell, where a glassy carbon crucible serves as a cathode, at the temperature of 550 degrees C, at current densities of 0.1-1.0 A/cm, and carbon dioxide is used as a carbon source.    USE - Electricity.    ADVANTAGE - New generation of fuel elements and electrolysers for electrochemical formation of hydrogen. 2 ex
NOVELTY - A continuous feeding straw carbonization device comprises feeding push rod (1) located inside the feeding cylinder (2) connected with the heater (3) located inside the temperature control tank (4) which is connected to the exhaust pipe (5) installed with one-way valve (6), and is connected to the gas collecting device (10); and discharge cylinder (8) located at the bottom of the tank installed with discharge push rod (7) and closed pressure valve (9).    USE - Continuous feeding straw carbonization device.    ADVANTAGE - The device solves the problems such as low processing efficiency, low carbon, high carbon emission and exhaust gas contains an amount of harmful component of the existing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of continuous feeding straw carbonization device.    Feeding push rod (1)    Feeding cylinder (2)    Heater (3)    Temperature control tank (4)    Exhaust pipe (5)    One-way valve (6)    Discharge push rod (7)    Discharge cylinder (8)    Closed pressure valve (9)    Gas collecting device (10)
NOVELTY - A refining method comprises mixing crude proton pump inhibitor, catalyst, and mixture of salt and alcohol compounds; heating mixture; adding active carbon to decolor; stirring; filtering while hot; and cooling to precipitate crystals. The catalytic agent is metal zinc or metal nickel.    USE - Refining method used for reducing amine oxide of proton pump inhibitor (claimed).    ADVANTAGE - The method is environment-friendly and simple, has low cost, and improves yield, quality, and purity of product.
NOVELTY - Biomass is quickly pyrolyzed to obtain bio-oil. The bio-oil is distilled at normal pressure to separate heavy-component distillate and light-component distillate, where the main component of distillate is 2-9C compound. The distillation residue tar is mixed with biomass and subjected to pyrolysis and distillation.    USE - Usage method of biomass to produce 2-9C chemical products e.g. organic carboxylic acid, aldehyde, ketone, ester, alcohol, and phenolic compound, and to produce bioenergy (all claimed).    ADVANTAGE - The method is simple, convenient and economical, and does not require bio-oil preprocessing, high pressure/vacuum operation, and any additional reagent.
NOVELTY - Lime and zeolite are injected into livestock waste in container, phosphorus and nitrogen contained in the mixture are removed, and air purification is performed. The resulting product is separated. Sulfated aluminum and caustic soda are injected into water, purified and dehydrated. The dehydrated product is subjected to far infrared radiation and dried. Sawdust, rice husk, carbon and waste wood are mixed to obtained product and naturally dried. The dried mixture is mixed with adhesive and dye, mixed, milled, agitated, compression-molded and pelletized to obtain color pellet.    USE - Manufacture of color pellet.    DETAILED DESCRIPTION - Livestock waste is stored in a container and stirred. Lime and zeolite are injected into the container, phosphorus and nitrogen contained in the mixture are removed, and air purification is performed. The resulting product is separated into livestock waste and wastewater. Impurities contained in wastewater are removed. Sulfated aluminum and caustic soda are injected into water, purified and dehydrated. The dehydrated product is subjected to far infrared radiation and dried. Sawdust, rice husk, carbon and waste wood are mixed to obtained product. The obtained mixture is naturally dried. The dried mixture is mixed with adhesive and dye, mixed, milled, agitated, compression-molded and pelletized to obtain color pellet.
NOVELTY - Bipolar electrolysis unit includes a block of electrodes equally spaced from each other and provided with holes for passage of hydrogen-oxygen mixture and electrolyte. Block of electrodes is placed in a shell from dielectric material. Shell encloses the electrodes without any gaps. The shell is submerged into the housing of electrolysis unit with electrolyte. At the same time, the housing with electrolyte can contain at least one additional block of electrodes in shells. Blocks of electrodes are electrically connected to each other in parallel or in series.    USE - Metallurgy.    ADVANTAGE - Improvement of an electrolysis unit. 2 cl, 3 dwg
NOVELTY - Processing of molasses alcohol wastewater comprises pre-processing pig manure wastewater with water, diluting molasses alcohol wastewater; processing bagasse, spraying wastewater granular sludge and pig manure mix, filling reactor with water, adding nickel chloride (NiCl2), cobalt chloride (CoCl2) to accelerate granular sludge formation; diluting molasses alcohol wastewater, circulating in reactor, recycling until no gas formation, carrying out continuous operation for 7 days; and taking molasses alcohol wastewater chemical oxygen demand (COD) and pig wastewater, reacting for 3-4 days.    USE - Method for processing molasses alcohol wastewater (claimed).    ADVANTAGE - The removal rate of wastewater COD is 72%, and pure methane production is 2.45 m3 per day.    DETAILED DESCRIPTION - Processing of molasses alcohol wastewater comprises:    (A) pre-processing pig manure wastewater with water at mass ratio of 1:50 for 3-5 days, passing through 25 mesh sieve, taking filtrate wastewater, diluting molasses alcohol wastewater to COD concentration of 293110-347800 mg/L;    (B) processing 0.4 m3 bagasse, spraying wastewater granular sludge and 200 kg pig manure mix, and 30% total volume of reactor working volume, filling reactor with water, adding NiCl2, CoCl2 every 4 g to accelerate granular sludge formation;    (C) diluting molasses alcohol wastewater 10 times to COD final concentration of 29311 mg/L, flow rate is 15 m3/hour, circulating in reactor, after two days, completing cycle until COD removal rate is 60%, gradually reducing inlet COD of water, recycling until no gas formation, carrying out continuous operation for 7 days; and    (D) taking molasses alcohol wastewater COD and pig wastewater at mass ratio of 3:1-3:2, controlling total COD at 4000-7000 mg/L, and reacting for 3-4 days.
NOVELTY - The device has a mixer connected with a heat exchanger. The heat exchanger is connected with a lower part of a tower-type fixed bed reactor through a preheater. A condensing system is connected with the heat exchanger. First condenser is connected with the heat exchanger, and second condenser is connected with an oil tank. Third and fourth condensers are connected with a gas storage tank. A tower type fixed bed reactor i.e. reaction kettle, is connected to an upper end tubular fixed bed reactor that is divided into first stage reactor and second stage reactor.    USE - Device for producing bio-diesel from waste illegal cooking oil and waste engine oil.    ADVANTAGE - The device can produce bio-diesel with better temperature fluidity and stable product quality. The tower-type fixed bed reactor is applied to catalytic cracking reaction, so that heating convenience is improved, investment and operating cost are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing bio-diesel from waste cooking oil and waste engine oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for producing bio-diesel from waste illegal cooking oil and waste engine oil.
NOVELTY - An ethylene cracking raw material preparing method involves subjecting hydrogenated light C5 fraction raw materials to hydrogenation reaction by a hydrogenation catalyst fixed bed in the presence of hydrogen to convert unsaturated hydrocarbons in the light C5 fraction raw materials to saturated hydrocarbons. Part of the hydrogenation products is returned as solvents and passed through the hydrogenation catalyst fixed bed together with the raw materials. The hydrogenation products as the solvents are desulfurized by a desulfurizer fixed bed before being mixed with the raw materials.    USE - Method for preparing an ethylene cracking raw material.    ADVANTAGE - The method enables hydrogenating the light C5 fraction materials with 0.002 wt.% active sulfides, and ensuring the long-period operation of the desulfurizer and the hydrogenation catalyst.    DETAILED DESCRIPTION - An ethylene cracking raw material preparing method involves subjecting hydrogenated light C5 fraction raw materials to hydrogenation reaction by a hydrogenation catalyst fixed bed in the presence of hydrogen to convert unsaturated hydrocarbons in the light C5 fraction raw materials to saturated hydrocarbons. Part of the hydrogenation products is returned as solvents and passed through the hydrogenation catalyst fixed bed together with the raw materials after being mixed with the raw materials, where the feeding weight ratio of the hydrogenation reaction product solvent and the hydrogenated light C5 fraction raw materials is 1:(6-10). The hydrogenation products as the solvents are desulfurized by a desulfurizer fixed bed before being mixed with the raw materials, where volume liquid hourly space velocity is 3-16 hr-1, pressure is 0.2-0.6 MPaG and the feeding temperature is 5-60 degrees C, the desulfurizer is a copper (Cu2+) modified Y type molecular sieve, and the content of copper in the molecular sieve is 1.6-4.8 wt.%.
NOVELTY - The system has a roller extruding machine connected to a fuel gas generator that is arranged on an upper end of a fuel gas furnace body. Column particle fuel is injected into the generator. A fuel gas furnace body is connected with a fuel gas-generating stove. A steam pipe (2-15) is connected to a grate transmission shaft (2-1). The transmission shaft is connected with a main shaft (2-8). A gas mixing pipe (2-17) is formed with a grate transmission shaft hole. The steam pipe is connected to a grate transmission shaft via a transmission component that is connected with a motor.    USE - Pulverized coal mud biomass molded fuel gas column particle preparing system.    ADVANTAGE - The system reduces production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a pulverized coal mud biomass molded fuel gas column particle preparing system.'(Drawing includes non-English language text)'    Grate transmission shaft (2-1)    Main shaft (2-8)    Hearth (2-11)    Steam pipe (2-15)    Gas mixing pipe (2-17)
NOVELTY - The generator has a furnace body (3) opened with a feeding port (5). A lower part of the furnace body is provided with a dust hopper (1). An upper part of an inner container is provided with a storage hopper (8). An inner wall of the furnace body (4) is connected with an air inlet (7) whose pipeline (10) is fixed in a blower (12). An upper part of an ash bucket is provided with an air outlet (2). A lower part of the body is protruded inward to form a wedge bump (9).    USE - Biomass fuel gas generator.    ADVANTAGE - The generator is simple and convenient to operate, and has high heat value and stable combustion to generate tar gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass fuel gas generator.    Dust hopper (1)    Air outlet (2)    Furnace body (3)    Inner wall of furnace body (4)    Feeding port (5)    Air inlet (7)    Storage hopper (8)    Wedge bump (9)    Pipeline (10)    Blower (12)
NOVELTY - Saccharifying raw bagasse by using ion liquid resistance bacteria and the cellulose enzyme involves extracting the DNA of strain to culture, and shaking culture of bacteria sp.; freeze-drying powder cellulase; pre-processing ionic liquid 1,3-phosphate to dissolve at 120 degrees C to 30 minutes, adding bagasse and sodium acetate buffer solution whose pH value of 4.8 to form ionic liquid/solvent system; and then in-situ enzymolysis bagasse with cellulose in ionic liquid/solvent system at 50 degrees C and the constant temperature shaking.    USE - For saccharifying raw bagasse (claimed).    ADVANTAGE - The method is simple and two-step method as compared with the existing ionic liquid treatment bagasse; has high efficiency; and is economical process.    DETAILED DESCRIPTION - Saccharifying raw bagasse by using ion liquid resistance bacteria and the cellulose enzyme involves extracting the DNA of strain to culture, shaking culture of bacteria sp.; freeze-dried powder cellulase: culturing the fermentation liquid by centrifuge 8 minutes to remove thalli, after ammonium sulfate precipitation to obtain active protein, activated protein further freezing and drying to obtain cellulose; drying cellulose powder in enzymolysis of bagasse: pre-processing ionic liquid 1,3-phosphate to dissolve at 120 degrees C to 30 minutes, adding bagasse and sodium acetate buffer solution whose pH value of 4.8 to form ionic liquid/solvent system; and then in-situ enzymolysis bagasse with cellulose in ionic liquid/solvent system at 50 degrees C and the constant temperature shaking.
NOVELTY - Composite microorganism flocculating agent comprises Bacillus mucilaginosus (30-50%), Bacillus subtilis (10-25%), Saccharomyces cerevisiae (20-40%) and Penicillium diversum (10-20%), where total bacteria count of the flocculating agent is greater than one billion per gram.    USE - The composite microorganism flocculating agent is useful for treating waste leachate sewage (claimed).    ADVANTAGE - The composite microorganism flocculating agent accelerates degradation of the organic matters in the waste percolate and removal of heavy metal, reduces sludge yield and lowers waste water recovery cost, and has stable water quality and low ammonia nitrogen content.    DETAILED DESCRIPTION - Preparing the microorganism flocculating agent comprising culturing Bacillus mucilaginosus, Bacillus subtilis, Saccharomyces cerevisiae and Penicillium diversum, curing the cultured bacteria and then filtering by adding biological fermentation liquid of microorganism thalli using a 1-5 nm gap filter film, concentrating to obtain concentrated fermentation liquid, adding and uniformly mixing obtained concentrated fermentation liquid (5-8%) and sodium alginate with weight ratio of 100:1-100:1.5, adding calcium chloride solution (0.08-0.15 mol/l) to the fermentation liquid with volume ratio of 1:3-1:5, slowly stirring and then adding sodium ion and calcium ion, gradually hardening calcium alginate and then curing for 3-5 hours, adding chitosan solution (4-6 g/l) and film-forming embedding particle with weight ratio of 2:1:4, and then reacting for 15-30 minutes, filtering and washing with physiological saline.
NOVELTY - A sea water desalting water supply system comprises natural energy generating device, hydrogen generator, hydrogen storage, hydrogen fuel battery, solar energy heat exchange device and vacuum distillation device.    USE - Sea water desalting water supply system.    ADVANTAGE - The system reduces production cost of fresh water.
NOVELTY - Forming (S)-3-methylamino-1-(2-thienyl)-1-propanol involves taking 3-methylamino-1-(2)-1-acetone as substrate, where the substrate is performed asymmetric reduction reaction in the presence of a biological catalyst (preferably ketone reductase), co-factor and cofactor regeneration system (preferably glucose and glucose dehydrogenase). The asymmetric reduction reaction is carried out at pH of 6-8 in water phase buffer solution in the initial state in the reaction system of the substrate at a concentration of 100-150 mg/ml. The ketone reductase with the substrate have mass ratio of 1-2%.    USE - For preparing (S)-3-methylamino-1-(2-thienyl)-1-propanol (claimed).    ADVANTAGE - The method reduces the usage of enzyme; has low production cost; is high-efficiency biological conversion process; and is suitable for industrialization.    DETAILED DESCRIPTION - Preparing (S)-3-methylamino-1-(2-thienyl)-1-propanol involves taking 3-methylamino-1-(2)-1-acetone as substrate, where the substrate is performed asymmetric reduction reaction in the presence of a biological catalyst, co-factor and co-factor regeneration system to form (S)-3-methylamino-1-(2-thienyl)-1-propanol. The biological catalyst is ketone reductase. The co-factor regenerating system comprises glucose and glucose dehydrogenase. The coenzyme is pyrroloquinoline quinone. The asymmetric reduction reaction is carried out at pH of 6-8 in a water phase buffer solution in the initial state in the reaction system of the substrate at a concentration of 100-150 mg/ml. The ketone reductase with the substrate 3-methylamino-1-(2)-1-acetone have mass ratio of 1-2%.
NOVELTY - A Mikania micrantha n-butanol extract comprises 4-10 wt.% ferulic acid and 4-10 wt.% chlorogenic acid.    USE - The M.micrantha n-butanol extract is useful in preparation of herbicide for paddy field (claimed) to inhibit normal weeds in farmlands.    ADVANTAGE - The M.micrantha n-butanol extract has good quality due to the presence of ferulic acid and chlorogenic acid. The herbicide containing M.micrantha n-butanol extract can substitute the existing chemical herbicide for greatly improving the safety of pesticides. The M.micrantha n-butanol extract has a great significance to economic benefits and social benefits, and removes the harm of the M.micrantha.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) preparation of the above-cited M.micrantha n-butanol extract, involves taking dry M.micrantha and crushing into crude powder, adding 95% ethanol to the powder, refluxing, extracting and recycling the ethanol to obtain the extract, further extracting the extract respectively using petroleum ether, ethyl acetate and n-butanol, decompressing and recycling the n-butanol and drying to obtain dry extract; and (2) herbicide comprises M.micrantha n-butanol extract as active ingredient.
NOVELTY - The modified electrode has a working electrode that electrolysis the water. A catalyst material is deposited on the working electrode. The catalyst material is contained with the cobalt or nickel. The working electrode is made of carbon material. The carbon material is selected from one of graphite, carbon nanotubes, amorphous carbon or glassy carbon. The working electrode is graphite rod electrode.    USE - Modified electrode for catalyzing electrolytic water.    ADVANTAGE - The manufacturing process of modified electrode can be simplified. The modified electrode can be operated conveniently. The electrolytic water can be catalyzed effectively. The power consumption of modified electrode can be reduced. The catalyzing efficiency of water can be improved. The application rate of modified electrode can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of modified electrode for catalyzing electrolytic water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modified electrode.
NOVELTY - The system has a turbine connected with a low pressure heater that is provided with a steam pipeline. A biomass gasification device is connected with a pipeline of low pressure heater and provided with multiple low pressure heaters. Multiple high pressure heaters are connected in series. The low pressure heater and a condenser are provided with a pipeline. An inlet pipe and an outlet pipe of the low pressure heater are connected with an outlet pipe of the biomass gasification device and the steam pipeline.    USE - Hybrid power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hybrid power generation system.
NOVELTY - The device has two baffle plates non-sequentially connected with three closed spaces. An air inlet pipe is extended into the first closed space that is formed with a sealed box body. A connecting pipe is located in the box body. An end of the connecting pipe is extended into the first closed space. The connecting pipe is connected with the second closed space. Another connecting pipe is located in the box body and extended into the second closed space. An air outlet pipe is extended into the second closed space.    USE - Device for eliminating noise generated in a fuel cell air transmission device during discharge of gas in a tank car and filling gas in a tube line.    ADVANTAGE - The device has better noise reducing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device for eliminating noise generated of a fuel cell air transmission device during discharge of gas in tank car and filling gas in a tube line.
NOVELTY - Drying and cooling sieving integrated machine, belonging to the field of feed processing equipment technology field. It comprises a drying cylinder and a cooling cylinder is inclined to the drying cylinder and the cooling cylinder set with air inducing mechanism, and the other end of said drying cylinder is provided with feeder, the other end of the cooling cylinder body provided with cylinder sieve. The said drying cooling screening machine, compact in structure, reasonable in design, drying, cooling, screening a part is tightly combined, small volume, light weight, low energy consumption, short process flow, small investment, small floor area, reduces the labour cost, and it is in favour of industrialized production.
NOVELTY - Straw for preparing quickly-available potassium fertilizer rich in potassium, organic alcohol and carbon dioxide comprises straw cleaning machine, kettle for dissolving straw, fermentation tank, carbon dioxide collector, alcohol distilling device, polyacetal trap device, solid-liquid separating device, drying device, crusher, purification and dewatering device and spray-drying tower.    USE - As device i.e. straw for preparing quickly-available potassium fertilizer rich in potassium, organic alcohol and carbon dioxide (claimed).    ADVANTAGE - The straw is capable of regenerative and reuse without pollution and waste; and is energy-saving.
NOVELTY - Cellulase enzymolysis pine needle extracting resveratrol by crushing pine needle, adding distilled water, and mixing them uniformly, adding cellulase enzymolysis and water, and soaking, carrying out ultrasonic extraction, extracting solution, vacuum pumping, filtering, repeatedly extracting filter residue, and combining crude extract liquid to concentrate; removing impurities, tracking and monitoring using thin-layer chromatography, and collecting resveratrol section eluent, and concentrating the eluent, recrystallizing the rough crystal, vacuum freezing and drying to obtain the resveratrol.    USE - Method for cellulase enzymolysis pine needle extracting resveratrol (claimed).    ADVANTAGE - The method is simple and environment-friendly, has low cost, and can provide resveratrol product having high purity.    DETAILED DESCRIPTION - Cellulase enzymolysis pine needle extracting resveratrol comprises:    (A) crushing pine needle, adding distilled water for 5-10 times at room temperature, and mixing them uniformly;    (B) adding 0.05 by weight of cellulase enzymolysis, adding water with 95 mass% ethanol solvent, and soaking for 2 hours;    (C) carrying out ultrasonic extraction, extracting solution, vacuum pumping, filtering to obtain crude extract liquid, repeatedly extracting the filter residue with 75-95% ethanol solvent for 2 times, and combining the crude extract liquid to concentrate, where the concentrated extracting solution on polyamide resin;    (D) using 35% ethanol for removing impurities from solvent, using 75-95% ethanol solvent, tracking and monitoring using thin-layer chromatography, and collecting resveratrol section eluent; and    (E) concentrating the eluent to obtain crude crystal, recrystallizing the rough crystal for 4 times with ethanol, vacuum freezing and drying to obtain the resveratrol.
NOVELTY - A device comprises a main pipe containing calamine cream or battery, and a U-shaped measuring pipe arranged at 10-30 cm far away from the bottom of the main pipe, where the diameter of the main pipe is 14.5-25.0 mm and volume scales are marked on the outer wall of the measuring pipe.    USE - Device for determining an expansion rate of a battery and calamine cream and a hydrogen evolution amount of zinc powder (claimed).    ADVANTAGE - The method enables detecting hydrogen evolution amount of the zinc powder in an accurate manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for determining an expansion rate of a battery and calamine cream and a hydrogen evolution amount of zinc powder using the device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device.
NOVELTY - The system has a measuring device provided with a natural gas and carbon monoxide measuring device sensor. A micro-processor is connected with a gas well with a gas well alarm device. The microprocessor is connected with a wireless signal transmitting module that is connected with a wireless signal receiving module through a wireless network.    USE - Gas well harmful gas monitoring system.    ADVANTAGE - The system has simple structure and smart design, and can monitor the concentration of harmful gas in the gas well, and remind municipal department about harmful gas leakage.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gas well harmful gas monitoring system. '(Drawing includes non-English language text)'
NOVELTY - Natural purification, deodorization and treatment of urban domestic sewage and industrial sewage in biological fluidized bed reactor comprises setting biological fluidized bed reactor with natural purifying and deodorizing system, feeding activated sludge, controlling anoxic state of aeration reactor, adding biological proliferation nutrients, acclimatizing heterotrophic and chemoautotrophic microorganism in activated sludge, modifying into deodorant predominant microflora and proliferating; and transferring into multi-structure processing unit sewage treatment plant, and treating sewage.    USE - Method for naturally purifying, deodorizing and treating urban domestic sewage and industrial sewage in biological fluidized bed reactor (claimed).    ADVANTAGE - The device has simple maintenance.    DETAILED DESCRIPTION - Natural purification, deodorization and treatment of urban domestic sewage and industrial sewage in biological fluidized bed reactor comprises setting biological fluidized bed reactor with natural purifying and deodorizing system in sewage treatment plant, feeding activated sludge into reactor, controlling anoxic state of aeration reactor, adding biological proliferation nutrients, acclimatizing heterotrophic and chemoautotrophic microorganism in activated sludge, modifying into deodorant predominant microflora and proliferating; and transferring into multi-structure processing unit sewage treatment plant, and treating sewage while naturally purifying odor. An INDEPENDENT CLAIM is included for the components biological fluidized bed reactor.
NOVELTY - The device has a hopper (1) connected with a feeding system (2) i.e. two-stage spiral feeder. A cold sand heating system (6) comprises cyclone heat exchangers. An air outlet opening is connected with a cyclone heater. An inlet is connected with the cyclone heater. A discharge opening of the cyclone heat exchangers is connected with a fluidized bed quick pyrolysis reactor (3). A lower end opening of the fluidized bed quick pyrolysis reactor is connected with the cyclone heater. The inlet is connected with a sand box to directly supplied cold sand. Flue gas is discharged into atmosphere.    USE - Device for quickly pyrolyzing biomass to prepare bio-oil.    ADVANTAGE - The device obtains high temperature sand and realizes self-heating type biomass fast pyrolysis to prepare the bio-oil.    DETAILED DESCRIPTION - The fluidized bed quick pyrolysis reactor is a fast fluidized bed reactor. An INDEPENDENT CLAIM is also included for a method for quickly pyrolyzing biomass to prepare bio-oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for quickly pyrolyzing biomass to prepare bio-oil.'(Drawing includes non-English language text)'    Hopper (1)    Feeding system (2)    Fluidized bed quick pyrolysis reactor (3)    Gas-solid separation system (4)    Cold sand heating system (6)
NOVELTY - The method involves adding water vapor as gasifying agent in a fluidized bed reactor, and feeding continuously biomass carbon to the reactor. Gasification reaction is performed under conditions of 700-950 degree Celsius of reaction temperature and water/carbon ratio of 1:5 to generate hydrogen-rich gas with hydrogen as main component.    USE - Method for preparing hydrogen-rich gas by biomass carbon.    ADVANTAGE - The method can be implemented in a simple manner, and enables controlling reaction condition in an easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a hydrogen-rich gas preparing method.'(Drawing includes non-English language text)'
NOVELTY - A Klebsiella primary amine bacteria (Klebsiella variicola Trb33 strain, March 23, 2012), preserved in China microorganism bacterial strain preservation management committee common microorganism centre, under the preservation number (CGMCCNO. 5933), and having relatively high potassium release function, is new.    USE - For preparing silicate microorganism fertilizer, and decomposing potassium feldspar and mica; and in promoting tobacco growth.    ADVANTAGE - The Klebsiella primary amine bacteria has relatively high potassium release function; can be used for preparing the silicate microorganism fertilizer, and decomposing potassium feldspar and mica; utilizes in the soil silicate mineral to release the soluble potassium from a tobacco to reduce dosage of chemical fertilizer, improve soil micro-environment and to improve tobacco leaf quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing Klebsiella primary amine bacteria, involving: (1) taking Klebsiella primary amine bacteria (Trb33 strain) from tobacco root, inoculating distribution to the inclined plane culture medium, activating for 36-48 hours, at culture temperature of 28-30 degrees C; (2) taking changed Klebsiella primary amine bacteria (Trb33 strain) in the step (1), inoculating in beef extract peptone liquid culture medium, at 28-30 degrees C and 160-200 rotation per minute (rpm) oscillation and cultivating for 24-36 hours.
NOVELTY - A strain Bacillus (Paenibacillus sp.) ZD01, preserved in China Centre for Type Culture Collection, under the address: China, Wuhan, Wuhan University, 430072, the preservation date: November 20, 2012, and the preservation number (CCTCC No: M2012463), is new.    USE - In preparation of microbial extracellular polysaccharides flocculating agent useful in the sewage treatment (claimed) for precipitation of suspended solids, dye and pigment decolorization and removal of heavy metal ions.    ADVANTAGE - The flocculating agent prepared by this method has high suspended particles flocculating activity, suspended reactive dye pigment bleaching activity and heavy metal ion removal activity; is high-efficient microorganism flocculating agent; has potential use in daily life, especially in industrial waste water treatment, particularly in the sewage pretreatment process, where it plays a significant role, in reducing the subsequent processing steps and cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the microbial extracellular polysaccharides flocculating agent, involving: inoculating the Bacillus (CCTCC No: M2012463) to fermentation culture medium, at 28-32 degrees C, and 100-200 rotation per minute (rpm) vortex oscillation cultivating for 3-4 days to obtain the fermentation liquid of the microbial extracellular polysaccharide flocculating agent PE-1, where the fermentation culture medium is composed of the following components: 3-60 of g/l sucrose, 0.1 g/l of yeast extract, 5-8 g/l of peptone, 1-5 g/l of monopotassium phosphate, 0.1-1 g/l magnesium sulfate, 0.01-0.05 g/l of ferric chloride, 0.01-0.05 g/l of manganese; the solvent is distilled water; and the pH is 7-7.5.
NOVELTY - The device has device main portion which is provided with the garbage microwave cracking element through the special pipeline of combustion chamber. The microwave heating temperature of the preset product is sampled and detected.    USE - Device for producing water electrolysis hydrogen using garbage microwave cracking secondary combustion.    ADVANTAGE - The environmental protection and easy automatic control of the device can be attained. The energy of the device can be saved. The generation of dioxin can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the device for producing water electrolysis hydrogen. (Drawing includes non-English language text)
NOVELTY - A high-efficient straw rotten agent comprises: 20-30 wt.% of Bacillus subtilis, 10-15 wt.% of Streptomyces albogriseolus, 5-10 wt.% of Buckle sac within Neurospora, 5-10 wt.% of Candida utilis, 10-15 wt.% of Aspergillus niger, 10-15 wt.% of Paecilomyces lilacinus, 10-15 wt.% of Trichoderma harzianum, and 20-30 wt.% of thermophilic bacteria.    USE - As high-efficient straw rotten agent (claimed) as fertilizer.    ADVANTAGE - The straw rotten agent protects the environment, improves the soil and the fertilizer utilization ratio, improves product number, quality and development of ecological agriculture comprehensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-efficient straw rotten agent involving: under the sterile condition, inoculating the Aspergillus niger, Paecilomyces lilacinus and Trichoderma harzianum in culture medium, and culturing for 4 days at 32 degrees C; inoculating the Candida utilis in the culture medium at 32 degrees C for 3 days, inoculating the thermophilic bacteria at 45 degrees C for 3 days, inoculating the Bacillus subtilis in nutrient agar culture medium, at 30 degrees C for 3 days, inoculating the Streptomyces albogriseolus in culture medium, at 30 degrees C for 5 days; and inoculating the Buckle sac within Neurospora in liquid amplification culture medium; and mixing the inoculates, followed by drying, crushing and sieving.
NOVELTY - Production of alcohol (liquor) involves using plant straw biomass containing carbohydrate as raw material, hydrochloric acid and ammonia water as auxiliary material, and pre-hydrolysis of the biomass into pool (tank), followed by hydrolyzing, neutralizing, and fermenting to obtain alcohol mash, and performing distillation of alcohol mash, to obtain alcohol (liquor).    USE - For producing plant straw biomass alcohol such as wine (claimed).    ADVANTAGE - The method has low conversion rate, high yield and low cost.
NOVELTY - The method involves providing gasification fuel in two burning layers. An air inlet device is provided on one of the layers. Partial combustion of the air inlet device is carried out by fire goods. Carbon dioxide is generated on a combustion layer by burning fuel carbon contact via reduction reaction to generate combustible gas carbon monoxide. A fire goods inlet is closed when the biomass gasification furnace works normally. The carbon monoxide is continuously generated by feeding supplementary fuel.    USE - Biomass gasification furnace gasification method.    ADVANTAGE - The method ensures stable biomass gasification furnace, and uniform wind pressure so as to control temperature of the hearth between 600 degrees and 650 degrees. The method ensures connection of drain pipe and drain valve with waste outlet opening so as to preventing the air channel from damage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification furnace hearth air inlet device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace hearth air inlet device.
NOVELTY - The device has a furnace body (1) installed on an inner wall of a furnace liner (3). An upper part of the furnace body is opened with a feeding port (7). A lower part of the furnace body is provided with a dust hopper (2). An upper part of an inner container is provided with an air outlet (4). An upper part of an ash bucket is provided with an air inlet (13) that passes through an air inlet pipe (14). The air inlet pipe is connected with a blower (15). A vibration blanking plate (6) is fixed to an inner part of the inner container. An upper cover of the body is provided with a cover (8).    USE - Biomass fuel gas generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass fuel gas generating device.    Furnace body (1)    Dust hopper (2)    Furnace liner (3)    Air outlet (4)    Vibration blanking plate (6)    Feeding port (7)    Cover (8)    Air inlet (13)    Air inlet pipe (14)    Blower (15)
NOVELTY - This utility model claims a kind of using microorganism technology of multi-level sewage treatment device, comprising a primary filtering device, an anaerobic microorganism reaction generator, an aerobic microorganism reaction generator, two-stage filtering device, a filtering device and a sterilizing device. The water outlet of the water inlet primary filter device is connected with the anaerobic biological reaction generator of the anaerobic bioreactor is a sealed tank body, a filling multi-hole fibre filler, the water outlet anaerobic microbe without the assistant of the response generator is connected with the aerobic microorganism reaction generator of the aerobic microorganism reaction generator is equipped with an aeration device and a rotary stirring device, the aerobic microorganism reaction generator orderly is connected with the secondary filtering device and filtering device, a filter device is connected with the sterilizing device. According to the multi-level device for treating rural domestic sewage by using microorganism technology capable of the domestic sewage and industrial sewage pass through gradually processing, capable of recycling the clean water, it not only can make the water source to be reused, but also avoids the environment pollution.
NOVELTY - This utility model claims a sludge rich oxygen supplying system for garbage fermentation special oxygen supply system, comprising an air pressure and drying system from the air after pressurizing and drying continuously for a plurality of alternating oxygen pressure swing adsorption and analysis of the absorption tower, it can control a plurality of said adsorption tower alternate adsorption and analysis of the automatic switching valve set, the inlet can pass through the top opening of the adsorption switch valve in the automatic switching valve set and a plurality of absorption tower is connected with the oxygen buffer tank, the oxygen supply system is the oxygen in the air by pressure swing adsorption technology, is directly provided to a fermentation system using oxygen instead of air for oxygen, so that the oxygen concentration is increased, the oxygen of the fermentation system, and when the oxygen in the total amount of the fermentation system in the first timing, the oxygen supply system blowing flow rate of the fermentation system to be greatly reduced, not caused by fermentation temperature is reduced due to excessive gas flow ratio of the air.
NOVELTY - This utility model claims a kind of used for production method of organic bio-fertilizer is rotten ferment process device, comprising a fermentation tank body, a stirrer, an electric heater, a filling pipe, a temperature control device, a feeding port, a discharging device, a fan, a stirring motor. Tank wall of the tank body is provided with an electric heater double-layer structure, the upper layer structure is formed in the cavity, and a temperature controller and a temperature sensor connected with the inner part of the tank body is provided with a blade stirrer, and a stirring motor to stir the oxygenation effect, the lower part of the tank body is provided with filling pipe is connected with a fan, improve the effect of oxygenation, tank body upper part is provided with the feeding port, lower part of the tank body is connected with the discharge device. For the production method of organic bio-fertilizer is rotten fermentation process device for water sediment or crop straw as raw material, carrying out micro-organism degradation, it can keep the best material for composting fermentation process condition, and it has good fermentation effect, the quality of the bio-fertilizer is stable, the production cost is low and so on.
NOVELTY - A kind of horizontal aerobic fermentation reactor, comprising a horizontal cylinder, is provided with a stirring device is set in the horizontal cylinder. Pass through jacket pipe is connected with the external interface, the fermentation material fast heating and controlling aerobic fermentation reaction is carried out at proper temperature, which avoids the over-high temperature fermentation so as to induce death and sleep of the aerobic microorganism by driving rotating movement with stirring device of the spiral blade to make the fermentation completely and uniform contact with the oxygen so as to generate aerobic reaction of high speed, generated by aerating flange, the reaction is connected with the external ventilation system for a centralized waste gas treatment discharging, and the reaction heat generated by the recovery to be used. This utility model small floor area, low driving power, environment-friendly and energy-saving.
NOVELTY - A kind of producing urea is a section of decomposition heater, a heat decomposition tower (1), the decomposition heating tower (1) is provided with a urine inlet (11) and a urine outlet (12), the decomposition heating tower (1) is provided with a heating device, the heating device is composed of a steam heating component and the hot water heating part, the decomposition heating tower (1) is set on the upper part of the steam inlet (13), is provided with a condensed water outlet in the middle of the decomposition heating tower (1) (15), a decomposition heating tower (1) is further provided with a hot water inlet (16), the lower part of the decomposing heat tower (1) is provided with a condensing water outlet (17). This utility model adopts the hydrolysis tower liquid outlet for heat exchange, which greatly reduces the consumption of the steam energy. Through the above calculation can be seen, a daily fluid production of 600 tons of urea device, using a section of decomposition heater base is provided, urea can save the steam for 70 kg, a price calculation according to each ton of 150 yuan, year production time to 330 days, namely year recovery benefit.
NOVELTY - A kind of straw gasification furnace, comprising a furnace body is provided with a feeding port, a furnace large cover, wherein the furnace body is provided with a fire-resisting brick, wherein the big furnace cover comprises a furnace cover, a furnace core, an inner cover and a furnace core protection cover on the inner cover and the furnace core, the furnace core and the inner cover to form the first mounting cavity, the inner cover and the furnace core to form the second protective cover is set with cavity, the furnace core comprises a edge of the core body, the core body is provided with a plurality of through holes. This utility model is a straw gasification furnace is provided with the first cavity, the second cavity is set with the two pieces is set with cavity can be used for placing tar absorbing device, absorbing gasification furnace when producing the tar, it is very environment-friendly.
NOVELTY - This utility model claims a kind of straw dry distillation cracking device, comprising a combustion furnace, the combustion furnace body is provided with furnace dry distillation bed and pyrolysis bed, lower part of rotary furnace is mounted with a rotating shaft, a rotating shaft extending in the furnace body extends into the combustion furnace, the dry distillation bed and bed and cracking in the furnace body of the rotating shaft is fixedly connected with the bottom end of the combustion furnace is provided with a discharging port carbon material, carbon material discharging port is connected with the cooler, the air outlet pipe on the combustion furnace is connected with a cyclone separator, the cyclone separator is provided with an exhaust pipe and dust, dust and slag of the cyclone separator. This utility model is featured with simple and smart structure, external gasification furnace is provided with a non-oxygen cover and a heat preservation layer, it can ensure fully reaction, at the same time, using cyclone separator to carbon particles and wood tar recycling, which improves the utilization of energy.
NOVELTY - This utility model claims a kind of combustion energy-saving furnace with biomass straw gasification device, comprising a gasification furnace and a gas storage cabinet, a gasification furnace side is provided with the straw crusher, straw crusher is opposite to the first, feeding port of the gasification furnace is connected with the air outlet of drier is connected outside the gasification furnace is provided with a non-oxygen, oxygen to form an interlayer cover is connected with the gasification furnace, the interlayer is filled with an insulating medium, the bottom of the gasification furnace carbon material discharging opening and a slag cooler, the air pipe on the gasification furnace is connected with a cyclone separator, the cyclone separator is provided with an exhaust pipe and dust, dust to a storage tank, the vent-pipe cyclone separator extends to the cooler, gas storage cabinet is connected with the cooler. This utility model is a simple improved cooling, drying the straw gasification furnace enters the combustion and heating, and the cyclone separator is carbon particle and wood tar recycling use and improve the utilization rate of the energy.
NOVELTY - A kind of straw gasification furnace, comprising a furnace body, a furnace core, inner cover and furnace core of cone cylinder wall is set with protecting cover on the inner cover and the furnace core, the furnace core and the inner cover to form the first mounting cavity, the inner cover and the furnace core to form the second protective cover is set with cavity, the furnace core comprises a edge of the core body, the core body is provided with a plurality of through holes. This new type of furnace cover, furnace core set with a protective cover on the inner cover and furnace core, in this way, to form the first mounting cavity is formed between the furnace core and the inner cover, the inner cover and the furnace core and protective cover to form a mounting cavity, the two is set with cavity for placing the tar adsorption device, it is very environment-friendly.
NOVELTY - This utility model claims a kind of used for straw gasification furnace of the furnace cover is provided with a through hole, a furnace body, a through hole and a lower through-hole through a connecting hole of the lower through-hole is connected with the furnace body is further formed with an annular groove. According to the depth of the annular clamp slot is less than the height of the furnace body. This utility model of the furnace cover is provided with an annular groove, it can use the slot and matched with the furnace when using, has good sealing effect.
NOVELTY - The utility model claims a biomass heating gasification furnace, comprising a gasification furnace and a purifier, wherein the gasification furnace comprises a furnace core and a furnace outer cylinder, a furnace core and a furnace outer cylinder is provided with a water storage chamber, is provided with water return port is provided with a water inlet, the lower part on the upper part of the outer furnace, the furnace core is fixed on the upper part is connected with the chimney of the furnace external cylinder, the middle part of the furnace core is set with the furnace external cylinder, upper part of the furnace core is set at the front side to the feeding port, a furnace core bottom furnace is provided with a fire grate, the fire grate is set at the lower end an ash ash front face is provided with ash opening cover is provided with an air supply opening on the side face of the ash chamber, a purifier and connected with the air inlet, the utility model double-use electric furnace is convenient to use, and safe, the produced gas capable of cooking, boiling water, but also increases the function of burning.
NOVELTY - This utility model claims a kind of heat by a water circulation of the marsh gas tank, comprising a biogas tank and cooling tank, the marsh gas tank comprises a shell body, wherein the shell body is provided with a hot water circulating device, wherein the cooling tank comprises a tank body, wherein the tank body is provided with a waste heat heating cycle, the heat circulator is provided with a hot water inlet and a cold water outlet, a circulator according to waste heat heating is provided with a hot water outlet and a cold water inlet, wherein the hot water inlet is connected with hot water outlet, a cold water outlet is connected with the cold water inlet through the pipeline, said hot water circulating device and waste heat heating circulator are spiral steel pipe structure. This utility model uses waste heat of the waste heat accelerate organic substance to promote marsh gas fast, saves coal, low cost, accelerate cooling tank cooling under the low temperature, the cold and heat exchange, and a the same can produce marsh gas.
NOVELTY - This utility model claims a water circulation heating of the marsh gas tank, comprising a biogas tank and cooling tank, the marsh gas tank comprises a shell body, wherein the shell body is provided with a hot water circulating device, wherein the cooling tank comprises a tank body, wherein the tank body is provided with a waste heat heating cycle, the heat circulator is provided with a hot water inlet and a cold water outlet, a circulator according to waste heat heating is provided with a hot water outlet and a cold water inlet, wherein the hot water inlet is connected with hot water outlet, a cold water outlet is connected with the cold water inlet through the pipeline, said hot water recycling device and waste heat heating circulator are steel continuous bending. This utility model uses waste heat of the waste heat accelerate organic substance to promote marsh gas fast, saves coal, low cost, accelerate cooling tank cooling under the low temperature, the cold and heat exchange, and a the same can produce marsh gas.
NOVELTY - This utility model claims a kind of organic waste fermentation tank, comprising a tank body, a tank body top end is provided with a feeding port, a tank body is set at the bottom, the tank body is provided with a hot air device, the hot air device is provided with an air inlet and an air outlet, the air inlet is connected with air inlet pipe, the air inlet is connected with the waste hot air source. This utility model adopts a non-stacking area of the fermentation tank, the fermentation tank is provided with a hot air device, the heat sealing of the exhaust gas for three-dimensional stacking high pressure heating. Saves land, and has no environment pollution, no atmosphere pollution, by weight of garbage, in the tank to store heavy pressure and a hot air heating device, to promote fast fermenting domestic garbage. So as to reduce the fermentation time, shortens the fermenting period, accelerate the domestic garbage processing speed.
NOVELTY - This utility model belongs to marsh gas engineering technology field, specifically relates to a kind of glass fibre reinforced anaerobic digester. The structure of the reinforced anaerobic digester is a thick and two ends pointed olive glass steel cylinder is set with a marsh gas sludge at the lower end portion of the cylinder, and the top is provided with a marsh gas collecting port, is provided with a feeding port and the water outlet port of the part. Wherein, olivary glass steel cylinder, composed of a glass fibre fabric and resin winding produce glass, glass fibre fabric, resin and fibre yarn winding manufacturing glass steel reinforced layer and glass fibre fabric, resin to form the outer protective layer. The glass steel anaerobic digester is provided with good marsh gas mud removing function, a sealing heat uniformity and long service life.
NOVELTY - This utility model claims a kind of multifunctional constant temperature solar marsh gas tank, comprising a hot water tank, a solar heat collector, a marsh gas tank and a marsh gas tank provided with storage water tank and connected with a water pipe, wherein the marsh gas tank is on the water inlet pipe section is equipped with a circulating pump, said solar heat collector is set on the other side and connected with a section of water pipe, wherein the solar heat collector is on the water inlet pipe section is equipped with a circulating pump, the control end of the three circulation pump is respectively connected with the electric control box. This utility model beneficial effects as follows: it can ensure constant temperature marsh gas tank, marsh gas tank lifting gas generating capacity, using solar energy lift environment temperature to marsh gas tank, especially in winter, it can completely solve gas production in winter is not enough and so on. Also, using marsh gas boiler for auxiliary heating of solar energy heat storage water tank solves the cloudy and rainy days solar heat collecting station effect of system without extra process cost.
NOVELTY - The utility model claims a marsh gas generator PH value automatic adjusting device, belonging to the technical field of automatic control, comprising a PLC controller, a device for a liquid container, lye container, an electromagnetic valve I, electromagnetic valve II, a marsh gas generator, a PH value sensor, a stirrer, a motor and a contactor, the pH value sensor output end of the PLC controller, the input end of the PH value sensor extends into the marsh gas generator, liquid container through the electromagnetic valve I is connected with the PLC controller, a lye container through electromagnetic valve II are connected with the PLC controller, the lower end of the stirrer extends into the marsh gas generator, the upper end of the stirrer by the motor and a contactor connected with the PLC controller. This utility model can automatically adjust the PH value in the marsh gas generator, the biogas slurry PH value is stable, accurate control, it is convenient to use, it solves the problem that the marsh gas generator for adjusting pH, at the same time, the structure is simple and the operation is convenient.
NOVELTY - The first heat exchanger the utility model claims a CO transformation device, comprising the following steps: receiving a CO-containing raw material gas via a tube-pass inlet of the first heat exchanger is connected with the tube pass outlet and a pre-conversion reaction of raw material gas of the pre-conversion furnace, wherein at least three groups of converter downstream of the pre-conversion furnace, a converter comprises a mixer, a filter and a quenching transformation. Preferably is provided with a heat exchanger between the second converter and the third converter. Shell side inlet reaction gas outlet of the first heat exchanger and the second heat exchanger is connected with the third transducer is connected to the first heat exchanger shell pass outlet. According to this utility model is especially suitable for the device for CO conversion technique of low water-gas ratio. Change process of the steam is at least divided into three sections mixed with reaction gas, quenching cooling, entering into a shift converter for conversion reaction, so as to prevent over-temperature shift converter, which effectively prevents the methanation side reaction.
NOVELTY - This utility model claims a kind of pulse gas stripping sludge discharge device for clarification tank, a biochemical reaction pond and a sludge discharging pool, and a sludge reflux and biochemical denitrifying. The device comprises a sludge inlet pipe, a pulse air cans, a pulse part, pipe, air inlet pipe, a sludge outlet pipe and a fixing support seat, an air inlet pipe is welded on the pulse air cans on one side of pulse air lift tank is set in pulse component, a pulse component and the sludge inlet pipe, two ends are connected with the pulse gas stripping sludge discharge device is mounted on the clarification tank, a biochemical reaction pool or mud pool, controlling discharging flow rate and discharging time by controlling valve automatic sludge-discharging function, the device discharging, no blockage, simple structure, energy saving, discharge amount be adjusted at random, a mud discharging any arranged and it is easy to operate, no maintenance, effectively solves the problem that the gravity and sludge pump sludge. A long period stable operation of the system.
NOVELTY - This utility model claims a kind of removing nitrogen and phosphorus in municipal sewage processing device, which provides a kind of nitrification and de-nitrification algae biochemical reactor. Comprises the aerobic zone, an anaerobic zone and an aerobic zone end is provided with a water inlet at the bottom of the periphery of the anaerobic zone and an aerobic zone and the anaerobic zone is set at the bottom water outlet, the bottom of the aerobic zone is provided with a water distributing, and the top of the aerobic zone is provided with a distribution. And sewage into the aerobic area, algae and nitrifying bacteria treatment, then enter into the inner layer of the anaerobic zone, processing by denitrifying bacteria to the anaerobic zone, wherein a nitrogen pollution is greatly reduced. This utility model through the design of suitable fully considers, nitrifying bacteria and physiological and biochemical characteristics of denitrifying bacteria, first nitrification and denitrification, floor area of the device is small, the processing cost is low, investment and maintenance cost are low.
NOVELTY - This utility model claims a sewage treatment system of a photovoltaic slice production, wherein the system comprises a pipeline connected to a water reservoir, a dosing sedimentation tank, a multi-layer filter screen filter tank, an active carbon filter tank, a buffer tank, a neutralization reaction tank, a reverse osmosis membrane group, cleaning treatment tank and a clear water tank, a high pressure pump is set between the neutralizing reaction tank and the reverse osmosis membrane. The system uses the water filtering device is a series of enzymatic catalysis reaction, the turbidity of silicon carbide producing purified to be repeatedly recycled for purifying water. Thus it saves the water source, the discharge of the sewage can be reduced by 80% to 85%, reduces the production cost, at the same time, also reduces the environment pollution.
NOVELTY - This utility model belongs to sewage provided with device, relating to a kind of domestic sewage treatment device, wherein it is in turn set non-deposition corrosion in the horizontal tank body, scum separation net, gravel filter chamber, active adsorbing chamber and biological enzyme catalysis chamber, further set with dredging pipe corrosion in the sedimentation chamber, in the existing living septic tank is large, multiple chamber of continuous multi-way comprehensive treating domestic sewage, it has low processing cost, good purifying effect and improve living environment, treating domestic sewage reach the national comprehensive discharge standard, effectively solves the problem that domestic sewage and river polluted underground water, which avoids the underground pipeline blocking, reduces the sewage processing factory, dredging convenient service life of the device and so on;
NOVELTY - The utility model is harmless treatment of an organic fertilizer device, comprising a underground of the reaction tank is provided with a L-shaped opening at the first end of the reaction pool is provided with a reverse L-shaped sealing cover on the upper part of the L-shaped opening is connected with the reaction tank, wherein the reverse L shaped sealing cover, the upper part of the reaction tank is provided with an outlet, the inlet of the inverted L-shaped cover via a sealing reaction tank stacked is cement, the organic fertilizer raw material in the reaction tank for urine. This utility model of organic fertilizer raw material inlet of a water sealing, the sealing effect is good, the protection nutrition is not lost through reaction tank is cement piling, and avoid rain water scouring. This utility model has simple structure, convenient manufacture and low cost, protecting nutrition.
NOVELTY - This utility model claims a kind of domestic waste compost material ventilation draining device, belonging to the field of organic garbage treatment facility field. The device comprising: a cover plate and a ventilating plate, the cover plate is provided with at least four supporting legs, the cover plate is set on the ventilating plate passes through the upper part of the support leg of the bottom surface, the cover plate and the ventilation plate gas collecting port is connected with the water inlet as the air gallery; on the ventilation plate is provided with a ventilating plate is connected with the bottom of the hole. The ventilation plate of the device easy to assemble, the cleaning is convenient, the structure is simple and reasonable, it effectively guarantees the long-term stable running of the ventilation system for compost, and can improve the quality of the compost product.
NOVELTY - The utility model claims a cylinder-type organic fertilizer fermenting machine, comprising a base, a cylinder, a motor and an electric control box, wherein the two ends of the cylinder of rotating on the base, the roller is inclined horizontally, the front end of cylinder is higher than the back end of the cylinder upper part of the front end is provided with a feeding port, and the lower part is provided with a discharge port, the inner wall of the roller is extended with multiple rows of inclined forwards as blade, a motor connected with the electric control box is electrically connected with the gear is sleeved on outer wall of the roller and drives the roller to rotate under the control of the electric control box, organic material enters from the feeding port, turning under the pushing of the blade from the front end to the rear end of the roller move to the discharging port. This utility model realize continuous organic fertilizer fermentation, high efficiency and energy-saving, strong practicability, and can present bacteria agent is matched with the energy, strong adaptability, multiple functions; This utility model can be suitable for more than one raw material, and a water content of the mixture of the raw material, can be suitable for a plurality of climate environment.
NOVELTY - This utility model claims a biomass fuel gas, comprising a bottom plate (1), the lower layer sieve plate (2), a cylinder body (3), an upper sieve plate (4), an air inlet pipe (5), a cover plate (8), an air outlet pipe (11), a hand hole pipe (14), wherein the cylinder (3) is circular cylinder, the upper part is provided with cylinder flange (7) through the bolt (10) is connected with the cover plate (8), the lower is set with a bottom plate (1), the inner part is provided with the lower layer sieve plate (2), an upper sieve plate (4) two layers of filtering mesh, a cylinder body (3) is filled with water, the cylinder body (3) one side of the upper part is provided with an air inlet pipe (5), and the other one side set with air outlet pipe (11), overflow water pipe joint (13), a hand hole pipe (14), pipe joint (18). This utility model has advantages as follows: the biomass fuel gas fire arrestor has simple structure, reasonable design, and obvious purifying effect, high safety, good effect and low cost.
NOVELTY - Mobile anaerobic tank, which effectively utilizes the straw of the village, prevent the environment pollution, it not only realizes straw, but also has the effect of waste. Relieving energy, convenient people production and living. The device is composed of a carbon steel fermenting anaerobic reactor and red mud plastic hood, anaerobic reactor upper side is equipped with biogas slurry spraying pipe and a spray head, the lower part is set with biogas liquid pump, the bottom of the reactor is equipped with a drain valve, the top part of a flange, a bolt and a solid film of red mud plastic hood.
NOVELTY - Controlling turfgrass nematode comprises evenly mixing deep fertile soil and then dividing into two parts, carrying out dry heat sterilization of the soil, additionally taking inactivated waste compost and waste rubber particle, and taking raw material comprising inoculated soil, sterilized soil, waste compost, and waste rubber particle and then uniformly mixing, sowing turfgrass grass seed, and maintaining lawn grass seed to grow turf grass during water substrate and then culturing, and spraying diluted fertilizer during lawn growing period and later periodically.    USE - The method is useful for controlling turfgrass nematode (claimed).    ADVANTAGE - The method controls turfgrass nematode with reduced soil compactness, and is convenience for movement of water in the soil, can modify water retaining property of the soil.    DETAILED DESCRIPTION - Controlling turfgrass nematode comprises (1) evenly mixing deep fertile soil (5-15 cm) and then dividing into two parts, where one part is used as inoculating a soil, and the other part is disinfection soil, carrying out dry heat sterilization of the soil at 160 degrees C for 2 hours, additionally taking inactivated waste compost and waste rubber particle having a size of 0.5-1 mm, and taking the raw material comprising 90-160 pts. wt. of inoculated soil, 140-260 pts. wt. of sterilized soil, 90-460 pts. wt. of waste compost, and 10-20 pts. wt of waste rubber particle and then uniformly mixing, (2) uniformly sowing turfgrass grass seed in cultivation matrix at normal temperature, where the sowing density is 20-35 g/m2, and (3) maintaining lawn grass seed to grow turf grass during water substrate and then culturing at room temperature for 90 days, and spraying diluted fertilizer during lawn growing period and later periodically.
NOVELTY - Method for decomposing sawdust, involves completely soaking fresh sawdust in water, scattering urea during stack turning, stacking the mixed sawdust, punching holes on the stack surface after stacking, turning the stack after the central temperature of the stack rises to 50 degrees C, restacking after stack turning, again turning the stack when the central temperature of the stack rises to 50 degrees C, adding white-rot fungal agent during stack turning, stacking the mixture, turning the stack, stacking once after 15 days and ending decomposition after 15 days.    USE - The method is useful for decomposing sawdust used for cultivating fungal strains.    ADVANTAGE - The method is simple, convenient to operate, and cost-effective, utilizes only a small amount of urea and white-rot fungal agent, thus facilitates decomposition of sawdust with microorganisms, reduces sawdust decomposing time to only 40 days and land occupation of sawdust decomposition, can be applied to large-scale and continuous production factory-like edible fungus enterprises, and enables to improve yield and quality of strains.    DETAILED DESCRIPTION - Method for decomposing sawdust, involves (a) completely soaking fresh sawdust in water, scattering urea during stack turning and uniformly mixing the components, (b) stacking the mixed sawdust and punching holes on the stack surface after stacking, (c) turning the stack after the central temperature of the stack rises to 50 degrees C and restacking after stack turning, (d) again turning the stack when the central temperature of the stack rises to 50 degrees C, adding white-rot fungal agent during stack turning, uniformly mixing the components and stacking the mixture, and (e) turning the stack, stacking once after 15 days and ending decomposition after 15 days.
NOVELTY - In killing of apple snail, an external invasive plant Ageratum conyzoides (ageratum silybum marianum) powder, is used.    USE - In killing of apple snail (claimed).    ADVANTAGE - The method utilizes common external invasive plant material, Ageratum conyzoides (ageratum silybum marianum) of south area, which is easy to obtain; can be effectively kill apple snail at a certain injection molding; is good for controlling animal intrusion apple snail; provides a new way for resource utilization of harmful invasive plant; and provides great reference value for researching the ecological intrusion and intrusion control technology. The processing method has simple operation; does not need the complex program; is convenient for farmers in the field operation; saves the cost; and reduces the pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Ageratum conyzoides (ageratum silybum marianum) powder, involving: cutting and drying Ageratum conyzoides (ageratum silybum marianum) plant, grinding, filtering by 4-60-mesh sieve.
NOVELTY - This utility model claims a kind of intelligent integrated urban garbage processing system, comprising a pre-processing system and a comprehensive processing system, a pre-processing system comprises a garbage bag breaking machine and the fermentation storehouse, a comprehensive processing system comprises feeding machine, sorting machine, magnetic separator, a winnowing machine, a crusher, a roller screen, chain screen conveyer belt, a belt conveyor, a bracket and so on, evenly feeding machine by a belt conveyor and the sorting machine is connected with the lower machine set with chain screen conveyer belt, a conveyor belt chain on one side of the screen cover is set outside the machine. This device daily treatment capacity, high separation efficiency, recycling multiple kinds, it is suitable for all kinds of mixed waste, effectively control the environment pollution, protecting ecological environment, rational equipment configuration, advanced and simple production process, the technology is mature, it has obvious social benefit, a terminal product cost, and high utilization rate, large market space.
NOVELTY - This utility model claims a waste heat recycling dryer, comprising a shell body, a shell driven by the gear box, the inner shell is provided with inclined blade causing material, above the right end is provided with a lower hopper, right middle part of the lower end is provided with a high temperature air inlet, the left upper part of the front end is provided with an air outlet, the waste heat waste heat through air inlet pipe and a hot air distribution device connected with the left end lower part is provided with a downwards inclined discharging pipe. This utility model of the dryer as waste heat through air inlet pipe and a hot air distribution device connected with the air distribution device can be set in the fermentation tank, the weight of garbage, in the tank to store high pressure emitting device and a hot air heating method, fast fermenting domestic garbage. So as to reduce the fermentation time, shortens the fermenting period, accelerate the domestic garbage processing speed. Dryer so as to waste heat can be recycled, which not only saves energy, but also reduces the environment pollution.
NOVELTY - A kind of turner, comprising a machine frame, the upper frame is provided with an operation chamber, a machine frame left and right two sides of the lower part and the upper part is provided with a straight line walking device, a linear walking device is provided with a turning device, turning device is provided with a blowing device, left and right sides of the machine frame is provided with a sleeve for lifting and turning device of lifting device, the upper part machine frame is further equipped with a driving device, driving the blowing device blowing of dry turning material, line cam rapid cutting knife driven walking device moving and a driving lifting device is a lifting action of the power system. This utility model not only avoids increasing load of device and improves the work efficiency of the machine, and it does not need of turning the material drying.
NOVELTY - An iron-pyrite acid recycling purification device uses a circulation tank and a compound fertilizer tail gas absorption process. The hollow column is connected to a dilute acid filter. The filter is connected with a dilute acid storage tank. The dilute acid storage tank is connected with the compound fertilizer tail gas absorption process circulation tank.    USE - Iron-pyrite acid recycling purification device (claimed).    ADVANTAGE - The iron-pyrite acid recycling purification device enables recycling of tail gas at 150 ton/year and reduces the amount of carbide slag. The device is environmentally-friendly and economical.
NOVELTY - Controlling energy-saving serial system light source for improving grade of methane, comprises inoculating greater than 100 mg l-1 of micro-algae in a first level reactor by super-strong photosynthetic carbon oxidation reaction, fermenting methane using fermentation waste biogas slurry as a nutrient-rich substrate, passing light source into the reactor to grow the micro-algae, inoculating the grown micro-algae by controlling the light source, and passing methane into a next stage of serial reactor to gradually absorb carbon in the methane.    USE - The energy-saving serial system light source is useful for improving grade of methane (claimed).    ADVANTAGE - The method reduces energy consumption and improving the economic benefit of the system, and ensures that the system is simple and feasible, and convenient to operate.    DETAILED DESCRIPTION - Controlling energy-saving serial system light source for improving grade of methane, comprises inoculating greater than 100 mg l-1 of micro-algae in a first level reactor by super-strong photosynthetic carbon oxidation reaction, fermenting methane using fermentation waste biogas slurry as a nutrient-rich substrate, passing light source into the reactor to grow the micro-algae, inoculating the grown micro-algae by controlling the light source, and passing methane into a next stage of serial reactor to gradually absorb carbon in the methane, where the system comprises reactors whose top parts are provided with air outlets, which are connected in series via a pipeline, a multi-stage reactor, and the pipeline is provided with an air valve, which is provided with an LED lamp and a reverse guide device.
NOVELTY - Energy-saving power liquid spraying device comprises rotating wheel, global positioning system (GPS) device, fan, water, liquid inlet, and liquid inlet pressure.    USE - Energy-saving power liquid spraying device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for energy-saving liquid which comprises propanol, ethanol, ring removing agent, sulfanilic acid and hydrogen peroxide.
NOVELTY - The boiler has boiler portion (1), hearth (2), furnace liner, fan (3), furnace chamber (5), furnace door (6), feeding door (4), injection pipe (7), fire arrestor (8), low temperature plasma generator (9), high frequency high voltage power supply (10), steam switch (11) and steam pipe (12). High voltage power supply is connected with low temperature plasma generator connected with flame arrester. Fire arrestor is connected with injection pipe which is connected with hearth. End of steam pipe is connected with top end of furnace, while other end is connected with steam switch.    USE - Efficient and energy-saving boiler for plasma water decomposition hydrogen production.    ADVANTAGE - The fuel consumption can be reduced by 30% and the emission reduction targets by 40% can be achieved. The efficient and energy-saving boiler can be obtained. The market value of boiler can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the efficient and energy-saving boiler.    Boiler portion (1)    Hearth (2)    Fan (3)    Feeding door (4)    Furnace chamber (5)    Furnace door (6)    Injection pipe (7)    Fire arrestor (8)    Low temperature plasma generator (9)    High frequency high voltage power supply (10)    Steam switch (11)    Steam pipe (12)
NOVELTY - An anaerobic ammonium oxidation biofilm reactor comprises reaction tank (7). The reaction tank is provided with at least one filter assembly (6). The filter assembly is provided with non-woven fabric support cavity structure covered on outer surface. The top of each filter assembly are connected to water outlet pump (4) through water outlet pipe (9). The lower end of reaction tank is provided with water inlet pump (2). connected to water inlet valve (3) of reaction tank.    USE - New anaerobic ammonium oxidation biofilm reactor.    ADVANTAGE - The reactor enhances mass transfer and has simple structure and high removal efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for denitrification by feeding anaerobic ammonia oxidizing bacteria inoculation sludge through air inlet channel to water inlet of sewage; treating sewage; entering sewage to reaction tank, starting water pump when liquid level is higher than the top of filter assembly; filtering through filter assembly; and continuously drawn out processed water through water outlet pipe.
NOVELTY - A biological dialysis system comprises purification tank divided into water conveyance units connected with water drainage system with holes and is located along the longitudinal direction of the tank's top surface, and further connected to the water supply unit.    USE - Biological dialysis system used for cleaning sewage or sludge.    ADVANTAGE - The system can restore aquatic ecology, enhance basic and important water self-purification capacity and dirt holding capacity, saves energy, reduces emission, has low-carbon, and is a sustainable and environmental-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cleaning wastewater by filling tank with to-be-treated wastewater, inserting injection pipe of the conveyance unit into the bottom of the tank, implanting on the surface of the sludge, opening water supply unit, flowing water into the injection pipe, and discharging through the holes of the water drainage system purifying the sludge circulating from the bottom.
NOVELTY - Treating cryogenic high-efficiency ammonia nitrogen sewage comprises internally embedding nitrifying bacteria using high molecular material as carrier to form embedding vector; adding to the reaction vessel, introducing wastewater containing ammonia nitrogen, and activating embedding vector; and inoculating sludge when activation is successful, and introducing sewage to be treated on aeration biochemical treatment.    USE - Treating cryogenic high-efficiency ammonia nitrogen sewage (claimed).    ADVANTAGE - The nitrifying bacteria embedding carrier has wear resistance, good physical and mechanical performances, is chemically stable, biodegradable, contains large amount of good for nitrobacteria growth, can be diffused and keeps the active ingredients and mass transfer of substances. The method has high ammonia nitrogen treatment efficiency and short technique flow. The device is simple and the existing treatment process combined with the special carrier achieves good removal of low-temperature nitrogen.
NOVELTY - Removing antimony in sewage comprises introducing wastewater containing antimony to flocculation sedimentation tank, adding polymerized aluminum ferric chloride and sodium metasilicate coagulant aid for suspended particulates, removing suspended particles and flowing wastewater to adsorption tower containing biomass filter, and adsorbing to remove antimony.    USE - Removing method of antimony in sewage (claimed).    ADVANTAGE - The method is carried out at normal temperature without noise, uses non-toxic chemical agent which is harmless and not volatile, does not produce new waste and emulsion can be used circularly, uses raw materials that are easy to obtain and low in cost, has recycled heavy metal, and has high efficiency of removing antimony which is more than 99.9%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass filter by adding industrial wine waste slag which 0.3-0.5 times the quality of rice straw, adding and 0.5-1 g/kg sodium carbonate and 0.2-0.5 g/kg organic acid; uniformly stirring and mixing, controlling dissolved oxygen at 0.1-0.2 mg/L, pH at 6.5-7.5, temperature at 50-55 degrees C and electric potential at -110 to -200 mV, and fully fermentation and aging for 6-7 days; high-temperature sterilizing, pulverizing, crushing, and sieved to obtain 120-150 mesh size biomass adsorbent.
NOVELTY - Removal of phosphorus and nitrogen from high-phosphorus and high ammonia-nitrogen sewage involves entering pig-raising sewage into sewage collecting tank, fermenting to obtain biogas, entering into quenching and tempering tank, adjusting pH, precipitating magnesium ions, ammonia-nitrogen ions and phosphate ions, entering supernatant in artificial biofilm primary floating suspension device, adding phosphorus-accumulating bacteria and denitrifying bacteria to remove phosphorus and nitrogen and planting aquatic plant to absorb residual phosphorus and nitrogen.    USE - Removal of phosphorus and nitrogen from high-phosphorus and high ammonia-nitrogen sewage (claimed).    ADVANTAGE - The energy-saving, low-operation cost and simple-to-operate method utilizes three stages of artificial biofilm floating suspension device which creates anaerobic-aerobic or anoxic environment. The treated sewage reaches the required standards.    DETAILED DESCRIPTION - Removal of phosphorus and nitrogen from high-phosphorus and high ammonia-nitrogen sewage comprises entering pig-raising sewage into sewage collecting tank, fermenting to obtain biogas, entering into quenching and tempering tank provided with plate-shaped microporous aerator, adjusting pH to 7.5-9, precipitating magnesium ions, ammonia-nitrogen ions and phosphate ions to obtain ammonium magnesium phosphate for fertilizer, entering supernatant in artificial biofilm primary tank provided with microporous aerator, adding phosphorus-accumulating bacteria and denitrifying bacteria to remove phosphorus and nitrogen, entering into artificial biofilm secondary floating suspension device, adding phosphorus-accumulating bacteria, entering into artificial biofilm tertiary floating suspension device, adding phosphorus-accumulating bacteria and planting aquatic plant to absorb residual phosphorus and nitrogen.
NOVELTY - Production of composite biological enzyme comprises strain collecting and extracting process, culturing, fermenting strain, and separating and extracting of bio-enzyme. The collecting and extracting process involves taking bacteria from domestic sludge, culturing using corresponding culture medium to obtain biological enzyme needed strain; and adding bottom yeast for mixed fermentation. The separating and extracting of bio-enzyme involves physical separation and extraction or chemical separation and extraction.    USE - Production of composite biological enzyme used for reducing domestic sludge.    ADVANTAGE - The composite biological enzyme produces sewage sludge with clear smell, inhibits hydrogen sulfide during nitration process, and effectively reduces organic matter. It converts soluble organic substance into carbon dioxide, nitrogen, oxygen, water and sulfate. It reduces total suspended solids, chemical oxygen demand, and biological oxygen demand, thus reducing sludge production. It is non-toxic, non-corrosive, and does not produce secondary pollution.    DETAILED DESCRIPTION - Production of composite biological enzyme comprises strain collecting and extracting process, culturing, fermenting strain, and separating and extracting of bio-enzyme. The collecting and extracting process involves taking bacteria from domestic sludge, culturing using corresponding culture medium to obtain biological enzyme needed strain; and adding bottom yeast for mixed fermentation. The separating and extracting of bio-enzyme involves physical separation and extraction or chemical separation and extraction, in which physical separation and extraction involves centrifuging fermented product; and separating liquid to obtain bio-enzyme solution. The separating and extracting process involves adding ammonium sulfate for salting out; filtering; and drying to obtain solid fixed substance.
NOVELTY - Agent comprises ferrous gluconate.    USE - The agent is useful as normal fertilizer for controlling spider mite and iron deficiency.    ADVANTAGE - The agent is stable, can be prepared easily, and is convenient to use and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing ferrous gluconate, which involves preparing gluconic acid or gluconolactone solution, adding iron after the reaction, filtering, crystallizing and drying the obtained crystal.
NOVELTY - The excrement treatment device has a tank case (5) that is equipped with a vertical stirring shaft (6). The stirring shaft is provided with a radial direction of the stirring blade (2). The power machine (1) is connected with the stirring shaft. The upper portion of the tank case is equipped with a blower (4). The lower portion of the tank case is equipped with a feeding port (7).    USE - Device for treating excrement of human and animal.    ADVANTAGE - The usability of the excrement treatment device can be improved. The environment pollution can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the excrement treatment device.    Power machine (1)    Stirring blade (2)    Blower (4)    Tank case (5)    Stirring shaft (6)    Feeding port (7)
NOVELTY - Method for processing banana and taro residues for preparing bioorganic fertilizer, involves culturing Bacillus megaterium in nutrient broth, collecting thalli to prepare a material as organic fertilizer, crushing banana and taro residues, adding the cultured B.megaterium and performing aerobic fermentation to obtain fertilizer.    USE - The method is useful for processing banana and taro residues for preparing bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer can be prepared simply, and is cost-effective.
NOVELTY - Method of degrading waste paper for recycling, involves crushing the waste paper, adding yeast culture (5 times) to the waste paper at room temperature, carrying out degradation process at 25-36 degrees C for 6-10 hours, then adding water (10 times) to the mixture, filtering the mixture, obtaining the solution for recycling, removing residues, drying, sterilizing and degrading to obtain the fertilizer.    USE - The method is useful for degrading waste paper for recycling.    ADVANTAGE - The recycled paper is convenient to use, environmentally-friendly and cost-effective.
NOVELTY - Method for producing and processing humic acid based organic fertilizer, is claimed.    USE - The method is useful for producing and processing humic acid organic fertilizer (claimed).    ADVANTAGE - The method shortens ammonification time period of the fertilizer, provides high yield of the fertilizer, reduces production cost, occupies less additional site for production process, does not allow sewage to flow out to pollute surrounding water resources, and also airing or baking step is not required, completes production of the fertilizer within 7 days, and does not cause air pollution due to ammonia, thus the method contributes to development of an ecological and environment-friendly city.
NOVELTY - Method for preparing bio-organic fertilizer from marigold straws, involves crushing the marigold using crusher into particle size of less than 20 mm, mixing marigold straw, organic matter, microbial inoculum and water according to weight ratio of 10-60%, 20-40%, 0.05-0.5%, 19-50%, stacking and fermenting mixture at 50 degrees C, controlling the fermentation temperature to 40-60 degrees C for 5-15 days, crushing the mixture using crusher into granularity of 30-50 meshes, checking particles according to performance index, and packing product.    USE - The method is useful for preparing bio-organic fertilizer from marigold straws (claimed), which is used for controlling root-knot nematodes, gray molds, and molds.    ADVANTAGE - The prepared bio-organic fertilizer is suitable for industrial production.    DETAILED DESCRIPTION - Method for preparing bio-organic fertilizer from marigold straws, involves crushing the marigold using crusher into particle size of less than 20 mm, mixing marigold straw, organic matter, microbial inoculum and water according to weight ratio of 10-60%, 20-40%, 0.05-0.5%, 19-50%, stacking and fermenting mixture at 50 degrees C, controlling the fermentation temperature to 40-60 degrees C for 5-15 days, crushing the mixture using crusher into granularity of 30-50 meshes, checking particles according to performance index, and packing product, where the bio-organic fertilizer is packed in a woven bag or lining plastic film bag.
NOVELTY - The turner has machine frame (1) which is connected with arm (3). The arm is connected with roller device (2). The roller device is provided with left cylinder and right cylinder. The power output end is connected with left roller and the right cylinder is connected with left hydraulic motor. The plane blade of left cylinder and right cylinder is provided with the main portion.    USE - Roller type hydraulic turner for garbage treatment.    ADVANTAGE - The hydraulic motors directly transfer the power to drums, so that power transmission efficiency and working reliability can be improved. The noise generated from hydraulic turner can be reduced. The energy consumption of the turner can be reduced and the production efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the roller type hydraulic turner.    Machine frame (1)    Roller device (2)    Arm (3)    Hydraulic device (4)
NOVELTY - The biomass tower type compost processing device has a reaction tower (1) that is provided with a feeding port (9). The reaction tower is positioned lower than the feeding port provided with a filter screen (10). The reaction tower is provided with an air inlet (11) and a water outlet pipe (16). The air inlet is connected with a fan (13). The air outlet is provided with an air heater (12). The water outlet pipe is connected with a filtrate regulation tank (15) connected with a water inlet pipe (6) provided with a water pump (14).    USE - Biomass tower type compost processing device.    ADVANTAGE - The compost efficiency can be increased. The propagation of pathogenic bacteria and peculiar smell can be prevented effectively. The pollution-free organic farming can be performed effectively. The disease resistance and insect resistance of the compost processing device can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the biomass tower type compost processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass tower type compost processing device.    Reaction tower (1)    Water inlet pipe (6)    Feeding port (9)    Filter screen (10)    Air inlet (11)    Air heater (12)    Fan (13)    Water pump (14)    Filtrate regulation tank (15)    Water outlet pipe (16)
NOVELTY - In the preparation of fertilizer synergistic agent, a Bacillus subtilis bacteria phospholipid peptide, yeast liquid is used.    USE - In the preparation of fertilizer synergistic agent or fertilizer (claimed).    ADVANTAGE - The Bacillus subtilis bacteria phospholipid peptide, fermentation liquid acts as fertilizer synergistic agent or fertilizer, can improve the growth, yield and cutting rate of rice.    DETAILED DESCRIPTION - In the preparation of a fertilizer synergistic agent, a Bacillus subtilis bacteria phospholipid peptide, yeast liquid is used. The Bacillus subtilis bacteria phospholipid peptide, yeast liquid is prepared by: 1) selecting Bacillus subtilis E8 under preservation number (CGMCC No. 1107) and inoculating in an inclined plane culture medium at 31-35 degrees C for 48-72 hours; preserving at 4 degrees C for 2-15 days, where the inclined plane culture medium is as follows: 2-8 g/l beef extract, 5-15 g/l peptone, 2-8 g/l sodium chloride, and 10-25 g/l agar; 2) taking inclined plane preservation strain inoculated in a culture medium bottle, culturing at 3-35 degrees C for 2-28 hours, where the bottle culture medium is as follows: 15-25 g/l glucose, 2-10 g/l L-glutamic acid, 0.5-2 g/l potassium dihydrogen phosphate and 0.5-3 g/l yeast extract; and 3) taking one bottle culture, which is inoculated in ferment culture medium at 3-37 degrees C for 15-350 revolutions per minute (rpm), culturing for 24-72 hours; controlling pH value of the ferment liquid to more than 6.8 by using 3 mol/l of sodium hydroxide solution, where the fermentation culture medium is as follows: 3-50 g/l glucose or maltose, 3-50 g/l soluble starch or dextrin, 15-25 g/l L-glutamic acid, 0.5-2 g/l potassium dihydrogen phosphate, and 0.5-3 g/l yeast extract. An INDEPENDENT CLAIM is included for a fertilizer synergistic agent or a fertilizer comprising Bacillus subtilis bacteria phospholipid peptide, fermentation liquid.
NOVELTY - Plant nutriment comprises main material, auxiliary material, water, and biological fermenting agent, where the main material is at least one of crop straw, fruit residue, mushroom residue, distilled grain and furfural residue, the auxiliary material is manure or soil, the concentration of biological fermenting agent is 0.2% and water is 50%, and the volume ratio of main material, auxiliary material and fermenting agent is 3:5:1.    USE - The plant nutriment is useful for improving activity and stress resistance of plant, promoting plant to absorb the nutrients, and prolonging the florescence period.    ADVANTAGE - The plant nutriment is cost-effective and environmentally-friendly, can be prepared simply, and causes no toxic side effects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the plant nutriment, which involves cutting and crushing the main material, mixing and conveying the mixture to the fermentation tank of 15-45 degrees C, adding 15-20% of the auxiliary material and biological fermenting agent of 2%, mixing and stirring uniformly, adding water, stirring, controlling the temperature at 15-45 degrees C, fermenting the mixture for 288 hours in the fermentation tank at 45-55 degrees C, after fermentation detecting the fermented material for the presence of organic matter content, pH, and nitrogen, phosphorus and potassium content.
NOVELTY - Culture medium comprises 20-30 pts. wt. humus soil, 30-40 pts. wt. sandy loam, 60-70 pts. wt. decomposed human excreta and pig manure, 60-70 pts. wt. decomposed cotton seed hulls, and 30-40 pts. wt. pond sludge, where the above-mentioned components are mixed with to-be-treated soil, further diluted formalin is sprayed on the to-be-treated soil, and treated soil is used as the culture medium.    USE - As culture medium for Dahlia pinnata (claimed). The culture medium is useful for controlling insect pest diseases in the D.pinnata.    ADVANTAGE - The culture medium is reasonable in preparation, suitable for culture conditions of the D.pinnata, effectively enhances survival rate, ensures good growth and up-growth of the D.pinnata, provides good foundation for successful culture of D.pinnata, and saves culturing cost of the D.pinnata, as required raw materials used in the culture medium are easily available and cheap.
NOVELTY - Production of cinnamyl chloride involves pumping thionyl chloride into a reaction kettle, starting freezing salt water, adding cinnamyl alcohol, controlling at 15 degrees C while the exhaust gas absorption device is open, closing the freezing salt water inlet and outlet valve, continuously stirring and reacting, adding saturated aqueous solution of sodium carbonate or sodium bicarbonate to neutralize, standing and layering, separating out lower layer product, neutralizing, washing, decompressing, and collecting 1600 Pa at 105-110 degrees C fraction to obtain light yellow oily liquid.    USE - Method for the production of cinnamyl chloride (claimed) used a common medical intermediate for synthesizing cinnarizine, hydrochloric acid, and calcium antagonist drug; and used as a spice.    ADVANTAGE - The method is simple and feasible, is inexpensive, improves yield, and is environment friendly.
NOVELTY - Preparing magnolol comprises dissolving Magnolia bark total phenol in organic acid or alkali solution, and carrying out esterification of acid and alkali, completely separating the crystal out, centrifuging the crystal and collecting centrifugal liquid, adding acid solution to the centrifugal liquid, adjusting the pH value to acidity, centrifuging and collecting the precipitate, adding organic solvent into the precipitate, heating, concentrating, and recrystallizing after cooling to obtain the high purity magnolol.    USE - Method for preparing magnolol (claimed).    ADVANTAGE - The method is simple, environment-friendly and safe, and can provide product having high purity and high yield.
NOVELTY - Preparing potassium citrate, comprises adding water to citric acid ammonium salt to obtain citric acid ammonium salt solution, taking salt solution into ion exchange resin column and adding water to elute potassium ion solution, collecting the eluent, decompressing and concentrating the eluent to obtain potassium citric acid concentrated liquid, and adding active carbon and water to dilute the filtrate, and concentrating, cooling, crystallizing and drying the filtrate.    USE - The process is useful for producing potassium citric acid, which is used for medical use (all claimed).    ADVANTAGE - The process has gentle reaction conditions, convenient operation, is environment friendly, and produces less toxic potassium citrate.    DETAILED DESCRIPTION - Preparing potassium citrate, comprises adding water to citric acid ammonium salt at a certain temperature to obtain citric acid ammonium salt solution, taking the salt solution into an ion exchange resin column or macro-porous adsorption resin column and adding water to elute other impurities containing potassium ion solution, collecting the eluent, decompressing and concentrating the filtrate to a certain volume to obtain potassium citric acid concentrated liquid, adding active carbon and pure water to dilute the concentrated solution and then performing absorbing, discoloring, rough filtration, fine filtration and ultra-filtration and collecting, concentrating, and cooling the filtrate at room temperature, crystallizing and drying.
NOVELTY - Preparation of 1-bromoethylacetate comprises at controlled temperature, adding acetylbromide to alumina powder, slowly dropping paraldehyde, heating, continuously stirring, preserving temperature, obtaining the reaction mixed solution, filtering to remove the solid, controlling the temperature, slowly adding the filtrate with methylene dichloride, uniformly mixing, adding purified water, extracting, taking the organic phase, controlling the temperature, decompressing and distilling, and removing the fraction to obtain the product.    USE - Preparation of 1-bromoethylacetate (claimed).    ADVANTAGE - The method provides high purity 1-bromoethylacetate. It uses paraldehyde to replace acetaldehyde of the prior art and uses alumina for catalysis, thus, environment-friendly, ensures high product yield and high purity, has mild and easy to control process condition, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of 1-bromoethylacetate comprises at controlled temperature T1 of 12 degrees C, adding acetylbromide to alumina powder, slowly dropping paraldehyde, heating at T2 i.e. 12-20 degrees C, continuously stirring, preserving temperature for t i.e. 0.5-5 hours, obtaining the reaction mixed solution, filtering to remove the solid, controlling the temperature at T3 i.e. 20 degrees C, slowly adding the filtrate with methylene dichloride, uniformly mixing, adding purified water at T4 i.e. 20 degrees C, extracting, taking the organic phase, controlling the temperature at less than 25 degrees C, decompressing and distilling, and removing the fraction to obtain the product. The volume ratio of acetylbromide and paraldehyde is 5:0.2-0.4. The weight of alumina is 1.0-1.5 wt.% of the volume of acetylbromide.
NOVELTY - A losartan biphenyl is prepared by providing o-dichlorobenzene and chlorotoluene nitrile as raw materials, and imidazole-1-butyl-3-methylimidazolium alkaline ionic liquid/water system, loading nickel chloride in alkaline ionic liquid as catalyst, carrying out coupling reaction, and filtering to obtain product.    USE - Method for preparation of losartan biphenyl (claimed).    ADVANTAGE - The method avoids damage to environment, has low production cost, recycles catalyst, and avoids decomposition of catalyst loss. It is also convenient for large-scale production.
NOVELTY - A medical use sulfaguanidine is produced by providing sodium, sodium carbonate and guanidine nitrate, and adding catalyst and co-catalyst; raising temperature to 120 degrees C, and pumping ammonia and carbon dioxide; raising temperature to 125-145 degrees C, melting, sealing reaction system, keeping temperature and reacting for 1-3 hours; adding raw material to purified water, stirring, cooling, adding sodium hydroxide aqueous solution, cooling, filtering, and washing; adding active carbon into solution, boiling, adsorbing, decoloring, and filtering.    USE - Method for production of medicinal sulfaguanidine (claimed).    ADVANTAGE - The method is simple, shortens reaction time, has high product yield, and has no pollution to environment.    DETAILED DESCRIPTION - Medical use sulfaguanidine is produced by providing sodium, sodium carbonate and guanidine nitrate at mole ratio of 1.2-1.5:1.0:1.5-1.8, adding catalyst and co-catalyst; raising temperature to 120 degrees C, opening vacuum, and pumping ammonia and carbon dioxide; continuously raising temperature to 125-145 degrees C, melting, sealing reaction system, keeping temperature and reacting for 1-3 hours; adding raw material and to purified water, stirring, naturally cooling to 50 degrees C, adding sodium hydroxide aqueous solution, cooling to 20-30 degrees C, filtering, and washing to pH value of 7-7.5; adding active carbon into solution, boiling, adsorbing, decoloring, filtering by 0.45 mu m filter film, fine filtering by 0.22 mu m filter film, performing hollow fiber ultra-filtration, and collecting filtrate; and cooling filtrate to room temperature, centrifuging, and fluidized-bed drying.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram illustrating a production method of medical use sulfaguanidine. (Drawing includes non-English language text).
NOVELTY - N-vinyl pyrrolidone rectification polymerization inhibition comprises adding polymerization inhibitor to small amount of N-vinyl pyrrolidone (NVP), stirring and dissolving crude product; continuously dropping or one-time quantitative adding water to NVP, mixing, added polymerization inhibitor is 50-1000 ppm; pumping mixed material into rectifying tower, normal vacuum rectifying, collecting refined and rectified NVP, where rectifying kettle temperature is 90-160 degrees C, and tower top pressure is 5000 Pa.    USE - Method for inhibiting polymerization of N-vinyl pyrrolidone rectification (claimed).    ADVANTAGE - The method improves product yield, reduces waste slag, improves production efficiency, reduces production cost, and reduces environment pollution.
NOVELTY - Preparation of 6-chloro-3-methyluracil comprises reacting 1-methylbarbituric acid and chlorinating agent in water-immiscible organic solvent, where chlorinating agent is phosphorus oxychloride, and refluxing to obtain a reaction mixture; and adding water to the reaction mixture, and quenching.    USE - Method for preparation of 6-chloro-3-methyluracil (claimed).    ADVANTAGE - The method can reduce the use amount of the phosphorus oxychloride, does not need decompressing and distilling phosphorus oxychloride, mild reaction conditions, and easy to operate.
NOVELTY - A thiazole derivative (II) is prepared by diazotizing thiazole ester derivative (I) with alkyl nitrite (R3NO2) as diazotizing agent in an anhydrous polar solvent at 30-80 degrees C to remove the nitride to obtain compound (II). The anhydrous polar solvent is anhydrous N,N-dimethylformamide, anhydrous N,N-dimethylacetamide, anhydrous acetonitrile , anhydrous tetrahydrofuran, anhydrous dioxane and anhydrous 1,1,3,3-tetramethyl urea.    USE - Method for preparation of thiazole derivative (claimed).    ADVANTAGE - The method has mild reaction, simple operation, less by-product, used smaller molar volume, simple post-treatment, is suitable for industrial production, environment-friendly, and can obtain higher yield and purity.    DETAILED DESCRIPTION - A thiazole derivative of formula (II) is prepared by diazotizing thiazole ester derivative of formula (I) with alkyl nitrite (R3NO2) as diazotizing agent in an anhydrous polar solvent at 30-80 degrees C to remove the nitride to obtain compound (II). The anhydrous polar solvent is anhydrous N,N-dimethylformamide, anhydrous N,N-dimethylacetamide, anhydrous acetonitrile , anhydrous tetrahydrofuran, anhydrous dioxane and anhydrous 1,1,3,3-tetramethyl urea.    R1=H or 1-3C alkyl;    R2=Me, Et, n-Pr, or iPr; and    R3=2-8C alkyl.    An INDEPENDENT CLAIM is included for preparation of thiazole ketone derivative of formula (IV) by converting the ester group of compound (II) into an aldehyde group to obtain compound (IV).
NOVELTY - Semisynthetic preparation of sumac leaf saponin is carried out by adding naringin, ethanol aqueous solution, iodine and weak alkaline salt, then heating and stirring to react, and hot filtering or centrifuging the reaction product to obtain precipitate.    USE - Method for semisynthetic preparation of sumac leaf saponin (claimed).    ADVANTAGE - The method utilizes raw materials that are easy to obtain and have low cost, involves simple operation, and is environment-friendly.
NOVELTY - The gasifier (2) has a gasifying agent supply unit (20) for supplying a gasifying agent i.e. water vapor. A turntable (13) opens an inner cylinder lower end part and gap under an inner cylinder (12). A thermal storage property protrusion (14) is provided in a rotation-center part of the turntable, where a space (22) of the inner cylinder and the protrusion is provided as a gasification area of carbonized material. Combustion gas emitted in a carbonization furnace is introduced into a space i.e. combustion gas area (23), of an outer cylinder (11) and the inner cylinder.    USE - Thermal decomposition gasifier for manufacturing pyrolysis gas by changing biomass e.g. organic waste such as scrap wood, chemically according to thermal decomposition and gasification.    ADVANTAGE - The gasifier rotates with the turntable such that the gasification area tends to carry out heat conduction of the space of the inner cylinder, so that pyrolysis gas with uniform composition ratio is efficiently generated by carrying out high temperature heating of the carbonized material, thus providing uniform temperature distribution in a rapid and efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a top cross-sectional view of an inside-and-outside cylinder part of a thermal decomposition gasifier and a side partial cross-section view of a thermal decomposition gasifier.'(Drawing includes non-English language text)'    Thermal decomposition gasifier (2)    Outer cylinder (11)    Inner cylinder (12)    Turntable (13)    Thermal storage property protrusion (14)    Gasifying agent supply unit (20)    Space (22)    Combustion gas area (23)
NOVELTY - Producing ethanol comprises hydrogenating acetic acid in a reactor in presence of a catalyst comprising at least one active metal on a silica support, where the active metal is cobalt, copper, gold, iron, nickel, palladium, platinum, iridium, osmium, rhenium, rhodium, ruthenium, tin, zinc, lanthanum, cerium, manganese, chromium, vanadium and/or molybdenum.    USE - The method is useful for producing ethanol (claimed) that is used in e.g. fuels (for automobiles, boats and small piston engine aircraft), solvents (for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks and pharmaceuticals), chemical feedstocks, pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption.    ADVANTAGE - The catalyst exhibits: selectivity of greater than 60% to ethanol; and radial crush strength of at least 4 N/mm, preferably 4-12 N/mm (all claimed). The method: utilizes catalyst that is stable so that the decline in productivity is less than 6% per 100 hours; and provides less than 1% of undesirable products.
NOVELTY - A system of production of oligosaccharides specifically for organic rice is provided. The system includes a reaction tank, a plurality of feed tanks, a stirring device, a weighing device, a plurality of sensors, a temperature controlling device, a solid-liquid separation device, a controller, and a collection device. A plurality of feed tanks separately contain raw materials such as rice, water and enzyme solution. The sensors are used to detect the temperature and the pH value in the reaction tank. The controller modulates the raw materials from the feed tanks to the reaction tank and monitors the processing conditions of the reaction tank, so that the enzyme solution can treat the reactant to produce oligosaccharide, thereby simplifying the complicated steps of the conventional oligosaccharide process.
NOVELTY - Fuel additive formulation comprises a solution of hexylene glycol and boric acid.    USE - The fuel additive formulation is useful for preventing phase separation in ethanol blended fuels (claimed).    ADVANTAGE - The fuel additive formulation reduces friction, corrosion and wear in internal combustion engines that run on ethanol blended fuels, and thus: increases engine efficiency and performance, and extension of engine life; reduces engine emissions, green house gases and other environmental pollutants; and reduces repair and maintenance costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preventing phase separation in ethanol blended fuels comprising: providing the fuel additive formulation, where the formulation is formulated to inhibit or reverse phase separation in ethanol blended fuels and enhance anti-friction and anti-wear properties; and applying the fuel additive formulation to a vehicle having a fuel storage and delivery system which uses ethanol blended fuels.
NOVELTY - Extracting a lipid fraction from trap grease, comprises (a) mixing a volume of vegetable oil with a volume of trap grease, where the mixture is comprised of an aqueous fraction, a solid fraction and a lipid fraction, (b) heating the mixture to a temperature of 50-100 degrees C for a period of time sufficient to extract at least 80% of the lipids from the trap grease, and (c) separating a portion of the lipid fraction from the solid fraction.    USE - The method is useful for extracting a lipid fraction and forming biodiesel from trap grease (all claimed).    ADVANTAGE - The method is capable of extracting a lipid fraction from trap grease in a cost-effective and less energy intensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for forming biodiesel from trap grease comprising the step (a) as above per se, (b1) heating the mixture to a temperature of 50-100 degrees C for a period of time sufficient to evaporate the aqueous fraction, (c1) separating the solid fraction from a portion of the lipid fraction, and (d1) treating the portion of the lipid fraction with at least one of an acid esterification reaction or a transesterification reaction.
NOVELTY - The device has a reactor comprising an inner space with an oxidation zone for oxidization of a carbon-containing starting material and a reduction zone for reducing intermediate products of the oxidization. A heating unit (23) is arranged at a post-treatment unit (24) i.e. combustion unit, for heating the residual substance by a thermal reactor. Heat transfer partition walls (21) are provided between the post-treatment unit and the heating unit to transfer heat from the thermal reactor into an inner space (25) of the post-treatment unit and separating the inner space from the heating unit.    USE - Device for producing a flammable gas mixture from a carbon-containing starting material i.e. woods, in a system for producing heat energy and/or electrical power (claimed).    ADVANTAGE - The heating unit is arranged at the post-treatment unit for heating the residual substance by the thermal reactor such that the residual substance can be removed in a cost-effective manner, thus enabling economic operation of the system while increasing efficiency of the overall system.    DETAILED DESCRIPTION - The reactor is provided as the heating unit. The heat transfer partition walls are formed as reactor cladding housings. The post-treatment unit and/or the heating unit are designed as gasification and/or pyrolysis unit. An INDEPENDENT CLAIM is also included for a system for producing heat energy and/or electrical power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a post-treatment unit.    Suction element (2)    Heat transfer partition walls (21)    Heating unit (23)    Post-treatment unit (24)    Inner space of post-treatment unit (25)
NOVELTY - Apparatus (10) comprises a mixing device (14) including at least one mixing unit (12), which is rotatable around a vertical axis (24) using a motor (32) of the apparatus. The apparatus at the region of the axis includes a vertically extending shaft, in which a connecting line for the motor is vertically guided. The shaft has a widening at a junction, at which the connecting line is bent backwardly from the slot in the radial direction to the motor and is guided from the shaft, in order to protect the connecting line against an excessive mechanical stress during rotation of the mixing device.    USE - The apparatus is useful for mixing the contents of a biogas reactor (claimed).    ADVANTAGE - The biogas reactor exhibits high efficiency, and the apparatus minimizes the formation of thick and tough floating- and top layers on the surface of fillers of the reactor, thus it prevents upgrading and leakage of digestion gas during fermentation- or digestion process.    DETAILED DESCRIPTION - Apparatus (10) comprises a mixing device (14) including at least one mixing unit (12), which is rotatable around a vertical axis (24) using a motor (32) of the apparatus, where the motor is radially spaced from the axis. The apparatus in the region of the axis includes a vertically extending shaft, in which a connecting line for the motor is vertically guided. The shaft has a widening at a junction, at which the connecting line is bent backwardly from the slot in the radial direction to the motor and is guided from the shaft, in order to protect the connecting line against an excessive mechanical stress during rotation of the mixing device. An INDEPENDENT CLAIM is also included for a biogas reactor for generating biogas by decomposing biomass, comprising the above mentioned apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a bioreactor.    Apparatus (10)    Mixing unit (12)    Mixing device (14)    Axis (24)    Motor (32)
NOVELTY - Biotechnological complex comprises tank-receiving box, filtration unit, and biological purification unit which are connected sequentially. The tank-receiving box of fecal drains, mechanical cleaning unit, fecal pump, reactor-homogenizer, filtration unit, compost receiving box, biohumus unit and biohumus receiving box are connected sequentially. The unit of filtration has the output on the receiving box of filtrate, which is further connected sequentially with the reactor-fermentor of filtrate, the receiving box of bioslime and biohumus unit.    USE - The biotechnological complex is useful for processing fecal drains of the enterprises of housing and utilities economy (claimed).    DETAILED DESCRIPTION - Biotechnological complex comprises tank-receiving box, filtration unit, and biological purification unit which are connected sequentially. The tank-receiving box of fecal drains, mechanical cleaning unit, fecal pump, reactor-homogenizer, filtration unit, compost receiving box, biohumus unit and biohumus receiving box are connected sequentially. The unit of filtration has the output on the receiving box of filtrate, which is further connected sequentially with the reactor-fermentor of filtrate, the receiving box of bioslime and biohumus unit, where the fermentor unit is connected with the reactor-fermentor of filtrate, which is turn connected with cryogenic unit and the receiving box of water-salt concentrate. The complex further comprises unit for preparing foliage, and receiving area of the foliage. The biological purification unit has output on the receiving box of purified water.
NOVELTY - The installation comprises an agitator and doors. The agitator is provided with lateral units that are connected with walls of the doors.    USE - The installation is useful for preparing a compost (claimed).
NOVELTY - The production line has a peat portion whose output is sequentially and technologically connected by pulp line with section of mechanical processing unit of peat mass and with section of the stage of finished product. The output section of the peat portion is connected with the bottom of reservoir. The input section of biomass to the condensed peat is arranged before the section of mechanical processing of peat. The section of sublimation complete drying of the length of peat is arranged before the section of the stage of finished product.    USE - Production line for producing molded solid fuel from peat feedstock.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the production line for producing molded solid fuel from peat feedstock. (Drawing includes non-English language text)
NOVELTY - Autonomous peat-processing complex for producing and combusting peat-wood briquettes, comprises unit of splitting peat and crusher of sawdust with subsequent supply of ground sawdust in the unit of the pressing of fuel pellet or into the mixing and dispensing device, and the milled peat is into the unit of the pressing of fuel pellet or to the crusher of wet peat into the paste with subsequent supply of paste by screw into the mixing and dispensing device, connected with the point of forming, and drying peat-wood structure and group.    USE - The autonomous peat-processing complex is useful for producing and combusting peat-wood briquettes (claimed).
NOVELTY - Line for producing briquettes of fuel from waste of plant feedstock and filtrate, comprises sequentially installed feeding helical conveyer, magnetic separator, grinding mill, storage bunker, loading helical conveyer, briquetted device with molding chamber, produced in form of heated collar, and strip conveyor for supply of briquettes in sequentially installed devices for surface of briquettes and their packing in shrink-wrap, where the line additionally comprises bale opener and pug mill installed parallel to the storage bunker, where feedstock enters storage bunker and bale opener.    USE - The line is useful for producing briquettes of fuel from waste of plant feedstock and filtrate (claimed).
NOVELTY - An ionized hydrogen water is manufactured by making water and microorganisms to contact in which hydride ion is contained.    USE - Manufacture of ionized hydrogen water for generating hydrogen gas and for reducible drinking water (all claimed).    ADVANTAGE - The method is inexpensive and easy and the microorganism can carry out hydride ion production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) microorganisms which decompose hydrogen molecule and generates hydride ion comprises Bradyrhizobium genus, Mesorhizobium genus, Burkholderia sp. strain or Novosphingobium genus;    (2) method to generate hydrogen gas which involves adding acids such as hydrochloric acid or acetic acid to ionized hydrogen water and supplying hydride ion, or adding hydrocarbons such as ethanol to ionized hydrogen water and reacting with dissolved hydrogen and dissolved oxygen in ionized hydrogen water at the same time hydrocarbon is decomposed;    (3) reducible drinking water comprising ionized hydrogen water which is filtered or sterilized;    (4) foodstuff comprising the microorganisms as freeze-dry sample and to eat; and    (5) method to add methane and hydrogen sulfide to ionized hydrogen water and modifying to hydrogen gas.
NOVELTY - The reformer has a combustion zone (28) to receive at least fuel and to convert fuel into heat to provide heat to a reforming zone (29) arranged annularly about the combustion zone. The combustion zone includes a structured catalyst support provided on one side of a separating wall and coated with a catalyst to induce fuel combustion reaction. A reforming zone receives the fuel, and produces a reformate containing primarily hydrogen. The reformer side of separating wall includes a structured catalyst support coated with a catalyst to induce the fuel reforming reactions.    USE - Heat integrated reformer for production of hydrogen from fuel source for fuel cell applications.    ADVANTAGE - The combustion and reformer zones are separated by a metal partition and are in close thermal contact so as to facilitate the efficient transfer of heat from the combustion to the reforming zones.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an integrated steam reformer/combustor assembly for use in a fuel processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the heat integrated reformer.    Cylindrical wall (27)    Combustion zone (28)    Reforming zone (29)    Assembly housing (30)    Tapped tube (31)
NOVELTY - A heating article consists of lamellar element made of environmentally-friendly combustible material. A layer formed using plant components of fallen leaves of wood, bushes, grass, straw and/or poplar down and/or casing formed using seed of wood is arranged on lamellar element. The lamellar element is joined with assembly unit having spiral web structure using fixing component.    USE - Heating article (claimed).
NOVELTY - Fuel briquette obtained by compressing powdered wood and having a predetermined shape, which is spherical, is claimed.    USE - Used as a fuel briquette.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing briquettes, comprising a frame, a dispenser for compressible matrix mass containing the cylindrical lateral surface, a mechanism for creating a pressing force in the form of a group mounted on a fixed punch plate whose lengths successively increase by the end stage of briquetting, and a receiver finished briquettes drive, where each punch has a working surface of a hemispherical, each of the matrix is provided with a semi-spherical working surface, vertically movable bottom is rigidly secured to a spring loaded slider on the end containing the video, and the matrix is mounted on the track conveyor with the device mounted on the frame rectilinear guide and cam with curved track on the bottom surface to move along the guide rollers sliders.
NOVELTY - Pressure agglomerated molded solid fuel comprises plant biomass, where the plant biomass comprises shredded plant biomass and, as the essential binding material, cellulosic wool from hammer shredding of cellulosic material wastes, where the cellulosic material formerly being treated in papermaking process, and where the fuel shows a density of at least approximately 1100 kg/m3.    USE - As pressure agglomerated molded solid fuel (claimed).    ADVANTAGE - The pressure agglomerated molded solid fuel shows a density of at least 1050 kg/m3, preferably at least 1100 kg/m3, especially 1100-1200 kg/m3; is prepared at low power cost and without aid of additional binder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method (M1) of the preparation of molded solid fuel comprising pressure agglomerated plant biomass, involving: providing plant biomass and cellulosic material wastes, where the cellulosic material formerly being treated in papermaking process; shredding the plant biomass together with the mentioned cellulosic material wastes in a hammer rotor mill at an ambient temperature; and by performing pressure agglomeration of the obtained mixture without aid of a binder, under the pressure of 15-45 MPa at a temperature below 100 degrees C, to obtain molded fuel of a density of at least 1000 kg/m3.
NOVELTY - The installation has heat-transfer agent preparation unit that includes furnace and surface heater. A drying chamber is set with injecting mechanism for introducing slurry of biomass, gas-outlet flues for gaseous coolant, and line of unloading finished product. A purification system of finished heat-transfer agent is set with centrifugal tube, scrubber of Venturis, and surface condenser-cooler which is connected with scrubber through pneumo-separator. Output of finished heat-transfer agent is provided to prepared product unloading line in drying chamber.    USE - Installation structure for drying biomass.    DETAILED DESCRIPTION - The installation structure has finished heat-transfer agent through gas-outlet flue that is connected to surface heater, and condensate withdrawal line in fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the installation structure for drying biomass.
NOVELTY - Solid fuel composition comprises mixture of used coffee grounds and at least a cellulosic agent, which includes scurf of coffee grains.    USE - The solid fuel composition is useful for preparing by-products for food industry, and for preparing heating granule or pellet for an industrial boiler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition comprising drying the used coffee grounds in an oven, mixing the dried coffee grounds with scurf of coffee beans, humidifying the mixture to 15%, and granulating the humidified mixture on a sector.
NOVELTY - The method involves directing fast-flowing plasma through an electron removal area such that the fast-flowing plasma interacts with a target (20). Microwave energy is used in vicinity of the electron removal area to polarize the fast-flowing plasma as the plasma interacts with the target. A portion of free electron is removed within the plasma using an electron removal circuit (22). The plasma is decelerated and cooled such that fuel transitions from a plasma state to a non-plasma state in absence of the removed electrons. An altered molecular substance is collected.    USE - Method for modifying a molecular substance i.e. methane or propane hydrocarbon fuel, by altering molecular chain length for a motor vehicle.    ADVANTAGE - The method enables simply loading required and prepared fuel into a separate pressurized chamber, which is pressurized to a level greater than an accelerator chamber to produce a desired flow. The method enables reducing an amount of oxidizers in a fuel stock to minimize combustion phenomena, so that scrubbing process is employed to eliminate unwanted constituents. The method enables avoiding combustion process, so that production of unwanted greenhouse gas is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram illustrating process for modifying a molecular substance.    Fuel stock and additives (12)    Fuel injector (16)    Target (20)    Electron removal circuit (22)    Refinery (26)
NOVELTY - Producing hydrocarbons from biomass, involves: supplying a feed stream; supplying a heated hydrocarbon solvent; combining the feed stream and the heated hydrocarbon solvent to produce a reactor feed; and hydrodeoxygenating the reactor feed to produce hydrocarbons. The feed stream comprises a synthetic polymer and biomass having fatty acids and/or glycerides.    USE - For producing hydrocarbons from biomass (claimed). Also useful for the production of hydroprocessed biofuels such as renewable diesel and jet fuel, and bio-based products, such as solvents and chemical intermediates.    ADVANTAGE - The present process can trap phosphorus during conversion of fats and oils to biofuels and bio-based chemicals, such that the trapped phosphorus can economically be recovered for reuse (e.g. as fertilizer).
NOVELTY - Converting biomass oxygenates into hydrocarbon fuels, comprises (a) providing a biomass derived oxygenate feed, (b) hydrogenating the oxygenate feed with hydrogenation catalysts, (c) condensing obtained hydrogenated product with a condensation catalyst to produce a condensed or oligomerized product, (d) polishing the condensed or oligomerized product with a hydroprocessing catalyst, and (e) isolating obtained one or more hydrocarbon range fuel products.    USE - Converting biomass oxygenates into hydrocarbon fuels such as gasoline, vacuum gas oil, diesel, and jet-fuel, where the biomass is e.g. sugars, carbohydrates, lignins, fatty acids, proteins, oils, eucalyptus oil, forest residues, dead trees, branches, leaves or tree stumps (all claimed).    ADVANTAGE - The method ensures that the biofuels can be used as a gasoline substitute, and performs synthesis of hydrocarbons from biological sources without requiring more efficient and fungible source of renewable fuels in a wide range of application.
NOVELTY - Process (P1) for preparing a substituted N-(3,5-dichloro-pyridin-4-yl)-benzamide compound (VIc), comprises: (a) converting a substituted benzaldehyde compound (IIc) to a substituted (3,5-dichloro-pyridin-4-yl)-(1-phenyl-meth-(E)-ylidene)-amine compound (Vc) in a one-pot reaction; and (b) oxidizing (Vc) under conditions suitable to provide (VIc).    USE - The process is useful for preparing (VIc) (claimed), which is useful as anti-asthmatic agent or antiinflammatory agent. No biological data given.    ADVANTAGE - The process is simple, safe, economically efficient, energy efficient and environmentally friendly.    DETAILED DESCRIPTION - Process (P1) for preparing a substituted N-(3,5-dichloro-pyridin-4-yl)-benzamide compound of formula (VIc), comprises: (a) converting a substituted benzaldehyde compound of formula (IIc) to a substituted (3,5-dichloro-pyridin-4-yl)-(1-phenyl-meth-(E)-ylidene)-amine compound of formula (Vc) in a one-pot reaction; and (b) oxidizing (Vc) under conditions suitable to provide (VIc).R1, R2 = 1-4C alkyl (that is partially or completely substituted with F), 3-7C cycloalkylmethyl (both preferred), H, 1-6C alkyl or 3-7C cycloalkyl.    INDEPENDENT CLAIMS are also included for:    (1) the compound (Vc);    (2) a substituted 4-dihydroxymethyl-benzene-1,2-diol compound of formula (IIIc); and    (3) a process (P2) for preparing (VIc), comprising: contacting (IIc) with 3,5-dichloro-pyridin-4-ylamine under conditions sufficient to provide (Vc); and the step (b) as above per se.    either R4, R5 = 1-6C alkyl or acyl; or    R4+R5 = 5-7 member cyclic ring (optionally substituted).
NOVELTY - Method (M1) for chain modification of hydrocarbons and organic compounds, comprises: contacting an aqueous electrolyte (120), a powered electrode including a catalyst, and a gaseous methane feedstock (130) in a reaction area; and activating the methane in an aqueous electrochemical reaction to generate methyl radicals at the powered electrode to yield a product (160).    USE - The method is useful for chain modification of hydrocarbons and organic compounds.    ADVANTAGE - The method: prevents the deposition of impurities in water, hence prevents the deactivation of the catalyst; and can be performed at room temperatures and pressures, as compared to conventional methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for chain modification of hydrocarbons and organic compounds, comprising: contacting an aqueous electrolyte with a catalyst in a reaction area; introducing the gaseous methane feedstock directly into the reaction area; and reacting the aqueous electrolyte, the catalyst and the gaseous methane feedstock at a temperature of -10 to 1000 degrees C and pressure of 0.1-100 ATM.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an electrolytic cell.    Electrochemical cell (100)    Electrolyte (120)    Gaseous methane feedstock (130)    Three phase interface (155)    Product (160)
NOVELTY - Producing liquid fuel from synthesis gas, involves reacting the gas at pressures of 500-3000 psi and temperature of 200-400 degrees C over a catalyst, where the catalyst is copper, zinc, and potassium on a substrate.    USE - For producing liquid fuel comprising methanol, ethanol, propanol, butanol, and hydrocarbons from synthesis gas (claimed) used in automobiles.    ADVANTAGE - The method increases both the quantity and quality of product; produces liquid fuel that is usable in high concentration in both existing gasoline and diesel engines, and transportable in existing pipelines.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst comprising copper, zinc, and potassium deposited on a substrate; or copper on hydrotalcite, where the hydrotalcite is a strongly basic variety with a magnesium oxide (MgO) to alumina ratio of greater than 1:1.
NOVELTY - The apparatus (1) has a material supply device (12) that supplies a source gas. A combustor (15) burns source gas and combustible gas of hydrogen-containing-gases with air and heats modifier (7). A selective-oxidation device (9) oxidizes carbon monoxide in hydrogen-containing-gas by oxidizing agent gas. An oxidizing agent gas supply device (14) supplies oxidizing agent gas. A controller (17) controls supply amount of air and supply amount of oxidizing agent gas, based on specific ratio of mass flow rate of source gas and volumetric flow rate of source gas.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The carbon monoxide contained in the hydrogen-containing-gas can be removed fully, so that the performance of the hydrogen generating apparatus can be maintained. The efficiency and useful durability of the hydrogen generating apparatus can be improved effectively. The situation of fall and power generation stop of the electric power generation efficiency of the fuel cell can be prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell system; and    (2) a method for operating hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Modifier (7)    Selective-oxidation device (9)    Material supply device (12)    Oxidizing agent gas supply device (14)    Combustor (15)    Controller (17)
NOVELTY - Recovering oil from thin stillage obtained in the production of a fuel from a carbon source, comprises contacting thin stillage with yeast or a salt to enhance separation of oil from the thin stillage, and separating oil from the yeast-containing thin stillage, where the thin stillage is an emulsion comprising water, dissolved solids and oil.    USE - The process is useful for recovering oil from thin stillage obtained in the production of a fuel from a carbon source (claimed), where the fuel is biofuel.    ADVANTAGE - The process allows simple and economical recovery of the oil from thin stillage with high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) producing ethanol from the carbon source containing polysaccharides, comprising reducing the polysaccharides in the carbon source to produce simple sugars, fermenting the simple sugars to produce ethanol and whole stillage, separating the whole stillage into a distillers grain component and a thin stillage component, contacting the thin stillage component with yeast or salt, and separating oil from the yeast/salt-containing thin stillage component; and    (2) enhancing the separation of oil from a oil-in-water emulsion comprising at least 1 wt.% of oil and at least 5 wt.% of solids, comprising contacting the emulsion with the yeast/salt.
NOVELTY - A catalytic biomass pyrolysis process involves reacting a biomass starting material under pyrolysis conditions in presence of catalyst and forming a stream comprising a pyrolysis product.    USE - Catalytic biomass pyrolysis process used for producing food products and biofuel for boiler, diesel engine and turbine.    ADVANTAGE - The method is carried out efficiently and economically using simple process in short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalytic biomass pyrolysis system.
NOVELTY - An electrode (100) has a photocatalyst layer (10), a current collection layer (30), and a contact layer (20) including semiconductor or conductor provided between the photocatalyst layer and current collection layer. The contact layer is provided along surface shape of the current collection layer side of the photocatalyst layer.    USE - Electrode is used for manufacture of hydrogen (claimed).    ADVANTAGE - The electrode increases conduction path between photocatalyst layer and current collection layer without inhibiting absorption of light by photocatalyst, and has excellent photoelectric conversion efficiency. The manufacture of hydrogen is efficiently manufactured in a short period of time, using the electrode.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of electrode, which involves forming photocatalyst layer, covering semiconductor or conductor to one side of the photocatalyst layer, forming contact layer, and forming current collection layer in a surface on the opposite side to the photocatalyst layer of the contact layer; and    (2) manufacture of hydrogen, which involves irradiating light to the electrode immersed in water or electrolyte aqueous solution, and performing optical hydrolyzing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrode.    Photocatalyst layer (10)    Photocatalyst particles (11)    Contact layer (20)    Current collection layer (30)    Electrode (100)
NOVELTY - Biorefining, involves: providing lignin biomass; processing the lignin biomass such as chemical processing, catalytic processing, biological processing and pyrolytic processing; and producing at least one product from the lignin biomass.    USE - For biorefining, for producing biobased chemicals, biofuels, and lignin residues, where the biobased chemicals comprise chemical of commodity chemicals, fine chemicals, and specialty chemicals. The biofuels include transportation fuels, heating fuels, and fuel additives. The transportation fuels include automobile fuels, truck fuels, ship fuels, and aircraft fuels. The heating fuels include home heating fuels, commercial heating fuels, and industrial boiler fuels (all claimed).    ADVANTAGE - The lignin residues provide energy production i.e. heat or power. The lignin biomass has a weight, and a waste product of the lignin biomass is less than 30 (preferably 10)% of the lignin biomass weight. The waste products of the processing of the lignin biomass provide energy production i.e. heat or power. The product of the lignin biomass has an economic value higher than boiler fuel. The method allows for the selective production of the biobased aromatic chemicals and biofuels. Additionally, a reduction of waste products may also be provided from the present method. The method utilizes lignin from biomass and other waste lignin sources, and converts them to value-added biobased materials while minimizing waste products within the process.
NOVELTY - Producing fuels and chemicals from biomass feedstock, comprises: (a) drying the biomass feedstock using heated dry carbon monoxide gas; (b) devolatilizing the feedstock by reductive torrefaction with heated dry carbon monoxide gas; (c) pulverizing the feedstock; and (d) pyrolyzing the feedstock by reductive pyrolysis with high pressure or high temperature carbon monoxide gas.    USE - The process is useful for producing fuels and chemicals from biomass feedstock where the fuel includes pipeline quality natural gas, dean syngas, gasoline, diesel fuel, aviation fuel, fuels oils and lubricants.    ADVANTAGE - The process: is simple, flexible, allows direct conversion of biomass feedstocks to desirable hydrocarbon; reduces yields of undesired co-products and processing temperatures, and allows construction from less costly alloys, especially for high halide containing feedstocks; and reduces production of polycyclic aromatic hydrocarbons, dioxins, other refractory organic compounds, and high viscosity by-products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an integrated system for producing fuel or chemicals from biomass feedstock comprising: a fixed bed reactor; a source of heated dry carbon monoxide gas for drying the feedstock; source of heated dry carbon monoxide gas for devolatilizing the feedstock; a means for pulverizing the feedstock; and a source of high pressure or high temperature carbon monoxide gas for pyrolyzing the feedstock by reductive pyrolysis; and    (2) a means for producing fuels and chemicals from biomass feedstock.
NOVELTY - A catalyst precursor comprises chemical composition containing oxygen, carbon, hydrogen and optionally nitrogen, and primary and secondary elements. The catalyst precursor has surface area of 0.1-50 m2/g.    USE - Catalyst precursor used for manufacture of fructose, methanol and formaldehyde, and iso-butane (all claEP2636446A1imed).    ADVANTAGE - The catalyst precursor and catalyst have high catalytic activity even when the surface area is low. The catalyst precursor and the catalyst are manufactured by a short and simple process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of catalyst precursor, which involves generating an aerosol comprising a mixture of organic derivatives, optionally diluting aerosol by gas and passing aerosol in plasma generated between electrodes at least one of which is being provided with a dielectric, to obtain catalyst precursor on one of the electrodes;    (2) semi-crystalline catalyst is obtained by the calcination of catalyst precursor;    (3) manufacture of fructose, which involves isomerizing glucose by using catalyst precursor;    (4) manufacture of methanol and formaldehyde, which involves converting methane and carbon dioxide using catalyst precursor; and    (5) manufacture of iso-butane, which involves isomerizing n-butane using catalyst precursor.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus used for manufacture of catalyst precursor.    Mass flow controllers (1, 2)    Atomizer (3)    Precursor liquids (4)    Flat water cooled aluminum electrodes (5, 6)    Glass plate (7)
NOVELTY - A porous material consists of a crystalline anodized film (2) having several pores (1), formed by anodizing process of aluminum or aluminum alloy, and penetrated in thickness direction. The zeta potential of total surface or one portion at the time of usage of porous material is less than 0 mV.    USE - Porous material for turbidity removal of raw water containing microorganisms and microorganisms separation membrane of membrane separation activated sludge process equipment (all claimed).    ADVANTAGE - The porous material prevents adhesion of living organisms.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of porous material.    Pore (1)    Anodized film (2)    Aluminum nacelle (3)
NOVELTY - A peptide comprising specific amino acid sequence, is new.    USE - The peptide is useful in metal adsorption agent for recovering metal, preferably rare metal chosen from palladium and platinum, from aqueous solution (all claimed).    ADVANTAGE - The peptide has minimal environmental impact and consumes minimal energy as compared to existing method.    DETAILED DESCRIPTION - A peptide comprising amino acid sequence of Ser-Asp-Pro-Leu-Val-X1-Arg-Ala-Ser-Leu-Ile-Gly-Leu-Leu-X2-Leu-Leu-Leu-Trp-X3-X4-X5-Arg-X6 (SEQ ID NO: 1), is new. The peptide comprises 100 or less amino acid residues.    X1=hydrophilic amino acid;    X2=His or Ala;    X3=Asp or Glu;    X4=aliphatic amino acid Met;    X5=Glu or Asp;and    X6=any amino acids.    INDEPENDENT CLAIMS are included for the following:    (1) metal adsorption agent comprising the peptide;    (2) method (M1) for recovering metal, involves contacting the aqueous solution containing the metal and the metal adsorbent; and    (3) method (M2) for detecting rare metal, involves performing the above-mentioned method (M1), and detecting structural change of the peptide.
NOVELTY - A hydrogen-separation system consists of hydrogen separator (11), decompression device (13), gas utilization apparatus (15), supply line (21), primary side line (22a) and secondary side line (22b). The fuel gas containing combustible gas is supplied to the hydrogen separator through supply line, where the hydrogen separates out, and reaches the decompression device through primary side line and the hydrogen pressure is reduced. Finally, the separated fuel gas reaches the gas utilization apparatus through the secondary side line and utilized.    USE - Hydrogen-separation system is used for separating hydrogen from fuel gas supplied to gas utilization apparatus e.g. gas engine or burner (claimed), waste gas discharged in chemical process, coal and petroleum refining off gas, natural gas, reformed gas and coke oven gas.    ADVANTAGE - The hydrogen-separation system separates hydrogen from basic fuel gas efficiently, prevents knocking and back fire in gas engine, and is compact.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the structure of hydrogen-separation system.    Hydrogen separator (11)    Decompression device (13)    Gas utilization apparatus (15)    Supply line (21)    Primary side line (22a)    Secondary side line (22b)
NOVELTY - A bacteria is obtained by introducing polynucleotide encoding D-lactate dehydrogenase into hydrogen-oxidizing bacteria, is new.    USE - The bacteria is useful for producing D-lactic acid (claimed).    ADVANTAGE - The bacteria produces D-lactic acid cost-effectively with high optical purity and reduced environmental impact, and can avoid the propagation inhibition by accumulating organic acid, and minimize the production of byproducts. The method is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the D-lactic acid, which involves culturing the above-mentioned bacteria.
NOVELTY - Method for utilizing excrement of pig, involves composting excrement of pig through selected composting process, where the composted manure is used as boiler fuel.    USE - The method is useful for utilizing excrement of pig as boiler fuel (claimed).    ADVANTAGE - The method effectively utilizes excrement of pig without requiring new installation and operation. The excrement of pig utilized as fuel for boiler does not exert any bad influence on operation on boiler.
NOVELTY - Pig excrement is utilized by selecting composting process of pig excrement, composting, and using compost as fuel.    USE - Utilization method of pig excrement (claimed).    ADVANTAGE - Pig excrement can be effectively used as low-cost fuel which does not affect the operation of an industrial furnace.
NOVELTY - A catalyst composition comprises calcium oxide as main component and has 90% accumulation value (D90) of particle size distribution of catalyst particles of 2 mu m or less.    USE - Catalyst composition used for manufacture of biodiesel fuel (claimed).    ADVANTAGE - The catalyst composition is manufactured economically using inexpensive raw materials. Since the catalyst having high reaction efficiency is used, the deterioration of the biodiesel fuel can be prevented effectively. Since the catalyst composition is enclosed in a non-oxidizing atmosphere, the deterioration of the catalyst is prevented and the catalyst composition with stable quality is provided. Since the adhesion of the residual catalyst particles to the reaction container is prevented effectively, the productive efficiency of the biodiesel fuel is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst composition, which involves distributing the catalyst raw materials containing calcium oxide in the solvent containing biodiesel fuel, primary grinding the catalyst raw material of 10 mu m or less in the calcium oxide dispersion liquid and secondary grinding the primary ground raw material produces catalyst particles of 2 mu m or less, to obtain catalyst composition; and    (2) manufacture of biodiesel fuel (BDF), which involves reacting lower alcohols and fats and oils in the presence of catalyst composition, having 0.05-0.5 pt. wt. catalyst particles with respect to 100 pts. wt fats and oils.
NOVELTY - Reprocessing raw liquid manure and/or fermentation residues obtained during biogas production, comprises: (a) clarifying the raw liquid manure and/or fermentation residues (110) in a first treatment unit (120) to obtain a first solid phase (4) and a first clarified liquid phase (5); (b) preconditioning the first clarified liquid phase; and (c) clarifying the first clarified and preconditioned liquid phase in a second treatment unit (150) to obtain a second solid phase and a second, further clarified liquid phase or clear phase.    USE - The method is useful for reprocessing raw liquid manure and/or fermentation residues obtained during biogas production.    ADVANTAGE - The method is carried out in a simple and improved manner that enables waste-disposal of treated liquid phase with regard to removal of slimy substances from the clear phase using the centrifuge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for carrying out the above mentioned method, comprising at least a first centrifuge, preferably a solid bowl helical conveyor centrifuge for dewatering the first clarified liquid phase and the first solid phase from the raw liquid manure and/or fermentation residues, and a first dosing unit for adding a flocculant to the first clarified liquid phase, or for adding an agent for adjusting the pH value of the first clarified liquid phase.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block representation of the method for reprocessing raw liquid manure and/or fermentation residues obtained during biogas production.    First solid phase (4)    First clarified liquid phase (5)    Raw liquid manure and/or fermentation residues (110)    First treatment unit (120)    Second treatment unit (150)
NOVELTY - Oil is recovered and ethanol is produced by dissolving starch by crushing organic refuse from home, hospital, and school, removing residue solid, adding enzyme in saccharification container in which saccharification solution has temperature of greater than or equal to 28 degrees C, and separating aqueous solution and oil component by 3-phase solid separation recovery using centrifugal separator in which separation process is performed in fermentation step only.    USE - Recovery and manufacture of ethanol and oil (claimed).    ADVANTAGE - Recovery and manufacture process of ethanol and oil is easy, ethanol manufacturing cost is reduced by effective utilization of recovered steam of incineration furnace, and amount of fossil fuel used in refuse treatment facility is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of oil recovery and ethanol production process. (Drawing includes non-English language text).
NOVELTY - An Escherichia coli capable of producing 3-amino-4-hydroxybenzoic acid from dihydroxyacetone phosphate, is new. The E.coli is modified such that to reduce activity of N-hydroxyarylamine O-acetyltransferase (NhoA) and increase aspartic semialdehyde.    USE - The E.coli is useful for producing 3-amino-4-hydroxy benzoin acid which is used for manufacturing polymer. The polymer is polybenzoxazole polymer (all claimed). The 3-amino-4-hydroxy benzoin acid is used as intermediate of dye, agrochemical, and other pharmaceuticals.    ADVANTAGE - The method is cost-effective as it utilizes E.coli, and environmentally-friendly. The polybenzoxazole polymer is highly thermostable, and has high strength, and high elastic modulus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing the 3-amino-4-hydroxy benzoin acid, involves cultivating the E.coli; and (2) method for manufacturing polymer which contains the 3-amino-4-hydroxy benzoin acids, involves polymerizing the 3-amino-4-hydroxy benzoin acid as a structural unit.
NOVELTY - A working fluid composition comprises a refrigeration oil having kinematic viscosity at 100 degrees C of 2-50 mm2/second and containing a complex ester having acid value of 0.5 mg potassium hydroxide/g or less and obtained by esterifying an ester intermediate obtained by reacting a neopentylpolyol and a dibasic acid with 1-20C monovalent alcohol and/or 2-20C fatty acids as base oil, and 2-4C hydrocarbon refrigerant.    USE - Working fluid composition for refrigerator, room air-conditioner and packaged air-conditioner.    ADVANTAGE - The working fluid composition has favorable compatibility, solubility with respect to hydrocarbon refrigerant, lubricity, electric insulation property and stability, and provides refrigerator having high cooling efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) refrigeration oil; and    (2) manufacture of refrigeration oil.
NOVELTY - The manufacturing method involves preparing fluorine-type solvent that is mixed with high oxygen permeable resin (34). The polymer electrolyte precursor is distributed in resin solution produced by dissolving high oxygen permeable resin in fluorine-type solvent. The high oxygen-permeable resin has oxygen permeability that is higher than oxygen permeability of polymer electrolyte.    USE - Method of manufacturing catalyst ink used in producing fuel cell of battery.    ADVANTAGE - Electric power generation performance of fuel cell is enhanced by improving the catalyst ink for forming catalyst electrode layer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the cathode structure.    Cathode (22)    Catalyst carrying carbon (30)    Polymer electrolyte (32)    High oxygen permeable resin (34)    Resin layer (35)
NOVELTY - Combined bioreactor for treating waste water, by anaerobic, aerobic and anoxic processes of degradation of organic matter with zone separator system and collection of biogases, scum and sludge, comprises an anaerobic zone on the bottom where organic matter is degraded by anaerobic bacteria which produce biogas (methane (CH4) and carbon dioxide (CO2)), an anoxic zone in the middle where denitrifying bacteria convert nitrates into gaseous nitrogen, and an aerobic zone in the upper part with a biological contact rotor.    USE - The combined bioreactor is useful for treating waste water, by anaerobic, aerobic and anoxic processes of degradation of organic matter with zone separator system and collection of biogases, scum and sludge (claimed).    ADVANTAGE - The bioreactor can achieve removal efficiency for biological oxygen demand (BOD) and total suspended solids (TSS) of greater than 95%. The power consumption is minimized. By using the biorector, one of the processes has the lowest cost per cubic meter of treated water.    DETAILED DESCRIPTION - Combined bioreactor for treating waste water, by anaerobic, aerobic and anoxic processes of degradation of organic matter with zone separator system and collection of biogases, scum and sludge, comprises an anaerobic zone on the bottom where organic matter is degraded by anaerobic bacteria which produce biogas (methane (CH4) and carbon dioxide (CO2)), an anoxic zone in the middle where denitrifying bacteria convert nitrates into gaseous nitrogen, and an aerobic zone in the upper part with a biological contact rotor, where nitrifying bacteria convert ammoniacal nitrogen into nitrites and nitrates; and the bioreactor comprises separators of rhomboidal section which define conical collectors which, when combined, form a polyhedral separator panel, each conical collector comprising a nozzle that connects it to a biogas network or to a sludge and scum network.
NOVELTY - A lignosulfonate (LS) gas hydrate comprises gas hydrate crystals; and LS.    USE - To transport and store methane gas used in energy production (claimed).    ADVANTAGE - The lignosulfonate gas hydrate increases the formation rate of methane hydrate. The induction and formation time required to reach 90% of the final volumetric capacity of the methane hydrate may be little as 100 minutes, 30 minutes, or even 5 minutes. The induction and formation time required to reach substantially full actual storage capacity is as little as 1000 minutes. The LS methane hydrate can be provided directly to an energy production facility, such as a combustion chamber. Unlike most current methane hydrates, in which the methane is first released and the promoter, such as sodium dodecyl sulfate (SDS), is recovered, there is no need for pre-release of methane when using methane hydrates containing LS. LS is cheap and simply burns along with the methane. Due to the low amounts of LS in the methane hydrates, any release of sulfur compounds is negligible. Water is vaporized and released with other exhaust gasses.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) making a lignosulfonate gas hydrate involving combining gas, liquid or solid water, and LS at controlled temperature and starting pressure for a time sufficient to form LS gas hydrate;    (2) method of producing energy from a lignosulfonate combustible gas hydrate involving providing an LS combustible gas hydrate directly to a combustion chamber, where combustible gas in the combustible gas hydrate and LS are converted to energy in the combustion chamber and water in the combustible gas hydrate is converted to steam;    (3) method of releasing gas from a lignosulfonate gas hydrate involving heating an LS gas hydrate to at least 0 degrees C.
NOVELTY - Propane and ethylene are made to contact with the trans hydrogenation catalyst at 50-400 degrees C to obtain propylene and ethane.    USE - Manufacture of propylene (claimed).    ADVANTAGE - The method enables economic manufacture of propylene with high selectivity.
NOVELTY - Method for purifying oil-polluted soil, involves mixing fertilizer and wood vinegar which were manufactured from raw material containing wood vinegar and fine coal in the oil-polluted soil contaminated with oil, and waiting for oil-polluted soil to change into good quality soil.    USE - The method is useful for purifying oil-polluted soil (claimed).    ADVANTAGE - The method requires less time and is environmentally-friendly.
NOVELTY - Preparing multifunctional organic fertilizer, involves (a) preparing organic materials, (b) preparing functional microorganism composition using functional microorganism breeding strains e.g. Streptomyces sp. strain DA1 0202 (cellulose decomposition) and Azotobacter vinelandii strain M2Per (nitrogen fixation), and (c) uniformly mixing the product obtained in step (a) with the product obtained in step (b), and adding mineral nutrients including urea, superphosphate, potassium oxide, and meso/microelements to the mixture, and piling the product.    USE - The method is useful for preparing multifunction organic fertilizer which is useful for rubber trees in nursery stage.    DETAILED DESCRIPTION - Method for preparing multifunctional organic fertilizer, involves (a) preparing organic materials including peat, agricultural byproducts and manure, removing impurities contained in organic materials, pre-treating each of the organic materials by immersing in clear lime water with a moisture of 40-45%, mixing each of the pre-treated organic materials with urea, spreading a microorganism composition evenly, covering and annealing to form carriers, and mixing the carriers to obtain carrier mixture, (b) preparing functional microorganism composition using functional microorganism breeding strains including Streptomyces sp. strain DA1 0202 (cellulose decomposition), Azotobacter vinelandii strain M2Per (nitrogen fixation), Bacillus subtilis strain BL10 (phosphate decomposition), Bacillus amyloliquefaciens strain LSC04 (indole-3-acetic acid (IAA) generation), Azotobacter beijerinckii strain ICMP 8673 (mucous membrane generation) and Bacillus subtilis (disease resistance), and (c) uniformly mixing the product obtained in step (a) with the product obtained in step (b), and adding mineral nutrients including urea, superphosphate, potassium oxide, and meso/microelements to the mixture, and piling the product.
NOVELTY - Fatty acid compounds and their esters production involves pre-heating reactants at 100-290 degrees C, where esterification reaction and dehydration polymerization are performed with glycerol at 300-450 degrees C and a pressure of 100-2500 psi by using a heterogeneous acid catalyst. The reactor effluent and esters of fatty acids, hydrocarbons, water and gases are separated.    USE - Method for producing fatty acid compounds and their esters used for preparing biodiesel comprising diesel, diesel oil or optional additives (claimed).    ADVANTAGE - The method efficiently produces fatty acid compounds and their esters in a simple manner, which provides an alternative fuel having physical and chemical properties similar to petroleum diesel, which can be used directly in motors without mechanical modifications or expenses maintenance. The obtained biodiesel is biodegradable and safe to handling, transporting and storing.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting gas chromatography-mass spectrometry analysis of the biodiesel phase upper layer. (Drawing includes non-English language text).
NOVELTY - The catalyst includes alcoholic alkali metal oxide combined with an alkali metal hydroxide. The alcoholic alkali metal oxide and metal hydroxide are alkaline earth metal having a particle size of 50-500 mesh.    USE - Catalyst used for producing esters from vegetable oils or animal fat through transesterification by using aliphatic alcohol (all claimed) and for producing biodiesel fuel for diesel engines.    ADVANTAGE - The catalyst efficiently produces biodiesel in a simple and cost-effective manner with improved yield.
NOVELTY - Metantek (sic) comprises a vertical cylindrical tank with many nozzles for supplying organic waste, discharging spent substrate and removing biogas to improve digestion, where the cylindrical container is enclosed in a heat insulating housing made of polystyrene and has a tapered bottom and the spherical dome.    USE - The metantek (sic) is useful for aerobic fermentation of diluted organic waste.
NOVELTY - The biodiesel is obtained by performing transesterification reaction with methyl and basic catalyst with vegetable fat from almond seeds, which are domestic and industrial discharges. The almond seed is a fruit of Anacardiaceae family plants. The fruit is also selected from Mangifera indica, Mangifera domestica or Mangifera sativa. The basic catalyst is sodium hydroxide.    USE - Biodiesel.    ADVANTAGE - The biodiesel is obtained by performing transesterification reaction with methyl and catalyst material vegetable fat from almond seeds, and thus provides environmental preservation, shows an acid value of 0.72 mg KOH/g, and can be prepared in a simple, eco-friendly and cost-effective manner by using seed fat which are domestic and industrial discharges.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biodiesel.
NOVELTY - Extracting bambusoideae leaves comprises adding subcritical solvent to bambusoideae leaves to extract.    USE - The method is useful for extracting bambusoideae leaves to produce a cosmetic composition (all claimed) comprising skin lotion, skin softener, skin toner, astringent, lotion, milk lotion, moisture lotion, nutritive lotion, massage cream, moisturizing cream, moisture cream, hand cream, foundation, essence, nutritious essence, pack, soap, cleansing foam, cleansing lotion, cleansing cream, body lotion and body cleanser.    ADVANTAGE - The method is capable of rapidly extracting the bambusoideae leaves in an environmental friendly and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising bambusoideae leaves extract.
NOVELTY - Single step heterogeneous catalytic process for preparation of alkynyl carboxylic acids (I), comprises carboxylation of terminal alkynes (II) with carbon dioxide in the presence of a heterogeneous catalyst, a base and a solvent at 50-60 degrees C for 12-16 hours under a pressure of 1 atmosphere.    USE - The process is useful for preparation of alkynyl carboxylic acids (I).    ADVANTAGE - The process: provides alkynyl carboxylic acids (I) with an yield of 70-94%, and has selectivity to alkynyl carboxylic acids (I) of 100%; is simple, reproducible, efficient and environmentally friendly; utilizes the heterogeneous catalyst that is economical, stable under thermal and air, and can be recovered and reused for several times without losing its activity; can be performed at ambient conditions with greater selectivity and yields; tolerates series of functional groups, such as alkoxy, fluoro and chloro; and enables synthesis of varied propiolic acids.    DETAILED DESCRIPTION - Single step heterogeneous catalytic process for preparation of alkynyl carboxylic acids of formula (R-CC-CO2H) (I), comprises carboxylation of terminal alkynes of formula (R-CC-H) (II) with carbon dioxide in the presence of a heterogeneous catalyst, a base and a solvent at 50-60 degrees C for 12-16 hours under a pressure of 1 atmosphere.    R = monovalent substituents consisting of alkyl, alkenyl, alkenyloxy, alkynyloxy, alkenylthio, alkynylthio, aryl, alkaryl, aralkenyl, aralkynyl, aryloxy, aralkoxy, cycloalkyl, heteroaryl or carbonyl (all optionally substituted by halo, hydroxy, nitro, amino, cyano, carbonyl, alkoxy, carboxy, ester, alkyl, alkenyl, alkynyl, thio, sulfonyl, sulfinyl, phenyl, heteroaryl or carbonyl).
NOVELTY - A bubble-free hydrogen supply device comprises hydrogen storage tank (5) through the pressure regulating valve and a bubble-free hydrogen supplying membrane assembly (1) and one end of the hydrogen chamber (7), bubble-free supplying membrane assembly is connected to the other end of carbon dioxide gas chamber by a pressure regulating valve and a carbon dioxide storage tank (6) is connected with secondary treatment water inlet pump (4) and connected to bubble-free supply inlet, and water outlet is connected to the biological contact reaction device (2) through the water pump (3).    USE - Bubble-free hydrogen supply device used for autotrophic denitrification of nitrate nitrogen in sewage treatment (claimed).    ADVANTAGE - The device has high removal efficiency of conversion of nitrate to nitrogen.    DETAILED DESCRIPTION - A bubble-free hydrogen supply device comprises hydrogen storage tank through the pressure regulating valve and a bubble-free hydrogen supplying membrane assembly and one end of the hydrogen chamber, the bubble-free supplying membrane assembly is connected to the other end of carbon dioxide gas chamber by a pressure regulating valve and a carbon dioxide storage tank is connected with the secondary treatment water inlet pump and connected to bubble-free supply inlet of the hydrogen membrane assembly, the water outlet is connected to the biological contact reaction device through the water pump and is connected with the bubble-free inlet, and the other end of the outlet is connected to the filter unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device.    Bubble-free hydrogen supplying membrane assembly (1)    Biological contact reaction device (2)    Water pump (3)    Water inlet pump (4)    Hydrogen storage tank (5)    Carbon dioxide storage tank (6)    Hydrogen chamber (7)
NOVELTY - A sewage treatment equipment comprises processing device (1) provided with a feeding and discharging device (2) with a liquid level controller (21) set on the inner cavity of the processing device, drain valve (3) at the bottom, external circulation control device (4) and a dosing device (5). The processing device is connected to the inner cavity of the feed pipe (22) and the discharge pipe (23) with feed pump (24) and discharge pump (25). The feed and discharge pumps were adjusted automatically through the feed and outlet valves which are connected to the liquid level controller.    USE - Sewage treatment equipment.    ADVANTAGE - The equipment is more convenient to operate, has good effect, and has cheaper labor force. The external circulation control device improves the strains of mixing effect and effectiveness of the treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage treatment equipment.    Processing device (1)    Feeding and discharging device (2)    Drain valve (3)    External circulation control device (4)    Dosing device (5)    Liquid level controller (21)    Feed pipe (22)    Discharge pipe (23)    Feed pump (24)    Discharge pump (25)
NOVELTY - A sewage treatment device comprises concrete blocks (1) provided with multiple water holes (2), and is set within a cavity filled with porous microbial carrier (3) (preferably ceramic chip, coke or coral) that adheres to the surface layer of water vaccine.    USE - Sewage treatment device.    ADVANTAGE - The device is capable of purifying contaminated water, river water and sea water. The concrete block is designed into rock or wood-like shape so that the device has beautifying effect to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage treatment device.    Concrete blocks (1)    Multiple water holes (2)    Porous microbial carrier (3)
NOVELTY - Synthesis of glipizide involves protecting 4-(2-amino ethyl)benzenesulfonic acid ammonia by t-butoxy carbonyl anhydride, reacting the protected compound with cyclohexyl isocyanate, deprotecting obtained reaction product, and reacted deprotected compound with 2-methyl-5-pyrazine carboxylic acid.    USE - Synthesis of glipizide (claimed).    ADVANTAGE - Glipizide with high purity of 99% or more is prepared at high yield without affecting the environment.
NOVELTY - A mild alkali soil modifying agent comprises 80-90 pts. wt. desulfurization waste, 3-5 pts. wt. inorganic accelerant, and 8-15 pts. wt. organic accelerator.    USE - A mild alkali soil modifying agent for improving soil.    ADVANTAGE - The mild alkali soil modifying agent improves soil fertility, reduces alkalization of soil, improves crops growth, increases fertilizer effect, and has pH value of higher than 8.5, water content of 10-20%, salt content of less than 0.5%, fine pore structure and excellent physical properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using mild alkali soil modifying agent comprising applying 1500-2000 kg/ hectare mild alkali soil modifying agent to the soil at a depth of 10 cm, irrigating 70 wt.% water, and irrigating 30 wt.% water.
NOVELTY - A Scenedesmus species strain ENN32 (CGMCC No. 6346), is new.    USE - The S.species strain ENN32 is useful for production of biofuel, preferably biodiesel or bialcohol, providing environmental protection, preferably sewage treatment of nitrogen, phosphorus, organic degradation and/or heavy metal ion adsorption or carbon dioxide outlet, and for preparing soybean acid, palmitic acid, palmitoleic acid, stearic acid, octadecenoic acid, parinaric acid, alpha -linolenic acid, gamma -linolenic acid, arachidic acid, behenic acid, astaxanthin, carotene, lutein, zeaxanthin and/or canthaxanthin medicament, food, health care products, feed product, aquatic product baits, drugs, cosmetic and/or pigments (all claimed).    ADVANTAGE - The S.species strain ENN32 has fatty acid content of greater than 40 wt.%, preferably 51-60 wt.% by dry weight, and has fast growth, and rapid grease accumulation. The tolerance temperature of S.species strain ENN32 0-40 degrees C, preferably 25 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing the S.species strain, which involves inoculating the S.species strain in BG11 culture medium at illumination intensity of 50-500 mu mol/m2.second, preferably 250-300 mu mol/m2.second, pH of 7-9, preferably 8, and temperature of 15-35 degrees C, preferably 25 degrees C.
NOVELTY - Gluconobacter oxydans engineering bacteria, is new. The bacteria is introduced into a promoter PtufB and glucose-6-phosphate dehydrogenase gene gox0145 of Gluconobacter oxydans, where the gene gox0145 is located in downstream of the promoter PtufB, which is subject to its regulatory control.    USE - Gluconobacter oxydans is useful in the conversion of D-arabitol for efficient preparation of xylitol (claimed).    ADVANTAGE - Gluconobacter oxydans engineering bacteria allows conversion of D-arabitol to prepare xylitol, which is more than that of an original strain, and ensures the conversion rate of 60-90%. The method is economical, easy to operate, energy saving and environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) constructing Gluconobacter oxydans engineering bacteria, comprising (a) cloning designed primer of promoter PfufB and glucose-6-phosphate dehydrogenase gene gox0145, (b) ligating the sequence of the promoter PtufB to a host expression vector to construct an expression vector with the promoter, (c) ligating the gene gox0145 downstream of the promoter to construct the recombinant expression vector, and (d) transforming the recombinant expression vector obtained in the step (c) into Gluconobacter oxydans to obtain Gluconobacter oxydans engineering bacteria; and (2) use of Gluconobacter oxydans in the conversion of D-arabitol for efficient preparation of xylitol.
NOVELTY - Preparing a base fertilizer comprises taking dry dairy manure, dry pig manure, dry chicken manure, monosodium glutamate leftover, rape straw, peanut straw, alfalfa, water peanut, bean cake, castor seed cake, dried canal mud, organic fertilizer hametz, urea, diammonium phosphate, amino acid chelated iron, amino acid chelated calcium, amino acid chelated magnesium, amino acid chelated selenium, amino acid chelated manganese, amino acid chelated copper and amino acid waste liquid as raw material.    USE - The process is useful for preparing a base fertilizer for Yuanyou pawpaw grown trees (claimed).    ADVANTAGE - The base fertilizer improves disease resistance and drought resistance of the trees.    DETAILED DESCRIPTION - Preparing a base fertilizer comprises taking dry dairy manure (10-12%), dry pig manure (10-12%), dry chicken manure (8%), monosodium glutamate leftover (5%), rape straw (5%), peanut straw (5%), alfalfa (7%), water peanut (5%), bean cake (5%), castor seed cake (5%), dried canal mud (10%), organic fertilizer hametz (2%), urea (4%), diammonium phosphate (3%), amino acid chelated iron (5%), amino acid chelated calcium (6%), amino acid chelated magnesium (0.1%), amino acid chelated selenium (1%), amino acid chelated manganese (2%), amino acid chelated copper (5%) and amino acid waste liquid (8%) as raw material.