NOVELTY - Compound microbial inoculum composed of any three of photosynthetic bacteria, Lactobacillus, Actinomycetes and Bacillus licheniformis, for efficiently processing offshore sewage, is new.    USE - For efficiently processing offshore sewage (claimed).    ADVANTAGE - The compound microbial inoculum efficiently processes offshore sewage, adopts multiple strains combination to treat offshore sewage, avoids halfway processing caused by single strain unresisting high shock load in processing sewage, where the strains are normal ones which is easy in preparation and low in cost; and reduces cost of processing sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing offshore sewage involving: (a) adding clear water and sewage to into a container, followed by adding white sugar, peptone, nitrogen-phosphorus-potassium mixed fertilizer and compound vitamin, and adjusting PH to 7-8; (b) according to total amount of water, adding 8-10% of the compound microbial inoculums; (c) aerating oxygenating for 24-48 hours, to obtain culture solution I; (d) adding the culture solution I into sewage treating pond or offshore sewage, and preserving the culture solution I as inoculant; (e) in the rest of culture solution I, respectively adding clear water and offshore sewage in 4.5 times of culture solution volume, adding white sugar, peptone, nitrogen-phosphorus-potassium mixed fertilizer and compound vitamin, adjusting PH to 7- 8; according to total amount of water, adding compound microbial inoculum, aerating oxygenating to obtain culture solution II; and adding the culture solution II into sewage treating pond or offshore sewage and preserving the culture solution II as inoculant; and (f) according to the method in step (e) continuing culturing for 6 times, adding all the culture solution into sewage treating pond or offshore sewage.
NOVELTY - A fungicide composition comprises heat fiber Clostridium (10-20%) of preservation number ATCC 27405, Desulfotomaculum (5-15%) of preservation number ACCC 00424, thermophilic Bacillus licheniformis (5-35%) of preservation number CCREMSDMCC120012, Butyrivibrio fibrisolvens (5-20%) of preservation number DSM 3071, Bacillus subtilis (25-35%) of preservation number ACCC 01179 and Lactobacillus thermophilus (10-20%) of preservation number ACCCl 1073.    USE - As fungicide composition for decomposing cotton stalk (claimed).    ADVANTAGE - The composition is capable of quickly decomposing the cotton stalk composite microbial inoculum. The culturing process measures cotton amount of decomposition, eliminates decomposition difference, keeps the decomposition of decomposition without phenomenon of vigorous repeated and next successive transfer culture of the strain, circulates successive transfer culture for 30-60 times, until decomposition ability is stable and stable to obtain the composite bacteria system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fungicide composition, involving: 1) preparing the cotton stalk pile fertilizer: (1) crushing the cry cotton stalk into the small section of 1-1.5cm; (2) screening the cotton stalk fast decomposing compound fungicide system; (3) observing the decomposing state each day; (4) repeating the part having stable decomposing stability, using the glycerol for storing or vacuum storing, preparing the cotton stalk fast decomposing fungicide, spraying the cotton stalk powder, pre-fermenting compound bacteria liquid (1-2%) in the fermentation cylinder to heat preservation and culturing at 50-60 degrees C, stirring for 1-2 times each day; and (5) spraying bacterial liquid weight of the polymer which is cotton stalk powder of 10-20%, then spraying immediately drying at 60-70 degrees C, the total water content is 20-25%, to obtain the product and packing.
NOVELTY - Formulation comprises sweet potato, additive A, additive B and stabilizing agent.    USE - The formulation is useful for producing ethanol fuel(claimed).    ADVANTAGE - The formulation: simply produces ethanol fuel with high quality in a cost-effective manner; and improves octane value in an energy saving manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the formulation comprising propagation of sweet potatoes, preparing yeast wine and then stewing to gelatinize, performing diastatic fermentation and then distilling, adding additives, testing and then barreling.
NOVELTY - The method involves injecting biomass into an interior elastic sleeve through biogas fertilizer and organic fertilizer. The sleeve is provided with a pipe to maintain chemical conditions of a fermenter for decomposition of biomass.    USE - Method for manufacturing an interior pipe of a flexible sleeve to inject a biomass into a reactor.
NOVELTY - A composition comprises (in wt.%) anti-foaming agent (0.1), cellulase (1), amylases (1), calcium hypochlorite (1), chlorine (65), sodium persulfate (1) and/or citric acid with pH value of 6-8.    USE - Composition for removing sludge from filter walls of a borehole during water treatment.    ADVANTAGE - The composition effectively removes sludge before surgery cementing casing.
NOVELTY - A hydrogen and biogas producing method involves supplying liquid containing organic fermentation products of hydrogen into a methane fermentation device by diffusion through a semipermeable membrane, and trapping microorganisms, where the installation comprises two portions containing hydrogen fermentation portion and methane fermentation portion.    USE - Method for producing hydrogen and biogas.
NOVELTY - The anaerobic baffled reactor (ABR) has a reactor body whose top and bottom parts are respectively provided with upper and lower baffles. The upper and lower baffles are vertically connected with each other. Two ends of the reactor body are respectively provided with water inlet and outlet pipes. The reactor body is orderly separated into six compartments by the upper and lower baffles along water flow direction. The first compartment is formed as a methane production area. The second compartment is formed as a clear water collecting area and connected with the water outlet pipe.    USE - Separated ABR.    ADVANTAGE - The ABR is simple in structure, inexpensive and small in volume, and has better blocking effect, strong hydraulic power resisting effect and prolonged service life. The ABR avoids hydraulic power loading defects, realizes sludge and water separating process and reduces hydraulic power retention time and sludge and mud production rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a separated ABR working method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a separated ABR.
NOVELTY - Producing ethanol, involves (a) obtaining straw hydrolysate by processing straw, adding water to the processed straw, adjusting the pH value of the processed straw, sterilizing the processed straw, adding cellulase and detoxicant to the processed straw, and (b) adding manganese chloride tetrahydrate, zinc sulfate heptahydrate, inositol and vitamin B1, nickel chloride hexahydrate, cobalt chloride octahydrate and pantothenic acid, to the straw hydrolysate, adding yeast to the mixed solution, and fermenting the solution.    USE - The method is useful for producing ethanol.    DETAILED DESCRIPTION - Method for producing ethanol, involves (a) processing straw at 180-210 degrees C for 4-8 minutes, adding water to the processed straw till the solid content of the processed straw reaches 18-23%, adjusting the pH value of the processed straw to 4.6-5.5, sterilizing the processed straw at 121 degrees C for 20 minutes, adding cellulose and detoxicant to the processed straw, where the ratio of cellulose to processed straw is 0.1:1, and ratio of detoxicant to the processed straw is 0.1:1, saccharifying the processed straw at 50 degrees C and 150 rotations per minute (rpm) for 48 hours to obtain straw hydrolysate, and (b) adding (in mg/l): manganese chloride tetrahydrate (1-25), zinc sulfate heptahydrate (2-10), inositol (50-150) and vitamin B1 (50-150), nickel chloride hexahydrate (10-90 mu m/l), cobalt chloride octahydrate (1-30 mu m/l) and pantothenic acid (1-10 ml/l), to the straw hydrolysate, and adjusting the pH value to 5.0-5.5 to obtain mixed solution, adding yeast to the mixed solution till the concentration of the yeast is 1.5 g/l, and fermenting the solution for 48-72 hours at 32-40 degrees C and 150 rpm.
NOVELTY - The absorber has an absorber body filled with composite aqueous solution that is formed by micro-element copper sulfate, ferrous sulfate, manganese sulfate and zinc sulfate with inorganic acid or organic acid. The inorganic acid is selected from one of sulfuric acid and nitric acid. The organic acid is selected from one of acetic acid, propionic acid, butyric acid, citric acid, malic acid, malonic acid, succinic acid or glutaric acid. The composite aqueous solution is formed by dissolving the copper, ferrous, manganese and zinc sulfates and inorganic acid or organic acid in water.    USE - Absorber for absorbing harmful gas produced by fermenting a material during an organic fertilizer producing process.    ADVANTAGE - The absorber can be filled with composite aqueous solution for absorbing large amount of harmful gas ammonia, hydrogen sulfide, sulfur dioxide and organic gas to be produced during material fermentation process, thus directly producing and utilizing liquid amount, secondary and trace element water-soluble fertilizer as raw material after solution drying process, effectively utilizing large amount of trace and secondary elements without loss and preventing environment from being polluted.
NOVELTY - Tail gas purification fermentation turner comprises a rack, a running gear arranged on left and right sides of the rack, and a turner arranged under the rack. The rack is further provided with a tail gas purification device for collecting, purifying and discharging the tail gas with dust and foul odor produced from fermentation, and turning according to the standards. The tail gas purification device further comprises a tail gas collection mechanism, a dust catcher and/or a deodorizer. The air outlets of the dust catcher and deodorizer are respectively connected with an air hose.    USE - The tail gas purification fermentation turner is useful in production of organic fertilizers.    ADVANTAGE - The tail gas purification fermentation turner: de-dusts, deodorizes and purifies the fermented tail gas during turning of the fermented materials; solves the pollution problem caused by dust and foul odor produced in the process of fermentation of organic raw materials during the production of organic fertilizers, improves production environment for the production of organic fertilizers; and is ecofriendly.
NOVELTY - Producing cellulosic ethanol comprises treating the raw materials by enzymolysis, fermentation, rectification and dehydrating, and treating the waste mash, the gas explosion treatment of the raw material by enzymolysis is as follows: subjecting the cellulose raw material to gas explosion by mixing water vapor with carbon dioxide (CO2) gas, the pressure of the operation pressure gauge is 0.1-2.0 MPa, the operation temperature is 100-240 degrees C, and the mol percent of the CO2 in the mixed steam is 1-60%.    USE - The method is used for producing cellulosic ethanol (claimed).    ADVANTAGE - The method and device are used for easy cellulosic ethanol production with high yield. The method realizes zero discharge of aerobic sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a device for cellulosic ethanol production, comprises enzymolysis unit and stirring tank which are connected with a material inlet of a high-temperature sterilizing device by pipelines; a heating medium inlet of the high-temperature sterilizing device is connected with a high-temperature water vapor pipeline; a hot material outlet of the high-temperature sterilizing device is connected with a material inlet of a heat exchanger by a pipeline; a cold material outlet of the heat exchanger is connected with a material inlet of a centrifugal concentrating device; a supernatant outlet of the centrifugal concentrating device is connected with a cold material inlet pipeline of the heat exchanger by a pipeline; a concentrated solution outlet of the centrifugal concentrating device is connected with a material inlet of an enzymolysis tank by a pipeline; a hot material outlet of the heat exchanger is connected with a mixing water inlet pipeline of the stirring tank by a pipeline; the heat exchanger is a dividing wall type heat exchanger or a completely countercurrent heat exchanger.
NOVELTY - Producing bio-organic fertilizer comprises: (i) pre-fermenting the poultry excrement in a mixed fermentation tank, and adding microbial strains and fermenting, so that the color of material is dark brawn and the smell is compost smell; (ii) mixing the fermented materials with the crushed crop waste; and (iii) turning the materials, crushing and screening, mixing with trace elements, granulating, stoving, cooling, screening and packing.    USE - The method is useful for producing bio-organic fertilizer.    ADVANTAGE - The fertilizer: ensures decomposition and deodorization of solid organic waste into high quality fertilizer; improves seedling disease resistance ability; improves the soil and hence increases the yield and quality of agricultural products; ensures rapid absorption; and is economical and eco-friendly.
NOVELTY - The equipment has a burdening system, a crusher, a double-shaft stirrer and a granulator. The burdening system is connected with the crusher. The double-shaft stirrer is connected in series with the granulator, a drying machine and the screening machine. The screening machine is connected with a low temperature strain loader, a weighing and packaging device and a stacking device. A coal cinder recycling device is connected to the drying machine.    USE - Fertilizer producing equipment.    ADVANTAGE - The fertilizer producing equipment can be achieved with high automation degree and with less environmental pollution. The labor intensity can be reduced and the energy consumption of equipment can be reduced at low production cost.
NOVELTY - Anti-soil acidification organic fertilizer additive comprises functional microbial fungicide composition, amino acid and humic acid powder. The additive further comprises zeolite powder, shell powder, silico-calcium powder and/or fused calcium magnesium phosphate.    USE - Used as an anti-soil acidification organic fertilizer additive.    ADVANTAGE - The organic fertilizer additive: improves the physical fertility, biological fertility and chemical fertility of the acidic soil; enhances the resistance to soil acidification; is safe to use; and can solve the threat of the acidity or acidic soil on agriculture production, environment and human health from food chain to the nutritionist point of view.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the anti-soil acidification organic fertilizer additive, comprising: (i) preparing the functional microbial fungicide composition and the amino acid solution; (ii) processing the obtain solution by spray drying embedding technology to the obtain a fungicide microcapsule; (iii) mixing the humic acid powder, zeolite powder, shell powder, silico-calcium powder and fused calcium magnesium phosphate to obtain mixed material; (iv) turning, heaping and curing the mixed material, drying and scattering to obtain powder mixture; and (v) blending the fungicide microcapsule and the powder mixture to obtain the anti-soil acidification organic fertilizer additive.
NOVELTY - Dissolving plant straw to produce cellulosic ethanol fuel, comprises taking organic acid or mixed acid of more than two organic acids as solvent, heating the acid mixture and then introducing in a reactor, adding plant straw into the reactor, hydrolyzing the mixture, eluting the hydrolyzate with solvent to obtain cellulose, distilling and rectifying the eluent to obtain furfural and lignin, degrading cellulose sugar to obtain cellulose and hemicellulose and then performing alcoholic fermentation process, and performing distillation of fermented mixture.    USE - The method is useful for dissolving plant straw to produce cellulosic ethanol fuel.    ADVANTAGE - The method is capable of simply dissolving the plant straw thus economically producing the cellulosic ethanol fuel with high yield.    DETAILED DESCRIPTION - Dissolving plant straw to produce cellulosic ethanol fuel, comprises taking organic acid or mixed acid of more than two organic acids as solvent, heating the acid mixture at 60-160 degrees C and then introducing in a hydrolysis reactor, adding plant straw into the hydrolysis reactor, where the mass ratio of straw and solvent is 1:4-1:6, hydrolyzing the mixture at 90 degrees C for 10 minutes and then maintaining the hydrolysis temperature to 60-160 degrees C in the reactor, eluting the hydrolyzate with solvent to obtain cellulose, distilling and rectifying the eluent to obtain furfural and lignin, degrading cellulose sugar to obtain cellulose and hemicellulose and then performing alcoholic fermentation process, and performing distillation of fermented mixture to obtain cellulose fuel ethanol.
NOVELTY - A device for processing garbage, comprises a temperature-keeping tank storing fermentation material liquid; a heat preservation tank provided with a feeding port at the upper part, a discharging port and a slag discharging port at the lower part; a stirring unit connected with the heat preservation tank to stir the fermentation material; a solar heat collector installed on the top of the tank; and a heating component connected with the temperature-keeping tank and the solar heat collector to heat the fermentation material liquid.    USE - The device is used for processing garbage (claimed).    ADVANTAGE - The device greatly reduces the biological anaerobic digestion needed energy consumption. The device is used for low-cost garbage processing.
NOVELTY - A nutrient organic flower fertilizer comprises rice water (2.7-2.8 kg), vegetable (0.8-1 kg), dry leaf (0.8-1 kg), egg shell (55-60 g), bean dregs (280-300 g), and fish viscera (220-240 g).    USE - Nutrient organic flower fertilizer.    ADVANTAGE - Raw material is domestic waste which is converted into useful product. It does not only reduce pollution, but also avoids hardening of soil.
NOVELTY - Invention relates to treatment of oil-bearing waters, in particular, industrial effluents, etc. Proposed device comprises catalytic chamber filled with catalyst, flotation chamber divided by horizontal diaphragm into cathode and anode chambers. Note here that said diaphragm is arranged between anode and cathode. It includes also branch pipe to feed cleaned water into anode chamber, branch pipes to discharge hydrogen gas and oxygen, anode made up of graphite plate arranged on anode chamber bottom. Besides, it comprises cathode composed of separate elements arranged parallel with anode. Used catalyst represents granular material with grain size of 2-5 mm of the following composition: iron - 38%, sulfur - 36%, liquid glass and sodium fluorosilicate making the rest. Said diaphragm is made from kapron fabric. Cathode is made of rectangular plates from carbon-bearing bulk. Said bulk accommodates electric contacts made up of copper screen connected to external current lead. Note here that said plate has through water passages. Note also that carbon-bearing bulk consists of 30-40 wt % of petroleum pitch, oil coke making the rest.    USE - Process engineering.    ADVANTAGE - Higher efficiency due to higher rate of bubbling. 4 dwg, 1 ex
NOVELTY - The tank has main portions in which opening portions are formed. The grating portions are inserted in the opening portions of the main portions. The nylon ropes are knotted on a cover of the main portions. A loading board is stretched toward the lower end of the main portion. The opening portions of main portion are covered by a plastic house. The upper end of main portion is connected with a pressure gage and a switch through a methane pipeline.    USE - Straw methane tank.    ADVANTAGE - The operating efficiency of straw methane tank can be improved effectively.
NOVELTY - Method for pre-processing straw raw material, involves crushing the straw raw material, adding crushed straw raw material to pre-processing reactor, adding volatile fatty acids or organic wastewater containing volatile fatty acids to the crushed straw raw material in a dry weight/mass ratio of 1:4-15, adding water to the reactor for adjusting mass concentration of dry straw raw material to 8-15%, stirring and uniformly mixing mixture, sealing the reactor after performing heat treatment at 80-160 degrees C for 0.5-5 hours to obtain pre-processed straw raw material.    USE - The method is useful for pre-processing straw chosen from haulm, wheat straw, corn stalks, rice grass, Chinese Pennisetum, or elephant grass, used as raw material in fermentation process for production of biogas.    ADVANTAGE - The method enables avoidance of corrosion of the reactor and pipeline, and solubility loss of organic material. The method enables reduction in mass accumulation of alkali metal, hence anaerobic fermentation inhibition and environment pollution are also avoided, thus subsequent use of biogas slag is enabled and pre-processing cost during biogas production is also reduced.
NOVELTY - Preparing sodium periodate, comprises mixing sodium chlorate with iodine and water, adjusting a pH value of mixed solution, and heating the mixed solution, adding sodium hydroxide solution into a mixed solution of sodium iodate and sodium chloride, measuring the pH value of the solution, controlling the pH value of the mixed solution and cooling, dehydrating and separating a sodium iodate crystal, and adding the sodium iodate and sodium persulfate with the sodium hydroxide solution, heating and cooling the mixed solution, and layering the cooled solution.    USE - The method is useful for sodium periodate, which is useful as oxidant, chromatographic analytical reagent, healthcare product and medical intermediate.    ADVANTAGE - The method provides sodium periodate with high production safety and reduced raw material consumption in an environment friendly-manner.    DETAILED DESCRIPTION - Preparing sodium periodate, comprises: (a) mixing sodium chlorate with iodine and water, adjusting a pH value of the mixed solution using concentrated nitric acid until the pH value reaches less than or equal to 1, where the mole ratio of the sodium chlorate to the iodine to the water is 11:6:3, heating the mixed solution for 0.5-1 hour, and absorbing the generated chlorine using alkali liquor to obtain sodium iodate and sodium chloride; (b) adding sodium hydroxide solution into the mixed solution of sodium iodate and sodium chloride, measuring the pH value of the solution, controlling the pH value of the mixed solution to greater than or equal to 7, cooling the mixed solution to 40 degrees C to obtain a sodium iodate crystal, and centrifugally dehydrating and separating the sodium iodate crystal to obtain sodium iodate; and (c) adding the sodium iodate and sodium persulfate with the sodium hydroxide solution, heating the mixed solution, and cooling mixed solution with water, and standing and layering the cooled solution to obtain finished product.
NOVELTY - Organic selenium-rich fertilizer is prepared by adding animal waste, vegetable residue and rapeseed cake into fermenting vat, adding water to the raw materials, covering and fermenting the materials until slight stink is produced, continuously adding water to the fermentation vat, fermenting the materials for 20-40 days or more till the solid materials are dissolved, filtering fermentation broth and obtaining mother liquor, adding sodium selenate into mother liquor, uniformly stirring and dissolving sodium selenate in the liquor, and packing organic fertilizer.    USE - As organic selenium-rich fertilizer.    ADVANTAGE - The fertilizer has selenium content of 25-35 g/l, produces agricultural products with high selenium content, and improves selenium level in selenium deficient regions.    DETAILED DESCRIPTION - Organic selenium-rich fertilizer is prepared by adding animal waste, vegetable residue and rapeseed cake into a fermenting vat, adding water to the raw materials, covering and fermenting the materials for 40-50 days until slight stink is produced, continuously adding water to the fermentation vat, fermenting the materials for 20-40 days or more till the solid materials are dissolved, filtering fermentation broth using a sieve having 100-200 meshes and obtaining mother liquor, adding 3-5 kg sodium selenate/100 kg of mother liquor, uniformly stirring and dissolving sodium selenate in the liquor, and packing the organic fertilizer.
NOVELTY - Synthesis of chiral 2,3-pinanediol (I) or (II) comprises adding alpha -pinene and peroxidation inhibitor to a solvent comprising water and alcohols, reacting at 10-40 degrees C, dropwise adding a strong base solution containing oxidant having a pH value of 11-14, heat preserving for 2-10 hours, adding a reducing agent to stop the reaction, separating, extracting, and concentrating.    USE - Method for the synthesis of chiral 2,3-pinanediol including sinistrogyration alpha -pinene or dextrorotation alpha -pinene (claimed) used as an intermediate for synthesis of protease inhibitor and anticancer drugs.    ADVANTAGE - The method achieves high liquid phase purity and stable chiral 2,3-pinanediol. It is inexpensive, has mild reaction condition, simple operation, and is environment-friendly. The yield is 60.7-76.6%, and has a purity of 98%.    DETAILED DESCRIPTION - Synthesis of chiral 2,3-pinanediol of formula (I) or (II) comprises adding alpha -pinene and peroxidation inhibitor to a solvent containing water and alcohols, reacting at 10-40 degrees C, dropwise adding a strong base solution containing oxidant at a pH value of 11-14, heat preserving for 2-10 hours, adding a reducing agent to stop the reaction, separating, extracting, and concentrating. The dosage ratio of the alpha -pinene and water is 1g/0.5-5 mL. The dosage ratio of the alpha -pinene and the alcohol solvent is 1g/3-20 mL. The mole ratio of the alpha -pinene and the peroxidation inhibitor is 1:0.5-3. The mole ratio of the alpha -pinene and the oxidant is 1:1-10. The mole ratio of alpha -pinene and the strong base is 1:0.1-2. The mole ratio of alpha -pinene and the reducing agent is 1:5-20.
NOVELTY - Preparation of a bromobenzyl compound (I) comprises reacting a benzene compound (II) and N-bromosuccinimide in water as solvent.    USE - Method for the preparation of a bromobenzyl compound (I) (claimed) used as an intermediate for organic synthesis; and used as raw material for medicine, pesticide, dye, and auxiliary chemicals.    ADVANTAGE - The method is simple, is inexpensive, has short reaction time, has mild reaction condition, is easy to control, has high product yield, has low energy consumption, and is environment-friendly.    DETAILED DESCRIPTION - Preparation of a bromobenzyl compound of formula (I) comprises reacting a benzene compound of formula (II) and N-bromosuccinimide in water as solvent.    R1, R2=H, CH3CO, tertbutyl, NHOCCH3, 1-4C alkoxy, or CN.    An INDEPENDENT CLAIM is included for a system for carrying out the preparation of (I).    DESCRIPTION OF DRAWING(S) - The drawing is a diagram of the system.    Temperature measuring device (1)    Charging device (2)    Temperature controlling device (3)    Ball valve (4)    Transparent pipe (5)    High power floodlight (6)    Circulating pump (7)
NOVELTY - Method for preparing high-purity baicalin involves (a) adding water to Scutellaria baicalensis, heating and extracting the mixture and obtaining extract, (b) directly absorbing the extract using macroporous resin, removing impurities by elution using ethanol-water mixture (0-30%), and continuing the elution process using ethanol-water mixture (40-60%), (c) collecting eluent and concentrating the obtained eluent, and (d) freeze drying and recrystallizing the concentrated eluent.    USE - The method is useful for preparing high-purity baicalin.    ADVANTAGE - The method enables to prepare baicalin of high purity (98%). The method is simple, cost-effective and environmentally friendly and carried out at mild condition.
NOVELTY - Continuous separation of triglyceride and free fatty acid from any mixture of triglyceride and free fatty acid included in crude vegetable oil, acid oil, animal grease, circulating vegetable oil, and palm oil fatty acid, comprises contacting the mixture with fatty solvent with low boiling point and water under vigorous stirring.    USE - The method is for continuous separation of triglyceride and free fatty acid from any mixture of triglyceride and free fatty acid included in crude vegetable oil, acid oil, animal grease, circulating vegetable oil, and palm oil fatty acid. It is useful for continuous esterification of triglyceride and free fatty acid (claimed) to obtain fatty acid methyl ester or ethyl ester for use as fuel for power generation and automobile in countries in the frigid zone and temperate zone.    ADVANTAGE - The ester is moderately dehydrogenated, so that the pour point of methyl ester and ethyl ester is reduced to lowest.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous esterification of triglyceride and free fatty acid from the mixture of triglyceride and free fatty acid treated by continuous separation method, comprising supplying a mixture of oil/grease and free fatty acid and 20-50 wt.% methanol into a fluidized bed reactor of reaction container, where solid catalyst for the reaction flows through methanol steam and is kept in a reaction medium by suspension; taking methanol steam from gas phase at the top of the reaction container and compressing into the container by a distributor at the lower part of the reactor, where catalyst is solid strong acid exchange resin and is limited in the liquid phase zone of the reactor between two separation sieves to allow the liquid and gas to flow in and out, and the catalyst is not allowed to be taken from the liquid phase region, and where the flow of the reactant and the volume of the reactor are designed, so that the retention time is 0.5-1.5 hours.
NOVELTY - Preparing alkali bentonite catalyst, comprises (i) mixing activated white clay with 8-20 times of water, adding activated white clay under 3-10% calcium hydroxide, stirring, and filtering to obtain a wet load of calcium hydroxide and activated white clay, and (ii) mixing wet load of calcium hydroxide and activated white clay with water, adding activated white clay into 20-80% sodium hydroxide, stirring, filtering, and drying, where the catalyst utilizes activated white clay as a carrier and calcium hydroxide and sodium hydroxide as active components.    USE - The catalyst is useful for synthesizing biodiesel.    ADVANTAGE - The catalyst has high activity and oil methyl esterification conversion rate of 95-97% under atmospheric pressure; and does not contain fatty acid monoglyceride and diglyceride. The method is economical and ensures a simple product separation and purification process, and utilizes the carrier and the active components, which are economical.    DETAILED DESCRIPTION - Preparing alkali bentonite catalyst, comprises (i) mixing activated white clay having a particle size of 100-300 with 8-20 times of water, adding activated white clay 3-10% the mass of calcium hydroxide, stirring for 2-6 hours, and filtering to obtain a wet load of calcium hydroxide and activated white clay, and (ii) mixing wet load of calcium hydroxide and activated white clay with 1-4 times of water, adding activated white clay 20-80% the mass of sodium hydroxide, stirring at 60-90 degrees C for 1-4 hours, filtering, and drying at 150-250 degrees C, where the catalyst utilizes activated white clay as a carrier and calcium hydroxide and sodium hydroxide as active components, which are loaded in the catalyst using wet load method.
NOVELTY - A halophenyl-2-(2-thienyl ethylamino) acetate (I) is prepared by performing substitution reaction between halogenated phenylglycine ester and 2-halo-ethylthiophene or 2-(2-thiophene) ethanol, or between 2-thiophene ethylamine and alpha -haloalkyl aryl acetate or alpha -hydroxy aryl acetate, in alcohol solvent and in presence of inorganic or organic alkali as acid binding agent.    USE - Method of preparing halophenyl-2-(2-thienyl ethylamino) acetate or its salt (claimed).    ADVANTAGE - The method involves mild reaction condition, and utilizes solvent which is low cost, environment-friendly and easy to recycle and purify, and has low toxicity. Further, the method is suitable for large scale industrial production and can be basis for industrial production of clopidogrel or its salt.    DETAILED DESCRIPTION - A halophenyl-2-(2-thienyl ethylamino) acetate of formula (I) or its salt is prepared by performing substitution reaction between halogenated phenylglycine ester of formula (II) and 2-amino-2-phenylacetic acid compound of formula (III) or between 2-(2-thiophenyl)ethylamine and 2-phenylacetic acid compound of formula (IV) in alcohol solvent and in presence of inorganic or organic alkali as acid binding agent.    X = Cl, Br, I. OCH2SO3H, OSO2Ph or OTs, and    Y' = Cl, Br or I.    N.B. Definitions are from dependent claims.
NOVELTY - The method involves performing a deoxidizing treatment on coal mine gas. Chemical absorbents in the gas concentration are removed. A three tower deep dehydration process is utilized for a deep dehydration drying function. A full-sulfur containing active carbon tower is utilized to remove mercury from coal mine gas. A low temperature liquefaction working procedure is adopted for performing double-stage mixed refrigerant liquefied circulation. A low temperature rectification process is performed by an internal winding type re-stage rectification tower structure.    USE - Method for purifying, separating and liquefying nitrogen coal gas that contains nitrogen and oxygen.    ADVANTAGE - The method enables recycling coal mine gas i.e. liquefied natural gas, in a large scale and avoiding accident and environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a purifying, separating and liquefying system for nitrogen coal gas that contains nitrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a liquefying nitrogen coal gas purifying, separating and liquefying system.'(Drawing includes non-English language text)'
NOVELTY - The device has a water tank which is connected with a water inlet pipe (6). A water outlet pipe valve (5) is connected with water outlet pipe (4) and water inlet pipe (8). The water inlet pipe is provided on water inlet of water tank temperature sensor (10). A water inlet pipe electromagnetic valve (9) is covered in hydrogen water tank (14) of heater (13). An electronic control unit by a shielding cable is connected with water inlet of water tank temperature sensor.    USE - Device for heating de-ionized water in hydrogen production machine for internal combustion engine of vehicle.    ADVANTAGE - The device is utilized to heat the de-ionized water by using cooling energy, so as to increase the load of internal combustion engine, and to prevent the de-ionized water freezing in the low temperature environment in vehicle hydrogen production machine water tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for heating de-ionized water in hydrogen production machine for internal combustion engine of vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for heating de-ionized water in hydrogen production machine for internal combustion engine of vehicle.    Water outlet pipe (4)    Water outlet pipe valve (5)    Water inlet pipe (6)    Water inlet pipe (8)    Water inlet pipe electromagnetic valve (9)    Water tank temperature sensor (10)    Heater (13)    Hydrogen water tank (14)
NOVELTY - The method involves rectifying a tower bottom liquid product through a reducing valve (V-101) and a guiding methane-nitrogen rectifying tower (T-102). A tower bottom methane product is obtained by the rectifying tower, a nitrogen-enriched tower top condenser (E-105), an over-cooler (E-202) and a raw material gas cooler (E-201). The methane product is cooled by the raw material gas cooler. Pressure in a gas storage tank is adjusted to desired pressure by a decompressing valve (V-103). 5 to 15 percent of methane gas is utilized in a double-stage nitrogen expansion refrigeration cycle.    USE - Coke-oven liquefied natural gas cryogenic separating method.    ADVANTAGE - The method enables performing coke-oven liquefied natural gas cryogenic separating operation with low cost, stable and simple operations and high natural gas recovery rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a coke-oven liquefied natural gas cryogenic separating method.'(Drawing includes non-English language text)'    Nitrogen-enriched tower top condenser (E-105)    Raw material gas cooler (E-201)    Over-cooler (E-202)    Guiding methane-nitrogen rectifying tower (T-102)    Reducing valve (V-101)    Decompressing valve (V-103)
(CZ201100422-A3)   NOVELTY - The method involves subjecting waste material to alkaline hydrolysis process by action of an organic base or a mixture of organic bases. The fractions of liquid proteinaceous hydrolyzate and refined fat or oil are mutually separated from a resultant product. Amine is used as the organic base or mixture of organic bases, where the amine is selected from a group consisting of isopropylamine, diisopropylamine, butylamine, cyclohexylamine and tetramethyl-ammonium hydroxide. The alkaline hydrolysis process is carried out by using a proteolytic enzyme.    USE - Method for deproteinization of waste of leather, meat and food for manufacturing biostimulators and biofuel.
NOVELTY - The air cleaner (100) has frame (10) to which front panel (20) is fixed by a support (30) positioned facing another support (32). The electrode portion (50) connects the supports, and electrode connection portion (40) connects electrodes in the supports. A plasma generator (70) supplies power to front panel and electrode portion, and releases plasma for purifying the neighboring air.    USE - Air cleaner.    ADVANTAGE - The air purifying efficiency can be improved. The structure of the air cleaner can be simplified. The cost of the air cleaner can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the air cleaner.    Frame (10)    Front panel (20)    Supports (30,32)    Electrode connection portion (40)    Electrode portion (50)    Plasma generator (70)    Air cleaner (100)
NOVELTY - The device has converter head, converter tail, converter transmission motor, trolley base frame and trolley device which are orderly arranged on base through pre-buried bolt. The washing tower is connected with tail gas fan provided with discharge chimney. The converter furnace is connected with end of biodiesel recovery device through pipeline. The other end of biodiesel recovery device is connected with afterheat boiler. The bottom portion of biodiesel recovery device is connected with biodiesel storage tank through liquid sealing pipe.    USE - Device for carbonizing active carbon carbide material, baking wet active carbon, regenerating powder active carbon and recovering biodiesel.    ADVANTAGE - The automatic control in the operation process can be realized in biodiesel recovering process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of device for carbonizing active carbon carbide material, baking wet active carbon, regenerating powder active carbon and recovering biodiesel. The device has converter head that is connected with biodiesel recovery device connected with afterheat boiler. The feeding screw is arranged inside converter head and provided with material feeding inlet. The converter transmission motor is connected with converter cylinder. The converter centre pipe is arranged inside thermocouple temperature measuring device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for carbonizing active carbon carbide material, baking wet active carbon, regenerating powder active carbon and recovering biodiesel.
NOVELTY - Processing glycerol salt-containing wastewater comprises adding 1.3-3.3 times n-butanol to glycerol salt-containing wastewater; recovering salt crystal in salt-containing glycerol in wastewater at normal pressure and 30-70 degrees C; dividing into upper liquid phase containing organic phase of 0.3% salt, and lower layer water phase; in upper layer of organic phase, recycling n-butanol and removing water, and obtaining 99.9% pure glycerin product; and in lower layer water phase filter, introducing filtrate to extraction tower and processing sodium chloride, and washing recovered crystal.    USE - Method for processing glycerol salt-containing wastewater (claimed) for wastewater treatment of epoxy resin production glycerol product, oil chemical production glycerol by-product and producing biodiesel by-product glycerin.    ADVANTAGE - The method has simple technique, and easy operation and control. It is environmental friendly. Glycerol and sodium chloride in wastewater can be recycled, thus reducing production cost.    DETAILED DESCRIPTION - Processing glycerol salt-containing wastewater comprises adding 1.3-3.3 times n-butanol to glycerol salt-containing wastewater; recovering salt crystal in salt-containing glycerol in wastewater at normal pressure and 30-70 degrees C; dividing into upper liquid phase containing organic phase of 0.3% salt, and lower layer water phase; in upper layer of organic phase, recycling n-butanol, at the same time removing water, and obtaining 99.9% pure glycerin product; and in lower layer water phase filter, introducing filtrate to extraction tower and processing sodium chloride, and washing recovered crystal.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a method for processing glycerol salt-containing wastewater.    Second distillation tower (C2)    Third distillation tower (C3)    Settling tank (D1)    Fourth pre-heater (H5)    First mixer (M2)
NOVELTY - High power off-grid wind power generator comprises an off-grid wind power generator (1) connected with a transformer (2) which is respectively connected with a rectifier (3), a gas generator (6) and a plant. The rectifier is connected with a hydrogen production unit (4) for producing hydrogen by electrolysis of water. The hydrogen production unit is connected with a controller. The controller is respectively connected with the off-grid wind power generator and a fuel gas generator, and the fuel gas generator is connected with the plant.    USE - Used as the high power off-grid wind power generator.    ADVANTAGE - The high power off-grid wind power generator: exhibits improved utilization rate of wind energy; avoids dependence on the power grid; and is cost-effective and efficient.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the high power off-grid wind power generator.    Off-grid wind power generator (1)    Transformer (2)    Rectifier (3)    Hydrogen production unit (4)    Gas generator (5)
NOVELTY - Preparing straw carbon includes preparing ingredients including coal, straw and flame retardant; crushing; pre-profiling; heating for the first time; further crushing and heating; activating; cooling; screening and packaging.    USE - Method for preparing straw carbon (claimed).    ADVANTAGE - The method prevents excessive carbonation and increases carbon density, is environment-friendly, and conserves resources. The straw carbon has smooth surface and uniform carbonation, and is not easy to break.    DETAILED DESCRIPTION - Preparing straw carbon comprises:    (A) preparing the ingredients including (pts.wt.) coal (3-5), straw (95-97) and flame retardant (0.1-0.5);    (B) crushing the straw, coal and flame retardant;    (C) drying the crushed straw powder into the dryer to ensure that the moisture content of straw is less than 20%;    (D) taking the dried straw out, mixing it with the pulverized coal uniformly to obtain the mixed powder;    (E) adding the mixed powder into a compacting shape machine for compression forming to obtain the particles with the diameter of 6-15 mm and length of 20-50 mm;    (F) heating the obtained particles for the first time at 150-200 degrees C for 20-60 minutes;    (G) cooling the particles, and crushing the particles again to obtain powder;    (H) adding the flame retardant of the weight ratio and the right amount of water to the powder to ensure that the moisture content of the powder is less than 20%;    (I) adding the mixed powder into the compacting shape machine for compression forming to obtain the particles with the diameter of 6-10 mm and length of 20-30 mm;    (J) heating the obtained particles again at 400-700 degrees C for 60-120 minutes;    (K) activating the particles obtained in the previous step at 850-950 degrees C; and    (L) cooling and screening the particles, and packaging the particles.
NOVELTY - The vehicle has a driving motor electrically connected with a hydrogen generator that is provided with a liquid storage chamber, a reactor, a gas-liquid separating device, a drying chamber and a waste liquid collection chamber. The reactor is made of PTFE. An end of the reactor is connected with a pipeline provided with a pump. A bottom part of the reactor is fixed to the drying chamber. A lower end of a waste liquid pipeline is provided with a filtering device. The drying chamber is arranged with a drying agent. The pipeline supplies hydrogen to a fuel cell.    USE - Hydrogen fuel battery electric vehicle.    ADVANTAGE - The vehicle utilizes the hydrogen fuel cell as power supply, and the final product is water, so that pollution to environment is reduced. The vehicle enables recycling the dirty oil and waste liquor for further use so as to save cost.    DETAILED DESCRIPTION - The filtering device is a net shaped or foam filter board.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a hydrogen fuel battery electric vehicle.
NOVELTY - A sludge synthesized fuel is prepared by taking dehydrated sludge in urban sewage treatment plants, and sending to high-speed stirrer; sending the quickly stirred sludge to a mixing stirrer, adding 5-20% of sludge drying agent and 1-5% of calcium oxide, completely stirring for 5-15 minutes, and preparing semi-finished sludge product; and sending the semi-finished sludge product to a stirrer with ultralow speed, adding 30-50% of coal powder, stirring for 10-20 minutes to prepare small particles, and sending the sludge without forming the small particles to a granulator to granulate.    USE - Method for preparation of sludge synthesized fuel (claimed).    ADVANTAGE - The method is capable of preparing sludge synthesized fuel with low energy consumption, is low in cost and is high in efficiency.    DETAILED DESCRIPTION - Preparation of sludge synthesized fuel comprises:    (A) taking dehydrated sludge in urban sewage treatment plants, and sending to high-speed stirrer to quickly stir for 1-10 minutes;    (B) sending the quickly stirred sludge to a mixing stirrer, adding 5-20% of sludge drying agent and 1-5% of calcium oxide, completely stirring for 5-15 minutes, and preparing semi-finished sludge product;    (C) sending the semi-finished sludge product to a stirrer with ultralow speed, adding 30-50% of coal powder, stirring for 10-20 minutes to prepare small particles, and sending the sludge without forming the small particles to a granulator to granulate; and    (D) placing the small particles and the small particles granulated by the granulator in a place with good ventilation, drying, and obtaining the sludge synthesized fuel.    The sludge drying agent is magnesium oxide, calcium sulfate, and ferric sulfate at a mass ratio of 3-5:2-5:1-3.
NOVELTY - Preparation of biodiesel alkaline ionic liquid comprises pre-heating castor oil to certain temperature; adding purified and dried alkaline ionic liquid and carbinol into three-opening flask; dissolving catalytic agent into reaction system; refluxing for certain period while magnetically stirring; quickly cooling at room temperature; transferring funnel to heat and layer; and carrying out gas chromatography to upper product.    USE - Preparation of biodiesel alkaline ionic liquid.    ADVANTAGE - The binuclear alkaline ionic liquid has strong basicity and good catalytic properties, thus catalysis and solvent action are integrated during reaction process. It solves problem of existing solid base catalyst that cannot be recycled. It has superior catalytic property than uninuclear alkaline ionic liquid, has low production cost, high yield, and can be recycled repeatedly to reduce cost of industrial production of biodiesel. The production process is simple and clean, and provides fatty acid methyl ester yield that can reach over 98% through experiment.
NOVELTY - Method (M1) for improving storage stability with respect to commercialized pellet, involves adding vegetable oil or ozonated vegetable oil to wood flour, and molding the mixture by pellet molder.    USE - The method is useful for improving storage stability with respect to commercialized pellet.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) pellet composition comprising vegetable oil or ozone-treated vegetable oil; and    (2) method (M2) for reducing high pressure loaded in the apparatus for preparing pellet.
NOVELTY - The method involves forming (S100) a supporter cathode sheet, a hydrogen activity firing zone depth sheet, a cathode functional layer sheet and an electrolyte film sheet using a tape casting. A stack of electrolyte film sheet is laminated (S200). The stack is pressurized and a green body is formed (S300). A buffer layer sheet is sintered (S400), where an anode is formed (S500) on the electrolyte film.    USE - Method for manufacturing a unit cell for a fuel cell (Claimed).    ADVANTAGE - The method involves forming a supporter cathode, a hydrogen activity firing zone depth, and a cathode functional layer, where electrolyte film is sintered in a green body, and hence ensures that the power density of a cell is improved by the increase of the fuel oxidation reaction velocity.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a unit cell manufacturing method. (Drawing includes non-English language text).    Forming a supporter cathode sheet, a hydrogen activity firing zone depth sheet, a cathode functional layer sheet and an electrolyte film sheet using a tape casting (S100)    Laminating a stack of electrolyte film sheet (S200)    Forming a green body and pressurizing the stack (S300)    Sintering a buffer layer sheet (S400)    Forming an anode on electrolyte sheet (S500)
NOVELTY - The purifying device is provided with electrolysis device (4). The electricity generated from driving of diesel engine (3) is replenished, so as to utilize as reducing agent of catalyst by supplying to the front end of the nitrogen oxide reduction catalyst (1). The hydrogen and oxygen are generated to the electrolysis reaction of water. The electrolysis device is connected to the storage battery (7) and is driven to the electricity of storage battery.    USE - Exhaust gas purifying device used for diesel engine (claimed) used in vehicle, ship, and industry.    ADVANTAGE - Since the electrolysis device is connected to the storage battery and is driven to the electricity of storage battery, the deterioration of the fuel efficiency can be prevented. Thus the working efficiency of the diesel engine can be improved without consuming more electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the exhaust gas purification device.    Nitrogen oxide reduction catalyst (1)    Diesel engine (3)    Electrolysis device (4)    Water tank (5)    Storage battery (7)
NOVELTY - An electrode catalyst layer comprises a carbon-supported platinum catalyst, and a water electrolysis catalyst capable of decomposing water inserted to the catalyst layer when the voltage of more than 1.4V is applied.    USE - Electrode catalyst layer is used for membrane-electrode assembly for fuel cell.    ADVANTAGE - The electrode catalyst layer prevents corrosion of carbon.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) film; and    (2) formation of film.
NOVELTY - The method involves separating the crude glycerine and biodiesel. The glycerine and fatty acid are separated from crude glycerine and biodiesel. The glycerine and mono-glyceride are hydrolyzed. The condensed water is removed.    USE - Method for generating glycerine.    ADVANTAGE - High purity glycerin can be manufactured without discharge of effulent, and the fabrication cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process for generating glycerine.
NOVELTY - The method involves separating biomass derived carbon dioxide and oxygen from a decarburization device by an air separation equipment. A gasification device is connected with a gasification medium, which generates crude synthetic gas dedusted by a purifying device from a feed system of raw material. The crude synthetic gas is mixed in saturated steam generated from a boiler by a raw synthesis gas conversion device. The synthesis gas is removed from a synthesis system of carbon dioxide, and the part or whole part of carbon dioxide mixed with the oxygen is separated into the gasification device.    USE - Method for preparing synthesis gas.    ADVANTAGE - The method enables improving biomass energy conversion efficiency and ensuring the synthesis gas to directly reach quality standard.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a synthesis gas preparing method. '(Drawing includes non-English language text)'
NOVELTY - The method involves placing wheat straw rod particles in a roller extruder, crushing by a roller extruder and sending the particles via a through hole of a circular plate to form compressed volume. The particles are passed through a series of roller wheels to form post wheat straw particle fuel. The post wheat straw particle fuel is continuously or intermittently injected in a fuel gas-generating stove. Air and steam are synchronously blown as a gasification agent in a gas generating furnace by the fuel gas-generating stove to keep temperature at 300-600 degree Celsius.    USE - Method for generating fuel gas by using wheat straw rod particles.    ADVANTAGE - The method enables adopting wheat straw rod particles as fuel, so as to replace block coal or coke, which ensures the cleanliness of the fuel gas, realizes high heat value, and directly pushes into gas turbine operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel gas generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fuel gas generating device.    Through hole (7)    Transmission shaft (8)    Idler wheel (9)    Material barrel (10)    Bevel gear (63)
NOVELTY - The furnace has a dust removing pool (1) filled with water. A lower furnace body (43) is provided with an ash hopper (42) that is formed with an ash discharge port (2). A lower part of the ash discharge port is formed with an ash outlet (46). An auger ash outlet machine (45) is formed with another ash outlet (47). A middle furnace body (32) and an upper furnace body (27) are respectively provided with a lower furnace body flange (16) and an upper furnace body flange (17). The upper furnace body is provided with a furnace shell (19) that is arranged in an inner furnace body (20).    USE - Biomass gas gasification furnace.    ADVANTAGE - The furnace is simple and reasonable in structural design, and has high stability, and improves production efficiency and realizes continuous gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas gasification furnace.    Dust removing pool (1)    Ash discharge port (2)    Lower furnace body flange (16)    Upper furnace body flange (17)    Furnace shell (19)    Inner furnace body (20)    Upper furnace body (27)    Middle furnace body (32)    Ash hopper (42)    Lower furnace body (43)    Auger ash outlet machine (45)    Ash outlets (46, 47)
NOVELTY - The separator has a sewage pipe (25) provided with a water inlet pipe joint (27). The water inlet pipe joint is placed at a lower part of a cylinder body (9). A drain pipe (2) is placed at a bottom end enclosure (3) and welded with a supporting frame (28). A middle umbrella cap (7) is welded on a draft tube (22) provided with a rectifying cover (21). A cylinder flange (16) is provided with a sealing flange (15). The sealing flange is welded on an upper part cover (12). The upper part cover is welded with an air outlet pipe (13). The air outlet pipe is welded with an air outlet flange (14).    USE - Biomass fuel gas oil-gas separator.    ADVANTAGE - The separator has simple structure and better purification effect, is easy to assemble and stable to operate, and reduces cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a biomass fuel gas oil-gas separator.    Drain pipe (2)    Bottom end enclosure (3)    Middle umbrella cap (7)    Cylinder body (9)    Upper part cover (12)    Air outlet pipe (13)    Air outlet flange (14)    Sealing flange (15)    Cylinder flange (16)    Rectifying cover (21)    Draft tube (22)    Sewage pipe (25)    Water inlet pipe joint (27)    Supporting frame (28)
NOVELTY - Performing dry distillation gasification of solid biomass comprises: (a) mixing solid biomass with high temperature flue gas containing carbon particles, and drying; and (b) respectively collecting the dry distillation gas and biological coke obtained by dry distillation.    USE - The method is useful for performing dry distillation gasification of solid biomass.    ADVANTAGE - The method utilizes carbon particles of heat radiation and conduction effect and hence ensures rapid physical and chemical changes in solid biomass and its decomposition into biological coke and dry distillation gas, has short processing time, produces product with high yield, and completely utilizes the raw materials.
NOVELTY - A biomass formed fuel production raw material water content monitoring and adjusting system comprises biomass forming fuel granulator (1) with upper part provided with a quenching and tempering machine (2). A feed end of quenching and tempering machine has water detection device (4) for detecting water level of the raw material. A back end of the quenching and tempering machine has water adjusting valve (3) with water adjusting signal control device (8) between moisture detection device and the water adjusting valve.    USE - A biomass formed fuel production raw material water content monitoring and adjusting system.    ADVANTAGE - The system provides automatic monitoring of soil moisture, providing for more stable production.    DETAILED DESCRIPTION - Biomass formed fuel production raw material water content monitoring and adjusting system comprises biomass forming fuel granulator (1) with upper part provided with a quenching and tempering machine (2). A feed end of quenching and tempering machine has water detection device (4) for detecting water level of the raw material. A back end of the quenching and tempering machine has water adjusting valve (3) with water adjusting signal control device (8) between moisture detection device and the water adjusting valve. The water detection device transmits the monitored water signal to the signal control device. The processed signal is transmitted to the water adjusting valve and the water adjusting valve adjusts the opening degree according to the signal.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the biomass formed fuel production raw material water content monitoring and adjusting system.    Fuel granulator (1)    Quenching and tempering machine (2)    Water adjusting valve (3)    Water detection device (4)    Adjusting signal control device (8)
NOVELTY - A carbon bonding agent is obtained using biomass-oil derived from corn core, rice hull, oak, rubber wood and other forestry waste.    USE - Carbon bonding agent is used in manufacture of carbon powder.    ADVANTAGE - The carbon bonding agent does not break after falling from height of 1.5 m and does not disperse after burning and stirring.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of carbon bonding agent in manufacture of carbon powder. Corn core, rice hull, oak or rubber wood is processed at 400-600 degrees C, to obtain biomass pyrolysis oil which is then dehydrated at 50-120 degrees C, to obtain carbon bonding agent. The obtained agent is mixed with carbon powder in mass ratio of 1:1~1:3 at 50-100 degrees C, formed at pressure of 0.2-0.6 MPa, and cured at 30-120 degrees C.
NOVELTY - The device has a fermentation chamber (1) connected with a container (4) by a valve (3) and a cable (2), where biogas is extracted from a tank. A movable dome (5) is mounted in the container. The container is connected with a suction line (9) through another valve (10) and a channel (11). The channel conveys material to the chamber. The movable dome is connected with another cable (6) through a third valve (7) of a canal (8), where the gas is lead-out from a digester.    USE - Anaerobic wastewater treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic wastewater treatment device.    Fermentation chamber (1)    Cables (2, 6)    Valves (3, 7, 10)    Container (4)    Movable dome (5)    Canal (8)    Suction line (9)    Channel (11)
NOVELTY - Pipeline conveying coal plant shell covering device comprises a plant crushing system, a stirring system and a forming system, where the plant crushing system comprises a plant feeding groove, a plant crusher and a plant unloading groove.    USE - Used as a pipeline conveying coal plant shell covering device.    ADVANTAGE - The device is capable of covering the coal in plant shell.
NOVELTY - A biogas digester process pipe device comprises a gas turbine meter arranged on the pipeline main body. The gas turbine meter fixedly connects the pipeline by pipeline flange.    USE - A biogas digester process pipe device.    ADVANTAGE - The device is safe to use, and has simple structure.
NOVELTY - Straw marsh gas engineering fermentation tank comprises an outer hood, an insulating layer and an inner wall. The fermentation tank is provided with a fabric distributor, which can achieve uniform distribution of fabric. The fabric distributor comprises a main pipe, a first grade branch pipe and a secondary branch pipe.    USE - Used as a straw marsh gas engineering fermentation tank.    ADVANTAGE - The fermentation tank utilizes circulating mixing system that can achieve uniform circulation of fermentation liquid, and completely contacts with the material and the strain, which solves the incrustation problem to achieve high-efficient straw fermentation.
NOVELTY - Domestic waste fermentation storehouse comprises a fermentation chamber. The fermentation chamber is externally provided with a waterproof wall. The interior of the fermentation chamber is provided with a spraying system. The bottom of the spraying system is provided with a lower grate penetrating fluid tank. The top of the lower grate penetrating fluid tank is provided with a water grate. The lower grate penetrating fluid tank is connected with a filter tank. The filter tank is connected with a marsh gas recycling tank via gate valve and pipeline. The gate valve is set with valve handle.    USE - Used as a domestic waste fermentation storehouse.    ADVANTAGE - The fermentation storehouse has simple structure and is convenient to use; ensures rapid recovery of waste to biogas for power generation or heating; and completely meets the national quantization of domestic waste reduction, recycling, harmless and industrialization.
NOVELTY - The machine has a combustion furnace provided with an outer wall and an inner wall, where the outer wall and an inner wall are connected to form a water cooling chamber. The water-cooling chamber is equipped with a water inlet pipe and a water outlet pipe. A bottom of the combustion chamber is provided with a furnace bridge. A lower part of the furnace bridge is provided with a slag collecting chamber. A fan is connected to a combustion chamber through an air pipe.    USE - Flushing paragraphs biomass gasification combustion machine.    ADVANTAGE - The machine is environment-friendly, energy-saving and better in heat energy utilization rate, and provides stable power range.
NOVELTY - The machine has a water-cooling chamber equipped with a water inlet pipe and a water outlet pipe. An inner wall is provided with a combustion chamber that is provided with a furnace bridge. A lower part of the furnace bridge is provided with a slag collecting chamber. The furnace bridge is provided with a stirring device that is connected with a stirring speed changing motor through a connecting device. An air outlet pipeline is connected with an air outlet opening of the slag collecting chamber. A fan air outlet is connected to the combustion chamber through an air pipe.    USE - Stirring biomass gasification combustion machine.    ADVANTAGE - The machine can improve dredge dust slag cleaning effect so as to ensure for stable and fully combustion. The machine has environment-friendly and energy-saving effect, high heat energy utilization rate up to 95 percent. The machine can reduce the ash residue to realize free control for adjusting feeding and air quantity. The machine can meet the industrial continuous stable range and high power demand, and can be adjusted according to actual requirement. The machine avoids need of high power and diesel oil or gas.
NOVELTY - The boiler has a furnace body whose inner wall is provided with a water chamber. An upper part of the water chamber is connected with a water outlet pipe. A lower part of the water chamber is connected with a water inlet pipe. A dust chamber is connected with an upper part of the furnace body. A gas collecting pipe is fixed in the water chamber. A lower end of the gas collecting pipe is connected with a hearth. An upper end of the gas collecting pipe is connected with a gas collecting chamber. Top of an air chamber is provided with a fuel gas outlet.    USE - Straw gasification energy-saving boiler.    ADVANTAGE - The boiler reduces heat loss and improves energy-saving effect.
NOVELTY - The system has a mobile deodorizing cover fixed to a fermenting groove. The mobile deodorizing cover is internally arranged with a throwing machine for overturning and throwing fermented manure into the fermenting groove. A top part of the mobile deodorizing cover is provided with a track. The track is fixed on a workshop. A main air pipe is fixed above the track. A lower part of the main air pipe is matched with the mobile deodorizing cover through a butt joint groove. The mobile deodorizing cover is provided with a transparent cover plate.    USE - Mobile fermented manure odor collecting system.    ADVANTAGE - The system is simple in structure and convenient to use, and can collect odor while processing solid waste fermented manure. The system reduces construction cost and processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a mobile fermented manure odor collecting system.
NOVELTY - Sludge circulation reactor comprises a reactor main body, which is inclined at the bottom of funnel-shaped structure. The middle part of main body is provided with a first flocculating chamber and a guide flow chamber. The outer side of guide flow chamber is provided with a separation chamber. The outer side of first flocculating chamber is provided with an umbrella shaped cover, which is set on a part of separation chamber. At least one mud residue concentrated chamber is set between umbrella shaped cover and separating chamber. A first water inlet pipe is set in first flocculating chamber.    USE - The reactor is useful for processing industrial organic waste water, and anaerobic pretreatment of wastewater sludge.    ADVANTAGE - The reactor improves biodegradability of waste water, is capable of carrying out uniform anaerobic fermentation process for various waste water of industrial collecting zone to make it stable with the same property of waste water; and provides processing conditions for the next stage.    DETAILED DESCRIPTION - Sludge circulation reactor comprises a reactor main body, which is inclined at the bottom of funnel-shaped structure. The middle part of main body is provided with a first flocculating chamber and a guide flow chamber from bottom to top. The outer side of guide flow chamber is provided with a separation chamber. The outer side of first flocculating chamber is provided with an umbrella shaped cover, which is set on a part of separation chamber. At least one mud residue concentrated chamber is set between umbrella shaped cover and separating chamber. A first water inlet pipe is set in first flocculating chamber. The top part of reactor main body is provided with a water collecting groove, which is connected to outer side of a water outlet pipe.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the sludge circulation reactor.
NOVELTY - A collecting device of domestic garbage field leakage sewage and marsh gas comprises a hollow tube and filling protective sleeve. The protective sleeve is provided with anti-seepage layer. The hollow tube is retained to form sewage collecting pipe. Garbage in upper layer and lower layer are smoothly distributed with hollow pipe for filling protection sleeve which is removed after filling protective sleeve. Uppermost layer is equipped with hollow tube which is retained to form marsh gas collecting pipe.    USE - A collecting device of domestic garbage field leakage sewage and marsh gas.    ADVANTAGE - The collecting device reduces sewage leakage and marsh gas overflow to underground water, reduces pollution of environment and atmosphere, and has very good spreading and using value.
NOVELTY - The method involves positioning UASB reactor on bio-fuel gas storage cabin. The organic waste is gathered by the material gathering pool. The gathered organic waste is fed to solid-liquid separator. The organic waste water is supplied to the heat exchanger. The high-temperature fuel gas is produced through the straw gasification furnace. The temperature of the organic waste water filled to heat exchanger is determined. The dust contained in high temperature fuel gas is removed.    USE - Method for producing bio-fuel gas.    ADVANTAGE - The fermentation cost of the bio-fuel gas can be minimized effectively. The heating temperature of the organic waste water can be improved effectively. The fermentation efficiency of bio-fuel gas can be improved. The production efficiency of bio-fuel gas can be improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating bio-gas fuel producing method.(Drawing includes non-English language text)
NOVELTY - Method for preparing compost, involves pulverizing rice hulls having particle size of 100-800 meshes, heating the pulverized product, adding manure or food waste to the obtained product, and aging the obtained mixture.    USE - The method is useful for preparing compost (claimed).    ADVANTAGE - The method is rapid and environmentally-friendly, and generates no bad odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost, which is prepared by the above-mentioned method.
NOVELTY - Method of processing alcohol fermentation wastewater, involves removing solid substance impurities from the alcohol fermentation wastewater, adjusting the pH value of the wastewater to 5-8, inoculating yeast seed liquid (2.5-20 volume/volume%) to the wastewater, performing aerobic fermentation for 2-5 days at 25-35 degrees C, collecting the yeast from the wastewater, and performing subsequent treatment to the wastewater according to the discharge requirements.    USE - The method is useful for processing alcohol fermentation wastewater.    ADVANTAGE - The method is simple and cost-effective, does not require addition of any nutrient substance, has high chemical oxygen demand removal rate, avoids the long time strain domestication stage desired in the traditional anaerobic and aerobic active sludge processing methods, produces the yeast rich in fat, protein, nucleic acid, lycopene and other yeast components with high added value, requires simple and normal aerobic fermentation device, does not require expensive and complex process devices used in the anaerobic active sludge method, and has short fermentation period.
NOVELTY - Dual-mode biogas digester comprises digester walls protruding from the ground, which are mutually provided with feed inlets and outlets. The upper surface of the biogas digester wall is provided with a water tank surrounding the biogas digester. The water tank is tightly connected to a cover on the upper biogas digester wall. The biogas digester wall is provided with a gas-guide tube connected to a gas storage cabinet. The convex plates protruding from the biogas digester walls are arranged on the position of inner side of the biogas digester wall in the vicinity of surface of biogas slurry.    USE - Used as a dual-mode biogas digester.    ADVANTAGE - The digester contributes to a well reciprocal conversion between fecal digester and straw digester due to the convex plates are arranged on the position of inner side of the biogas digester wall in the vicinity of surface of biogas slurry, has good utilization rate of resources with actual situations, and hence ensures utilization ratio by utilizing straw fermentation mode during the shortage of fecal matter and utilizing feces fermentation mode during the shortage of straws, and also ensures gas production and utilization of biogas digesters.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the dual-mode biogas digester.
NOVELTY - The dry system (100) has an incinerator (120) for supplying hot air to a rotary drum (130). A centrifugation device (140) is connected to the exit of rotary drum for separating pellet raw material ejected in rotary drum. A blower (150) is connected to centrifugation device. An exhaust control device (160) is installed at lower portion of centrifugation device for selectively discharging only pellet raw material having water content less than 12%.    USE - Dry system for manufacturing farming byproduct such as rice straw and barley straw, wheat straw, cornstalk, and red pepper into fuel pellet.    ADVANTAGE - Since exhaust control device is installed at lower portion of centrifugation device for selectively discharging only pellet raw material having water content less than 12%, the drying of pellet raw material can be performed easily. Hence farming byproduct can be manufactured reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows the front side view of the dry system.    Dry system (100)    Incinerator (120)    Rotary drum (130)    Centrifugation device (140)    Blower (150)    Exhaust control device (160)
NOVELTY - The method involves filling artificial wetland with combined filling material. The artificial wetland is divided into four groups. The water sewage pipe is connected from first grade artificial wetland to drop oxygen. The microorganism and planting in sewage are performed with combined filler (5) of lotus. The water is discharged by sewage drain pipe from thumb grade artificial wetland. The natural compound oxygen is recovered after entering next circulation, drop water aeration water power oxygenation and intermittent feeding of natural compound oxygen.    USE - Mountain urban constructed wetland sewage treatment system used for controlling discharge of methane.    ADVANTAGE - The artificial wetland having high dissolved oxygen state can be provided so that the methane producing bacteria can be effectively inhibited and the generation and discharge of methane can be controlled effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the mountain urban constructed wetland sewage treatment system used for controlling discharge of methane. (Drawing includes non-English language text)    Water inlet pipe (1)    Water distribution channel (2)    Filler (5)    Water collecting channel (6)    Water outlet pipe (7)
NOVELTY - A production technology for cultivating algae includes a first-stage cultivating process and a second-stage cultivating process. The first-stage cultivating process includes providing a first culture medium to increase the growth rate of the algae so that the algae have the optimum growth density. The second-stage cultivating process includes providing a second culture medium to produce fat or oil in the algae so that the algae have the optimum amount of fat or oil. Thus, the first-stage cultivating process and the second-stage cultivating process are proceeded individually so that the algae grows very rapidly in the first-stage cultivating process to reach the optimum growth density and then produces the fat or oil largely in the second-stage cultivating process to have the maximum amount of fat or oil so as to increase the productivity of the fat or oil.
NOVELTY - The present invention provides a complete method and equipment system for transforming sewage sludge in cities into storable gas, oil, and solid fuel. It is processed under fully closed equipment system, solving the currently existing deficiency problems like one-dimension environmental thinking and the defect that could cause secondary pollution. In particular, during the waste treatment procedure, the present invention eradicates the emission of carbon, waste gas, GHG, dioxin, and fly ash which contains trace concentrations of heavy metals, and therefore achieves the environmental treatment completely free from secondary pollutions, and recycles sewage sludge in cities wholly. The present invention is a safe method equipment system for city sewage sludge treatment.
NOVELTY - A cylinder particle fuel is manufactured by mixing crushed coal and straw cylinder particle, with weight ratio of crushed coal to straw cylinder particle of 1:0.15-0.7, and shape of the cylinder particle of solid core cylinder.    USE - Method for manufacturing cylinder particle fuel (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the straw roller extruder.    Cutter knife (1-5)    Steel plate (1-6)    Through-hole (1-7)    Main shaft (1-8)    Rollers (1-9)    Charging basket (1-10)    Discharge hole (1-11)
NOVELTY - Disposing urban and rural organic waste by using Bacillus subtilis, is claimed. The protection range of this method depends on the quantity and usage method of Bacillus subtilis.    USE - The method is useful for disposing urban and rural organic waste by using Bacillus subtilis.    ADVANTAGE - The method ensures rapid disposing of waste.
NOVELTY - Method for manufacturing mixed carboxylic acid involves performing anaerobic fermentation using marine algae.    USE - The method is useful for manufacturing mixed carboxylic acid used in biofuels chosen from alcohol and ester compound (all claimed).    ADVANTAGE - The method is simple, environmentally-friendly and cost-effective, provides high yields of mixed carboxylic acid, does not require complex bacterial strains, and produces mixed ethanol that has outstanding energy content, corrosivity and volatility compared to ethanol alone.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofuel, which comprises mixed carboxylic acid manufactured by the above-mentioned method as raw material and is manufactured by microbial fermentation or chemical reaction.
NOVELTY - Producing biological diesel oil with low temperature active lipase catalytic grease, where it is provided with low temperature rotating ester active lipase catalytic raw material oil and short chain alcohol ester exchange reaction for preparing biological diesel oil, short chain alcohol and oil raw material mol ratio is 2:1-5:1, the reaction temperature is 15-40 degrees C and the reaction in the solvent-free system or n-hexane system, enzyme adding amount is added with 60-130 U according to per gram of oil at low temperature, the raw material oil into synthetic diesel oil.    USE - The method is useful for producing biological diesel oil with low temperature active lipase catalytic grease (claimed).    ADVANTAGE - The method efficiently produces biological diesel oil with low temperature active lipase catalytic grease. The raw material grease and reaction process of methanol at low temperature can reach higher esterification rate can be effective to convert renewable oil raw material to obtain the high yield of biological diesel oil at low temperature. The method not only reduces the energy consumption of the production, it also overcomes the lipase thermal stability difference.
NOVELTY - Preparation of biodiesel comprises under heterotrophic condition, culturing oil-producing microalgae, separating and obtaining oil-containing microalgae; in the presence of catalyst and liquid alkane, reacting oil-containing microalgae with monohydric alcohol, separating and obtaining biodiesel.    USE - Method of preparation of biodiesel (claimed).    ADVANTAGE - The method reduces the use amount of monohydric alcohol, and has reduced reaction time.
NOVELTY - Carbon source and nitrogen phosphorus element in excess sludge are recycled by putting excess sludge in reactor; using sodium phosphate and sodium hydroxide solution to adjust pH of sludge; stirring and fermenting at 15-35 degrees C; using pH electrode for real time monitoring the pH change situation in the reactor; residual sludge fermenting for 4-14 days; centrifuging and separating to obtain supernatant fluid containing organic acid; and adding magnesium salt to residual sludge fermentation liquid.    USE - Method for recycling carbon source and nitrogen phosphorus element in excess sludge (claimed).    ADVANTAGE - The method has reduced cost.    DETAILED DESCRIPTION - Recycling carbon source and nitrogen phosphorus element in excess sludge comprises:    (A) putting excess sludge in reactor, the sludge having 9000-13000 mg/L of total suspended solids and 7000-11000 mg/L of volatile suspended solid; using sodium phosphate to adjust pH of sludge to 8-8.5 and using sodium hydroxide solution to adjust pH to 10; and discharging air from top of reactor, sealing the reactor, and stirring and fermenting at 15-35 degrees C;    (B) using pH electrode for real time monitoring the pH change situation in the reactor; and using sodium phosphate or sodium hydroxide solution to control the pH of the reactor;    (C) using sodium hydroxide solution to control pH value of the reactor;    (D) residual sludge fermenting for 4-14 days; and centrifuging and separating to obtain supernatant fluid containing organic acid; and    (E) controlling clear liquid pH under alkaline condition; adding magnesium salt to the residual sludge fermentation liquid; adjusting magnesium ion and ammonia nitrogen at a ratio of 1.8-2:1; stirring for 15-20 minutes; and centrifuging.
NOVELTY - The device has a cylinder stirrer (6), which has a main part located on a concrete membrane tank reactor (4), and a roller (7) provided with a guide blade and a lifting board. The end of a first drum (18) and a second drum (14) are respectively connected with a feeding device (2). A discharging device (13) is connected with a groove body (8). The bottom of the groove body is paved with a heat pipe (15). A biogas boiler (10) and solar water heater (11) are connected with the heat pipe through a water pipe (12). The second drum is provided with a second window.    USE - Continuous dry biogas fermentation device.    ADVANTAGE - Improves fermentation efficiency and yield by keeping continuous fermentation active strain and increasing heat transfer and mass transfer effect by material stirring.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biogas by continuous dry biogas fermentation device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the continuous dry biogas fermentation device.    Feeding device (2)    Concrete membrane tank reactor (4)    Cylinder stirrer (6)    Roller (7)    Groove body (8)    Biogas boiler (10)    Solar water heater (11)    Water pipe (12)    Discharging device (13)    Second drum (14)    Heat pipe (15)    First drum (18)
NOVELTY - A deodorant comprises (in mass%) 90-95 of modified iron powder, 3.8-7.5 of sodium dodecyl benzene sulfonate, 0.8-1.5 of sodium carbonate, and 0.4-1 of alkaline protease.    USE - Deodorant for treating domestic rubbish.    ADVANTAGE - The deodorant has high reliability, and removes hydrogen sulfide at a rate of 65-70% within 96 hours from the rubbish by reducing the odor concentration of 42-61%, and reduces the release of odor gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing deodorant    (2) a deodorant utilization method.
NOVELTY - Generating hydrogen by anaerobic fermentation of water bloom blue algae, comprises: (1) slaving and gathering water bloom blue algae; (2) directly encapsulating the gathered water bloom blue algae in a closed vessel to ferment; and (3) oscillating the water bloom blue algae at speed of 120-240 revolutions per minute for 6-48 hours to generate hydrogen.    USE - The method is useful for generating hydrogen by anaerobic fermentation of water bloom blue algae.    ADVANTAGE - The method is capable of simply generating the hydrogen with high efficiency and high yield in an environmentally friendly manner.
NOVELTY - A biomass cyclic utilization method comprises setting up ecological system on the roof, where the device comprises main water storage barrel, water supply pipe, planting device, aquarium, fermenting barrel, earthworm breeding box and assistant water storage barrel which are connected in turn so as to form circulation system of water and biomass.    USE - Biomass cyclic utilization method.    ADVANTAGE - The method can continuously absorb carbon dioxide and release oxygen, thus providing excellent food, processing kitchen garbage and reducing roof temperature. It also has protection function to the building. The water, fertilizer and soil have no pollution. Biomass obtained from planting is health food without public hazard.    DETAILED DESCRIPTION - Biomass cyclic utilization method comprises setting up ecological system on the roof, where the device comprises main water storage barrel, water supply pipe, planting device, aquarium, fermenting barrel, earthworm breeding box and assistant water storage barrel which are connected in turn so as to form circulation system of water and biomass. Water circularly flows by water gravity and water pump between main water storage barrel, water supply pipe, planting device and secondary water storage barrel. Based on water circulation, by planting and breeding, the biomass circularly changes between fermentation cylinder, earthworm breeding box, plant-growing tank and aquarium through degradation of enzyme and earthworm and photosynthesis of green plant to generate new biomass and oxygen continuously.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating biomass cyclic utilization method.
NOVELTY - The method involves preparing the mixed sludge by concentrating and dewatering the sludge. The mixed sludge is taken as the feed to conduct the anaerobic digestion. The sludge with the same volume is discharged, and refluxed. The sludge is processed by treating the microwave and alkali, and circulated to conduct the anaerobic digestion, so as to collect the methane. The alkaline reagent is included with sodium hydroxide, quick lime or calcium hydroxide.    USE - Method for generating methane for enhancing anaerobic fermentation.    ADVANTAGE - The biomass energy recovery of the sludge anaerobic fermentation can be improved. The gas production rate can be stabilized. The application range of methane generating process can be widened. The sludge recycling can be promoted.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the process of generating methane. (Drawing includes non-English language text)
NOVELTY - Preprocessing and recycling reflux sludge, comprises preparing mixed sludge by thickened sludge and dewatered sludge, performing an anaerobic digestion process on the mixed sludge, and discharging the sewage after preprocessing and recycling the reflux sludge to perform anaerobic fermentation and to produce marsh gas.    USE - The method is useful for preprocessing and recycling reflux sludge.    ADVANTAGE - The method improves the total gas production of anaerobic digestion, shortens the sludge retention time, and reduces the volume of the anaerobic fermentation tank.
NOVELTY - Household waste fermentation cabin comprises a fermentation cabin body externally provided with a waterproof wall. A spraying system located inside the fermentation cabin body and a lower-grate leachate pool located at the bottom of the fermentation cabin body. The leachate pool is located on a water grate, and is connected with a filtering pool provided with a biogas recycling pool through a pipe and a gate valve provided with a handle.    USE - Used as a household waste fermentation cabin.    ADVANTAGE - The fermentation cabin has simple structure, is convenient to use and realizes the reutilization of waste; ensures rapid recycling; and is suitable for industrialization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fermenting the household waste by using the household waste fermentation cabin, comprising (i) introducing the household waste into a bag breaking machine by a belt conveyer to break the bag, and then passing into the fermenting cabin by the belt conveyer; (ii) spraying the waste through the spraying system in the fermenting cabin to remove the odor, subjecting to anaerobic fermentation, allowing the leachate of the waste to flow into the lower-grate leachate pool through the bottom of the fermentation cabin; (iii) allowing the leachate in the lower-grate leachate pool to flow into the filtering pool through the strainer and into the biogas recycling pool; (iv) aspiring the biogas in the biogas recycling pool into the gas storage tank for heating and power generation; and (v) passing the waste into a sorting machine and subjecting to secondary treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the household waste fermentation cabin.
NOVELTY - Method for mixed culture fermenting pretreatment of crop straw, involves mixing the sludge with straw, and performing low intensity ultrasonic wave process-hydrolytic acidification breaking sludge using fermentation broth, pretreating the sludge using low intensity ultrasonic wave, and fermenting liquid of hydrolytic acidification to process straw.    USE - The method is useful for mixed culture fermenting pretreatment of crop straw.    ADVANTAGE - The method improves intermediate temperature two-phase anaerobic digestion performance in the sludge, improves the gas production rate and stability of sludge, and shortens the anaerobic digestion time.
NOVELTY - Improving wheat straw biogas yield through ammonium hydroxide pretreatment process, comprises (a) fully and uniformly mixing ammonia water, water and crushed wheat straw, sealing and storing the mixture at 30-35 degrees C for 7 days, discharging the materials, and (b) adding pre-treated wheat straw into sludge and then inoculating in an anaerobic digestion device, adding 75-80% of water into the reactor to obtain mixed suspension liquid, connecting the reactor with a gas-producing device, and performing the anaerobic fermentation process on the mixture for 50-60 days.    USE - The method is useful for improving biogas yield of wheat straw.    ADVANTAGE - The method is capable of conveniently improving the yield of the biogas in an economical manner.    DETAILED DESCRIPTION - Improving wheat straw biogas yield through ammonium hydroxide pretreatment process, comprises (a) fully and uniformly mixing ammonia water, water and crushed wheat straw, sealing and storing the mixture at 30-35 degrees C for 7 days, discharging materials, where: the wheat straw is crop wheat straw or corn straw; the wheat straw is crushed to less than 2 cm; the concentration of the ammonia water is 25%; the adding amount of the ammonia water counted by the ammonia content is 2-6% of the dry weight of wheat straw; and the water content is 4-7 times of the dry weight of wheat straw, and (b) adding pre-treated wheat straw into sludge and then inoculating in an anaerobic digestion device, adding 75-80% of water into the reactor to obtain mixed suspension liquid, connecting the reactor with a gas-producing device, and performing the anaerobic fermentation process on the mixture for 50-60 days at the temperature of (35|\1) degrees C, where the added amount of the wheat straw in the mixed suspension liquid is 50-60 g/l, and the content mixed liquor suspended solids of the anaerobic digestion sludge is 15 g/l.
NOVELTY - Improving biogas production of poplar waste, comprises mixing the alkali liquor and ground polar waste, regulating the humidity of the poplar waste to 80-90%, placing the mixture in a container and then sealing , discharging the mixture after 4 days, putting the pretreated poplar waste into an anaerobic fermentation device, and adding water into the mixture, regulating temperature and the pH of anaerobic fermentation, sealing the fermentation device, performing anaerobic fermentation for 65-70 days to produce biogas, and finally discharging the biogas residues.    USE - The method is useful for improving biogas production of poplar waste.    ADVANTAGE - The method allows simple and economical improvement of bio gas production in a convenient and environmentally friendly manner.    DETAILED DESCRIPTION - Improving biogas production of poplar waste by wet-type room temperature treatment, comprises uniformly mixing the alkali liquor and the ground polar waste, regulating the humidity of the poplar waste to 80-90% (w/w), placing the mixture in a container and then sealing at a room temperature, discharging the mixture after 4 days, putting the pretreated poplar waste to an anaerobic fermentation device, and adding water into the mixture till the TS load is 3.5-5% (w/v), regulating the anaerobic fermentation temperature to 35-38 degrees C and the pH value of the anaerobic fermentation environment to 6.8-7.5, where the carbon-nitrogen ratio of the fermentation system is 20-30:1 (w/w), sealing the fermentation device, performing anaerobic fermentation for 65-70 days to produce biogas, and finally discharging the biogas residues, where the alkali liquor is the mixture of sodium hydroxide and ammonia water.
NOVELTY - Yield of biodiesel prepared from microalgae grease by enzyme catalysis reaction is improved by extracting microalgae grease from cultured microalgae; using central composite design program to investigate influence of four factors comprising lipase amount, methanol amount, reaction temperature and reaction time and five-level different combination under microalgae grease transesterification reaction in enzyme catalysis reaction system; and building a response surface model equation to determine most preferable enzyme catalysis reaction condition for realizing highest yield of biodiesel.    USE - Method for improving yield of biodiesel prepared from microalgae grease by enzyme catalysis reaction (claimed).    ADVANTAGE - The method has mild catalysis reaction condition, less environment pollution, and high yield of biodiesel transesterified from microalgae grease of 73.41-76.48%.    DETAILED DESCRIPTION - Improvement of yield of biodiesel prepared from microalgae grease by enzyme catalysis reaction comprises:    (A) extracting microalgae grease from cultured microalgae;    (B) using central composite design program to investigate influence of different combinations of four factors comprising lipase amount, methanol amount, reaction temperature and reaction time and five-level different combination under microalgae grease transesterification reaction in enzyme catalysis reaction system; and    (C) building a response surface model equation to determine the most preferable enzyme catalysis reaction condition for realizing highest yield of biodiesel and making the microalgae grease biodiesel yield arrive at highest value under the most preferable enzyme catalysis reaction condition.
NOVELTY - A manufacturing method of eco-friendly recycled fuel comprises a treatment step, a filtration step and a pelletization step. A first filter member and a second filter member in the filtration step are used to separate soil impurities and organic compounds from organic waste water, wherein the soil impurities can be recycled as graded ingredients, and the organic compounds can be mixed with inflammable substances to be pelletized as fuel. This invention not only can solve subsequent treatment problems of organic waste water, but also can recycle them to produce graded ingredients and fuel, thereby reaching the effects of environmental protection and energy save.
NOVELTY - Synthesizing ethoxymethylene malononitrile, comprises: (1) dropping malononitrile into triethyl orthoformate under cooling condition in ice bath, and adding catalyst of anhydrous zinc chloride into cooled mixture and then reacting at 60-80 degrees C for 2-4 hours; and (2) distilling out the ethanol, cooling the mixture to precipitate out solid, and filtering and collecting the solid.    USE - The method is useful for synthesizing ethoxymethylene malononitrile.    ADVANTAGE - The method is capable of simply and economically synthesizing the ethoxymethylene malononitrile with high yield, purity and recrystallinity and improved stability and quality in an environmentally friendly manner.
NOVELTY - The device has a separating box (4) that is arranged in a reaction tank (5). A feeding port (211) is arranged along feeding direction of a valve plate (212). A separating barrel (2) is provided with an oil outlet pipe (225). The outlet pipe (61) of the oil pump is connected to the upper portion of the separating tank (3). Each separating tank is connected with an oil pipe (42). The outlet pipe is connected with the oil tank. A feeding door (12) is provided in the upper vat portion. An additive feeding hole is formed in the reaction tank.    USE - Device for separating garbage of food e.g. edible oil from biodiesel.    ADVANTAGE - The generation of waste in the food oil can be avoided. The efficiency and operability of the device for separating garbage of food from biodiesel can be improved.    DETAILED DESCRIPTION - An UV sterilizing lamp and hot water pipe (15) is connected with the electric valve (F2). A gear (214) is engaged with a rack (213), and is connected with a motor (D2). A gap is formed in the flange, and is connected with a trumpet outlet. A connecting plate (224) is connected with a transmission mechanism. A shaft sleeve (226) is connected with the connecting plate. The sedimentation tank (9) is connected with an electromagnetic valve (C2).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the device for separating garbage of food from biodiesel.    Separating barrel (2)    Separating tanks (3,9)    Separating box (4)    Reaction tank (5)    Feeding door (12)    Hot water pipe (15)    Oil pipe (42)    Outlet pipe (61)    Feeding port (211)    Valve plate (212)    Rack (213)    Gear (214)    Connecting plate (224)    Oil outlet pipe (225)    Shaft sleeve (226)    Electromagnetic valve (C2)    Motor (D2)    Electric valve (F2)
NOVELTY - The system has an oil tank (1) provided with a methanol dispenser tray (3) and a tray feeders catalyst (2), where the oil tank, methanol dispenser tray and tray feeders catalyst are connected to a programmable controller (4). Storage tanks and the tray feeders catalyst are connected through a mixer (5) that is connected with the oil tank and a cooler (7). A clarifier (8) is connected with the programmable controller.    USE - System for producing biofuel from vegetable oils.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for producing biofuel from vegetable oils.    Oil tank (1)    Tray feeders catalyst (2)    Methanol dispenser tray (3)    Programmable controller (4)    Mixer (5)    Cooler (7)    Clarifier (8)
NOVELTY - A fuel production method involves performing a heterogeneous process with etherification catalyst in liquid-liquid interface in presence of liquid acid catalyst to form ether fuel, and mixing obtained fuel with an ester to form rapeseed oil. Sludge is separated as crystalline potassium hydrogen sulfate, which is utilized as fertilizer in agriculture. The glycerin fraction is formed during production of biodiesel from vegetable oils or animal fats.    USE - Method for producing fuel from glycerin fraction.
NOVELTY - Preparation of catalyst comprises pretreating soluble metal compound with alcohol at 0-150 degrees C for 0.1-8 hoursto give 10-80 wt.% solution, diluting metal compound solution with water, slowly mixing precipitator into deposition reactor, controlling temperature at 0-120 degrees C and pH at 7-13, aging for 2-48 hours at 0-80 degrees C, filtering precipitate, washing and drying at 40-150 degrees C for 4-48 hours; and roasting in muffle furnace at 200-800 degrees C for 2-20 hours, and tableting, pelleting and reducing.    USE - Catalyst is used for one-carbon chemical reactions such as Fischer Tropsch, methanol synthesis and steam methane reformation.    ADVANTAGE - The catalyst has high deposition catalytic activity, high conversion rate, and has stable reaction performance.    DETAILED DESCRIPTION - The alcohol comprises methanol, ethanol, propanol, butanol, pentanol, ethylene glycol, propylene glycol, glycerol, butanediol and/or polyethylene glycol.
NOVELTY - Ethanol composition comprises 95.0-99.5 vol.% of ethanol and 0.5-5.0 vol.% of an alkyl ester of fatty acids and a contaminant metal content.    USE - Ethanol composition for use as jet fuel.    ADVANTAGE - The ethanol composition ensures good physical-chemical properties on systems of storage and transportation of fuel on aircraft.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating ethanol composition for reducing contaminant metal content.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting improving lubricity of ethanol. (Drawing includes non-English language text).
NOVELTY - A bio oil manufacturing method involves preparing a vapor phase cracking product using microporous molecular sieve catalyst and mesoporous skeleton including platinum, and condensing the prepared product with liquid bio oil.    USE - Method for manufacturing bio oil.    ADVANTAGE - The method enables manufacturing bio oil with increased stability, calorific value and aromatic compound, and improving selectivity of aromatic compound in the bio oil component.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for manufacturing bio oil.
NOVELTY - A benzoxazole-containing compound (I).    USE - New benzoxazole-containing compound is used for oil marker composition for distinguishing oil e.g. gasoline, diesel, fuel oil, kerosene, biodiesel and bio-ethanol (all claimed).    ADVANTAGE - The oil marker composition containing the benzoxazole-containing compound has excellent stability.    DETAILED DESCRIPTION - A benzoxazole-containing compound of formula (I).    R=1-16C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) oil marker composition, which contains benzoxazole-containing compound (I) (0.001-10 wt.%) and organic solvent (90-99.999 wt.%); and    (2) method of distinguishing oil.
NOVELTY - The system (S) has emission quantity information unit (100) to receive emission quantity information about air pollution material in atmosphere, and indexes exhaustion list of emission quantity information. An emission quantity calculation unit (200) computes the year emission quantity information while producing accumulation emission quantity information, global and specific location emission quantity information. A chemical species differentiation unit (300) produces chemical species emission quantity information to extract greenhouse gas and pollution material.    USE - Air pollution material emission quantity calculation system.    ADVANTAGE - The air pollution material and greenhouse gases are collected and emission quantity information is produced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the air pollution material emission quantity calculation system.(Drawing includes non-English language text)    Emission quantity information unit (100)    Emission quantity calculation unit (200)    Chemical species differentiation unit (300)    Emission quantity time assignment unit (400)    Air pollution material emission quantity calculation system (S)
NOVELTY - The device has a gasification furnace body fixedly connected with a baffle plate. An ash discharge port is formed in a middle part of the baffle plate and provided with a falling plate on a lower side of the baffle plate. The baffle plate is connected with the gasification furnace body to form an ash storage tank. The baffle plate is installed with a jet nozzle. A rocker shaft is arranged on an upper end of the gasification furnace body. A pressure rod is connected with the rocking shaft. A rear end of the pressure rod is arranged opposite to an end of the jet nozzle.    USE - Pressing material and ash discharge device for a biomass gasification furnace.    ADVANTAGE - The device can compact biomass material into an inner cavity of the gasification furnace body so as to enhance continuity and stability of gasification of biomass material to realize continuous gas supply. The device makes stored ash to be pressed to achieve continuous operation, and has wide practical and popularization values.
NOVELTY - The device has an ash storage tank arranged on a lower side of a baffle plate that is formed with a mounting hole, an ash storage box, a wall and a fan. The fan is connected to an air inlet pipe that passes through a gasification furnace body. An outer wall of the gasification furnace is assembled on the baffle plate that is arranged on an upper side of an ash falling pipe. The ash falling pipe is equipped with an air inlet nozzle. A rocker shaft is arranged on an upper end of the gasification furnace body. A pressure rod is connected to a rocking shaft that is connected with an air nozzle.    USE - Pressure device for use in a biomass gasification furnace.    ADVANTAGE - The device is easy to accumulate slag so as to realize a practical and popularization value.
NOVELTY - The stove has a stove body whose bottom part is provided with a fire grate, a hearth and a furnace. The furnace is provided with a feeding port and a flue. The hearth is provided with a gasification chamber that is arranged at an interval between upper and lower spaces. A gasification chamber is provided with a fire tube. The fire tube is formed with a vent hole and connected with a fire guiding tube of a combustion chamber through the grate and furnace. An upper opening of the combustion chamber is matched with the fire guiding tube. The gasification chamber is matched with the feeding port.    USE - Biomass energy-collecting stove.    ADVANTAGE - The stove can utilize coal and firewood so as to avoid formation of black smoke and blackening phenomenon of a pot during a fumigation process. The stove prevents environment from being polluted, avoids generation of excess flame and increases heat generation value for boiling water. The stove is simple in structure, and can be utilized in wide rural areas.
NOVELTY - Pyrolytic forming of biomass carbon comprises crushing biomass material, mixing with pulverized coal, drying, feeding into an inlet of an annular rotary furnace, passing metallurgical flue gas from the outlet of the rotary furnace, flowing the metallurgical flue gas according to the annular rotary furnace direction, heating and dry distillation of mixture to obtain biomass carbon and pyrolytic gas.    USE - The method is useful for pyrolytic forming of biomass carbon.    ADVANTAGE - The method: ensures carbonization quality of biomass carbon by controlling the reaction time and flow rate; and prepares biomass carbon, which can be recycled for smelting metal, and is suitable for smelting enterprises.
NOVELTY - The cracker has a cracking chamber including an end connected with a spiral feeding device and another end connected with a dust remover. A fire grate is placed on the cracking chamber. A dust cleaning cavity separates the fire grate and the cracking chamber. A gasification device is fixed with a pyrolysis chamber. An air guide device has a funnel including a funnel surface i.e. concave surface, in which a small hole is formed, an upper end and a tubular lower end passed through the fire grate and extended to the cracking chamber.    USE - Inner circulation type biomass particle cracker.    ADVANTAGE - The cracker can increase a contact area of gasification and biomass particle fuel, thus improving cracking efficiency, achieving complete cracking process, and improving dust removing efficiency of the cracker.    DETAILED DESCRIPTION - The cracking chamber is covered with a layer made of basalt reinforced ceramic composite material.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of an inner circulation type biomass particle cracker.
NOVELTY - Treating acidic wastewater, comprises conveying the acid wastewater in an regulating pool (2) to an anaerobic reactor (3) by a sewage lifting pump (1) for fermenting to produce acid and methane, regulating a pH value of the anaerobic effluent from the anaerobic reactor to 7-7.5, reflowing part of the anaerobic effluent to the regulating pool by a recovery tank (4) and conveying the remained anaerobic effluent into an water pool (5) for performing anaerobic reaction, where the content of the anaerobic effluent in the anaerobic reactor is 15 kg/m3.    USE - The method is useful for treating acidic wastewater.    ADVANTAGE - The method allows simple and economical treatment of acidic wastewater with reduced alkaline in a safe manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an anaerobic treating of acid wastewater.    Sewage lifting pump (1)    Regulating pool (2)    Anaerobic reactor (3)    Recovery tank (4)    Water pool. (5)
NOVELTY - Biomass composite fuel production system comprises raw coal crusher and straw crusher, in which raw coal and biological raw material respectively are carried out with physical processing through raw coal crusher and straw crusher; dosing machine used to automatically distribute material into weighing hopper according to process, and scale that automatically adds adjusted biomass additive of certain quantity to stirring barrel.    USE - Biomass composite fuel production system.    ADVANTAGE - The system has small floor area requirement, compact structure, rational layout, high utilization rate, and versatile. It is capable of processing of garbage.    DETAILED DESCRIPTION - Biomass composite fuel production system comprises raw coal crusher and straw crusher, in which raw coal and biological raw material respectively are carried out with physical processing through raw coal crusher and straw crusher; dosing machine used to automatically distribute material into weighing hopper according to process, and weighed mixture at regular time is added to hopper of forced stirrer and is conveyed to stirring barrel by lifting device of mixer; and scale that automatically adds adjusted biomass additive of certain quantity to stirring barrel, such that after stirring, material is discharged to argillization regulating reservoir to continue stirring and to make biomass additive react with material, thus treated mud material is changed into biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass composite fuel production system.
NOVELTY - Method of extracting biological active substance from marigold residues by subcritical water extraction, involves extracting the marigold residues by subcritical water extraction in subcritical water extraction device, concentrating the coarse extract liquid in a vacuum rotary evaporator, dissolving the concentrate in methanol, cooling the solution, centrifuging the solution, filtering the supernatant liquid, concentrating the filtrate in the vacuum rotary evaporator and drying the product.    USE - The method is useful for extracting biological active substance from marigold residues.    ADVANTAGE - The method is simple, cost-effective, environmentally-friendly and convenient and safe to perform, and has high efficiency and wide application value.    DETAILED DESCRIPTION - Method of extracting biological active substance from marigold residues by subcritical water extraction, involves (a) extracting the marigold residues by subcritical water extraction in subcritical water extraction device at 100-260 degrees C and at pressure of 4-7 MPa for 50-60 minutes, and obtaining a coarse extract liquid, where ratio of subcritical water to the marigold residues is 20-70 ml:1 g, (b) concentrating the coarse extract liquid in a vacuum rotary evaporator at 60 degrees C and obtaining concentrated liquid ( not greater than 10 ml), (c) dissolving the concentrate in methanol, (d) cooling the solution to 0-20 degrees C for 10-60 minutes, centrifuging the solution at a speed of 3500-6500 revolutions/minute (rpm) for 15-30 minutes, and obtaining the supernatant liquid, (e) filtering the supernatant liquid using a microfilter film having pore diameter of 0.22-0.45 microns, and obtaining the filtrate, and (f) concentrating the filtrate in the vacuum rotary evaporator at 45 degrees C and drying the product.
NOVELTY - Wastewater treatment system comprises a high temperature anaerobic tank and a thin film distilling device. The anaerobic tank contains anaerobes for decomposing the organic pollutants in the wastewater at 30-90 degrees C, and the oxidation-reduction potential of the wastewater in the anaerobic tank is 0 mV to -600 mV. The film distilling device separates the wastewater from the high-temperature anaerobic tank to make a portion of the wastewater passes through thin films in the distilling device in the form of steam to remove the inorganic pollutants in the wastewater.    USE - The wastewater treatment system is useful for simultaneously removing organic and inorganic pollutants in wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a wastewater treatment method for simultaneously removing organic and inorganic pollutants in wastewater, comprising inflowing wastewater into the anaerobic tank containing the anaerobes to decompose the organic pollutants in the wastewater by the anaerobes at 30-90 degrees C, where the oxidation-reduction potential of the wastewater in the anaerobic tank is 0 mV to -600 mV; flowing the wastewater in the anaerobic tank into the film distilling device, and passing a portion of the wastewater through the thin films of the film distilling device in the form of steam to remove the inorganic pollutants in the wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wastewater treatment system.
NOVELTY - A biodiesel comprises (wt.%) C14:0 methyl myristate (0.11-0.18), C16:0 methyl palmitate (7.23-8.45), C18:0 methyl stearate (4.1-5.34), C18:1 methyl oleate (19.16-23.42), C18:2 methyl linoleate (57.39-63.14), C20:0 methyl arachidate (1.54-2.51), C20:1 methyl cis-11-eicosenoate (0.61-0.98), C20:0 methyl behenate (1.33-2.4), and C24:0 methyl tetracosanoate (0.08-0.12).    USE - A biodiesel.    ADVANTAGE - The biodiesel is cheap, has high cetane number and excellent performance, meets national biodiesel standard, has simple preparation method having mild reaction condition, and can be applied to industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the biodiesel comprising mixing Silybum marianum oil and methanol at a molar ratio of 1:4-15, heating at 35-45 degrees C while stirring, adding potassium hydroxide (1-3 wt.%), heating at 45-75 degrees C for 30-120 minutes, cooling to room temperature, setting aside, subjecting to vacuum distillation to recover excess methanol, adding diluted sulfuric acid (5-15 mass%), regulating pH value, heating at 45-75 degrees C for 30-120 minutes, cooling to room temperature, subjecting to vacuum distillation, recovering excessive methanol from the upper product of the vacuum distillation, adding diluted sulfuric acid (5-15 mass%), neutralizing, washing with distilled water, and vacuum distilling.
NOVELTY - Carbon-containing core-shell type platinum copper-platinum catalyst comprises graphite fiber cloth as carbon carrier and active metal component supported on the surface of the carrier. The active metal component has a core-shell structure containing platinum-copper alloy as core and platinum as shell. The content of platinum and copper in carbon carrier is 0.19-0.2 mg/cm2 and 0.03-0.08 mg/cm2, respectively. The mass ratio of carbon carrier to active metal containing platinum is 1000-1842:1 and the mass ratio of platinum to copper in carbon carrier is 2.5-6.3:1.    USE - Carbon-containing core-shell type platinum copper-platinum catalyst is used for producing hydrogen.    ADVANTAGE - The carbon-containing core-shell type platinum copper-platinum catalyst has excellent catalytic efficiency and stability, and uses reduced amount of precious metal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of carbon-containing core-shell type platinum copper-platinum catalyst. The graphite fiber cloth is washed ultrasonically for 10-15 minutes in a vacuum environment. The resulting material is subjected to ion beam washing and ion beam sputtering deposition to obtain carbon-containing nanocrystalline thin film catalyst. The resulting catalyst is immersed in sulfuric acid solution having a mass concentration of 0.5-1 mol/L, washed ultrasonically with deionized water and dried to obtain carbon-containing core-shell type platinum copper-platinum catalyst.
NOVELTY - The membrane contains 20-30 weight percent of cellulose acetate, 30-50 weight percent of acetone, 30-50 weight percent of formamide and 10-20 weight percent of propane.    USE - Desalting reverse osmosis membrane.    ADVANTAGE - The membrane reduces production cost, and has better usage effect.
NOVELTY - Microbial triglyceride oil obtained from an oleaginous recombinant microbe, is claimed, where the fatty acid profile of the triglyceride oil comprises at least 40% of saturated fatty acid.    USE - The microbial triglyceride oil is useful: in microalgal oil, Prototheca moriformis oil or Chlorella protothecoides oil (claimed); and for making lipids and oil-based products, including fuels such as biodiesel, renewable diesel, jet fuel, oleochemicals and other compounds, in recombinant microorganisms (preferably oil-bearing microorganisms).    ADVANTAGE - The microbial triglyceride oil economically produces the oils with shorter chain length, higher degree of saturation, greater yield and efficiency and without pigments in an environmental friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a blended triglyceride composition comprising a microbial triglyceride oil and a triglyceride oil from soy, rapeseed, canola, palm, palm kernel, coconut, corn, waste vegetable, Chinese tallow, Olive, Sunflower, cottonseed, chicken fat, beef tallow, porcine tallow, microalgae, macroalgae, microbes, Cuphea, flax, peanut, choice white grease, lard, Camelina sativa, mustard seed, cashew nut, oats, lupine, kenaf, Calendula, hemp, coffee, linseed (flax), hazelnut, Euphorbia, pumpkin seed, coriander, Camellia, sesame, safflower, rice, rung tree, cocoa, copra, opium poppy, castor beans, pecan, jojoba, macadamia, Brazil nuts, avocado, petroleum, or a distillate fraction of any of the preceding oils; and (2) a product produced by chemically modifying a microbial triglyceride oil, where the triglyceride oil is chemically modified by one or more of hydrogenation, hydroprocessing, hydrotreating, deoxygenation, isomerization, metathesis, ozonolysis, epoxidation, oxidation, hydrolysis, sulfation, sulfonation, ethoxylation, propoxylation, amidation, or saponification.
NOVELTY - Crystalline form of D-7-(4-hydroxyphenylacetamido)-3-(1-methyl-1H-tetrazol-5-yl)thiomethylcephem-4-carboxylic acid (I) having an XRD spectrum as given in the specification, is new.    USE - In the manufacture of a medicament with antibacterial properties (claimed), for production of cefoperazone and cefpiramide.    ADVANTAGE - The compound is highly stable and pure thus making it an excellent starting material for the high yield, high purity production of both cefoperazone and cefpiramide; and can be prepared by efficient and environmentally friendly enzymatic condensation of a 3'-thiosubstituted beta -lactam nucleus with an appropriate side chain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the crystalline form of (I).
NOVELTY - The device has an inner container whose top end is extended into a furnace body. A head of an inner container is connected with a feeding hopper. A furnace cover is placed in a storage hopper. A fuel gas pipe is connected with the inner container. A fan is connected with an inlet pipe. A baffle plate is arranged at a lower side of an air inlet pipe. A clapboard is placed at a lower side of an ash outlet. A fuel gas pipe is provided with a gas pipe switch. A burning tower is equipped with an air inlet.    USE - Continuous medical waste innoxious gasification treatment device for use in a hospital.    ADVANTAGE - The device avoids environment pollution.
NOVELTY - The furnace has a pyrolysis furnace part provided with thermocouples and an intelligent temperature control reaction tube. The temperature control reaction tube is fixed at a bottom of a pyrolysis reactor pyrolyzing volatile product purge gas under the action of semi-coke. A separation device separates residual carbon into pyrolysis volatile by an air outlet of a reaction pipe. A two-stage condensing device condenses a volatile component into pyrolysis gas containing a large amount of a non-condensable substance. A pyrolysis gas outlet recycles the gas collected in a collecting bottle.    USE - Solid waste or biomass high efficiency gasification furnace for pyrolyzing oil producing system.    ADVANTAGE - The furnace realizes biomass material pyrolysis process of heat transfer, and effectively uses semi-coke product, which greatly improves the yield and quality of the liquid oil product. The furnace is good for volatile to escape, and obtains biological oil production rate above the normal biomass pyrolysis value.    DETAILED DESCRIPTION - The pyrolysis furnace part has an inner part provided with an inner interface that is made of high temperature stainless steel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solid waste or biomass high efficiency gasification furnace.
NOVELTY - Hydrogen is obtained using hydrogen storage alloy in presence of inert gas. The hydrogen is used for culture solution obtained by cultivating microorganisms having hydrogen production ability.    USE - Manufacture of hydrogen for fuel for battery.    ADVANTAGE - The method efficiently provides hydrogen without requiring separation of hydrogen from inert gas. Since the hydrogen throughput by microorganism increases, the productive efficiency per unit microorganism increases.
NOVELTY - The strain culture tank has a main portion whose upper end is fixed with a motor. A rotating shaft of motor is fixedly connected with a stirring shaft which is fixedly connected with a gear-type defoamer and a stirring paddle. An outer wall of main portion is provided with an interlayer water sleeve. The upper end of interlayer water sleeve is provided with a cooling water outlet, while lower end is provided with a cooling water inlet port. An upper end of air pipe is extended out of the main portion, while lower end is extended to lower portion of stirring shaft.    USE - Strain culture tank of biological composite fertilizer.    ADVANTAGE - The stirring and culturing function of strain culture tank can be improved by simple structure. The cost of strain culture tank can be reduced.
NOVELTY - A process and a system for producing methane gas from a marine system, are disclosed. Production of methane gas from an unconsolidated marine system with gas hydrate deposits by successive steps simultaneous or sequential usage of electric heating using dome-electrode system, pumping hot water, injecting carbon dioxide (CO2) from a drill head and reducing the pressure placed in a pre-drilled well head, is described. The dome for collecting the produced gas in a confined manner without leakage into the atmosphere, is also described. Image 0/0
NOVELTY - The furnace has a furnace body whose top part is provided with a feeding port that is covered by a turning cover, where a middle upper part of the furnace body is provided with a combustion chamber. A bottom part of the combustion chamber is provided with multiple turning fire grates. One end of a connecting rod is extended to the furnace body. A furnace ash cavity is connected with an ignition port by a control disk. The fire grates are connected with a fan through an air pipe. A pressure regulating valve is provided on the air pipe.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace avoids fire grate ash blockage problem, and is provided with a blower on a furnace ash and controlled by pressure regulating valve. The furnace has stable combustion effect, reasonable structure, high safety and high reliability, and does not produce spray fire.
NOVELTY - The device has a furnace wall installed on a discharging channel. The channel is provided with a slag outlet that is connected with a slag discharging groove. A lower part of the discharging groove is provided with a collecting device. A slag outlet is provided with a discharging refractory ash and a smoke exhaust hood. An exhaust pipe is connected with a draught fan.    USE - Liquid state slag-off device for a biomass gasification furnace.    ADVANTAGE - The device can effectively make biomass gasification furnace ash generated by the slag output smoothly, and effectively prevents discharging process of slag splashing and flame, reduces operation work intensity and heat loss and improves gasification efficiency, and is simple in structure and easy to realize.
NOVELTY - Method for sludge reduction by domestic sewage treatment process, involves increasing organism concentration to 3-10 times by membrane separation, and removing organism (50-80%) by anaerobic treatment.    USE - Method for sludge reduction by domestic sewage treatment process.    ADVANTAGE - The method produces is easy and cost-effective, and less excess sludge, and recovers methane gas.
NOVELTY - A fuel is prepared by mixing domestic garbage combustible component (62-80 %mass), coal liquefaction residue (12-28 %mass) and desulfurizing agent (8-10 %mass).    USE - Fuel.    ADVANTAGE - The fuel has high heat value, and is manufactured using simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fuel, which involves sorting municipal solid waste in waste paper and fabric as household garbage combustible component, drying the domestic garbage, drying at 200-300 degrees C, crushing, adding coal liquefaction residue and desulfurizing agent to mixture, fully stirring and mixing for 15-30 minutes.
NOVELTY - Preparation of biological oil and/or pyrolysis gas comprises soaking biomass into catalyst-containing solution; taking out; dry processing to obtain dry biomass; putting dry biomass into pyrolysis solvent; uniformly mixing; and subjecting into pyrolysis rectification at 200-350 degrees C for 3.5 hours to obtain oil and pyrolysis gas.    USE - Preparation of biological oil and/or pyrolysis gas.    ADVANTAGE - The method is simple, has mild reaction conditions, lower cost, and is easy for industrialization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oil used for biomass conversion.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for preparing biological oil and/or pyrolysis gas (Drawing includes non-English language text).
NOVELTY - The method involves rotating pyrolysis product roll at 900-1100 degrees centigrade during high temperature gasification cracking reduction reaction to generate biomass gas gasification. An air pre-heater is provided for pre-heating an air pumping device, and air residual and biomass fuel is entered into a combustion chamber via a gasification chamber. The gasification chamber is provided with a pyrolysis chamber to supply heat for pyrolysis. Flue gas is exhausted from a flue gas outlet. An ash slag is discharged from a slag outlet.    USE - Third segment separating type biomass gasification method.    ADVANTAGE - The method enables reducing content of tar in gas, improving production rate and providing a biomass gas gasification furnace with convenient, energy-saving and environment-friendly effects and continuous operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a third segment separating type biomass gasification method.
NOVELTY - A modified methanol fuel is prepared by processing methanol by steam generator, heating the steam to 300-350 degrees C by a tubular oven, and dealdehyde treating by a nickel-copper catalyst; carrying out secondary catalyst conversion to a mixture of aromatic hydrocarbon and alkane; and blending with a blast resistance agent, antioxidant, lubricant, purifying agent, and other additives, and uniformly mixing.    USE - A modified methanol fuel for an automobile (claimed).    ADVANTAGE - The modified fuel does not produce formaldehyde gas, has improved water resistance, and eliminates corrosivity of methanol.
NOVELTY - Production of biological diesel oil comprises pumping preheated oil and low carbon alcohol into filled solid acid or base catalyst of catalyzing and rectifying tower, and processing two counter-current contact, esterification or ester exchange reaction, and putting on solid acid or alkali catalyst bed layer in tower; distilling low carbon alcohol, condensing, flowing back condensed low carbon alcohol (33-90%) to tower top, and obtaining upper layer biological diesel oil and lower layer by-product glycerine.    USE - Method of production of biological diesel oil (claimed).    ADVANTAGE - The method is energy-saving and environment-friendly, and is suitable for industrial production.    DETAILED DESCRIPTION - Production of biological diesel oil comprises using oil and low carbon alcohol at mol ratio of 1:3-12, pumping preheated oil and low carbon alcohol into filled solid acid or base catalyst of catalyzing and rectifying tower, entering preheater pre-heating oil from top of the tower to the upper part in a form of liquid, and low carbon alcohol from top of tower part in a form of steam, and processing two counter-current contact, esterification or ester exchange reaction, and putting on solid acid or alkali catalyst bed layer in tower; distilling low carbon alcohol, condensing, flowing back condensed low carbon alcohol (33-90%) to tower top, recycling excess in catalytic rectifying tower bottom of settling and layering device, and obtaining upper layer biological diesel oil and lower layer by-product glycerine.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the production of biological diesel oil.
NOVELTY - A maize straw rapid ensiling complex microorganism additive (wt.%) comprises Aspergillus oryzae (L201) (10), plant lactic acid bacteria Lactobacillus (CGMCC. 155) (60), mixture of plant lactic acid bacteria Lactobacillus plantarum (ACCC 11016) (20) and lactic streptococci Lactococcus lactis (ACCC 11093) (10).    USE - As amino acid feed additive for rapid ensiling of maize straw.    ADVANTAGE - The maize straw rapid ensiling complex microorganism additive improves use effect and quality of silage; shortens the needing time of ensiling maize straw; and increases ensiling production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing maize straw rapid ensiling complex microorganism additive involving: 1) crushing dark green maize straw to prepare maize straw powder (95 wt.%) having particle size of 0.5-1 cm; 2) adding organic carrier (5 wt.%) prepared by mixing corn powder with bran (4:1) to the smashed straw, mixing uniformly and making the moisture of mixed materials at 65-70% to give ensiling raw material; 3) uniformly spraying the complex microorganism additive (2-3 wt.%) in the ensiling raw material, at same time, spraying inorganic additive (6-10 wt.%) prepared by mixing salt, urea and water, where the press density is 550-650 kg/m3, the fermentation temperature is 25-30 degrees C; sealing, pressing and anaerobically fermenting for 24-26 days.
NOVELTY - Preparing high energy organic fuel comprises adding low carbon alcohol (50-65 wt.%) and methyl tertiary butyl ether (5-10 wt.%) into a reaction kettle and then mixing, adding heavy aromatics (10-20 wt.%), naphtha (9-16 wt.%) and dimethylbenzene (8-12 wt.%) to the mixture, adding ethanol (0.2-1 wt.%) and 1# antiswelling agent (0.2-1 wt.%) to the mixture and then mixing using a high speed dispersing machine and repeatedly pumping the mixture into a high shear cycle using high shearing emulsifying pump.    USE - The high energy organic fuel is useful for replacing diesel fuel.    ADVANTAGE - The method is capable of preparing high energy organic fuel with improved social and economical benefits in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of preparing high energy organic fuel (Drawing includes non-English language text).
NOVELTY - High energy immiscible organic fuel prepared by mixing methyl tertiary butyl ether, 5C, sulfonated oil, heavy aromatics, ethanolamine and antiswelling agent and adding acetone and latent solvent 200# or 230# in a proportion of 1:2 and adding 40-60 wt.% of reduced methanol.    USE - Used as high energy immiscible organic fuel.    ADVANTAGE - The high energy immiscible fuel is capable of mixing with any immiscible gasoline and can be rapidly and economically prepared with less energy consumption in an eco-friendly manner.
NOVELTY - A biomass raw material is dried in a drier, and carbonized to obtain bio-char. The gas generated in drying process is collected, after cooling. Wood vinegar liquid and tar produced during carbonization are separated and purified. The purified gas is supplied to combustion chamber. The flue gas of combustion chamber is supplied to carbonization device as heat source, and exhaust gas of carbonizing device is supplied to drying device. Thus, continuous biomass carbonization is enabled.    USE - Continuous biomass carbonization method.    ADVANTAGE - The carbonized product of biomass having high quality is efficiently produced by effectively utilizing waste heat.
NOVELTY - Catalyst comprising a carrier, an active component and an auxiliary agent, is new, where the carrier is aluminum oxide and magnesium oxide; the active component is nickel oxide; the auxiliary agent is lanthanum oxide; and the catalyst comprises 30-50 mass% of nickel oxide, 1-5 mass% of lanthanum oxide, 30-50 mass% of aluminum oxide, 12-20 mass% of magnesium oxide and 1-3 mass% of graphite.    USE - The catalyst is useful for preparing natural gas from coke-oven gas and straw gas.    ADVANTAGE - The catalyst is capable of simply preparing the natural gas with high activity and thermostability and good carbon resistance and temperature resistant performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of catalyst.
NOVELTY - Method for preparing biomass diesel using waste fat and oils by catalytic cracking method, involves (a) preprocessing waste fat and oils, (b) thermally and catalytically cracking the preprocessed waste fat and oils, obtaining the crude oil, and catalytically cracking liquid phase and gas phase, (c) distilling the crude oil, and (d) refining the oil, filtering the oil and obtaining the product.    USE - The method is useful for preparing biomass diesel using waste fat and oils by catalytic cracking method.    ADVANTAGE - The method is simple, cost-effective, rapid and easy and convenient to perform under controlled conditions, and can crack long chain compound to reduce condensation point of distillate for transforming oil with high condensation point into light diesel with low condensation point and remove colloid, biological asphaltene and unsaturated compound to obtain clear diesel. The diesel has regular smell and does not exhibit bad odor even after storing for a long time. The diesel is not viscous, and does not block pipe.
NOVELTY - High-temperature high-activity calcium-based carbon dioxide adsorbent, comprises calcium oxide and tricalcium aluminate.    USE - The calcium based carbon dioxide adsorbent is useful for absorbing and strengthening methane steam, reforming and preparing hydrogen, and removing fossil fuel.    ADVANTAGE - The calcium based carbon dioxide adsorbent exhibits high carbon dioxide absorbing ability, is economical, convenient to operate and non-toxic, and has a simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing high temperature and high-activity calcium-based carbon dioxide adsorbent, comprises: (1) weighing and preparing suspension of calcium citrate with mass percentage of 145-30%, and adding a right amount of dispersing agent at the same time; (2) adding alcohol and aluminum salt into the suspension at 55-75 degrees C and then stirring at a constant temperature for 1.5-2.5 hours to obtain solution; (3) adding the solution at room temperature for 8-10 hours and then removing impurity ion via a filtering-washing method; (4) drying the solid at 100-120 degrees C for 10-12 hours; (5) heating the sample at 800-950 degrees C for 1-2.5 hours; and (6) grinding the sample to obtain high-temperature and high-activity calcium-base carbon dioxide adsorbent.
NOVELTY - The method involves setting hydrogen generator to the upper portion of the electrolytic power supply circuit. The electrolysis positive electrode wire is connected with an electronic voltage regulator to increase the output current provided to the electrolytic cell. The hydrogen energy is provided for the working of automobile engine.    USE - Method for driving internal combustion engine used in automobile, ship and fuel gas power generation system of industry.    ADVANTAGE - The pollution caused by the internal combustion engine can be reduced. The power consumption can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the internal combustion engine.
NOVELTY - Invention relates to chemistry and may be used in production of hydrogen. Hydrogen is produced with help of plasma generator with two electrodes, one made up of tapered-channel nozzle and another one made up of aluminium rod aligned with the first electrode to displace axially. Steam or steam-water mix is used as working plasma generating substances. Aluminium rod is fed into arc zone. Produced mix of hydrogen with aluminium oxide fine particles is cooled in water to separate pure hydrogen. Aluminium rod is connected to power supply positive terminal while said nozzle is connected to negative terminal.    USE - Process engineering.    ADVANTAGE - Production of pure hydrogen from water. 1 dwg
NOVELTY - A biofuel quick preparing method involves adding fat material with co-solvent and short chain alcohol solution dissolved with an alkaline catalyst, where utilized amount of the co-solvent is 10-100% of mass of the fat material, mole ratio of the short chain alcohol solution to fat is 3-4.5:1, and utilized amount of the alkaline catalyst is 0.5-5% of mass of the fat material. The mixture is placed in a temperature controlled reciprocating water bath bed. Ester exchange reaction is performed for 5-15 minutes at temperature of 20-30 degrees C and at a low speed vibration condition to obtain the biofuel.    USE - Method for quickly preparing biofuel at normal temperature and normal pressure through homogeneous phase base catalysis.    ADVANTAGE - The method enables for preparing the biofuel without needing high temperature, high pressure, high speed stirring and excessive short chain alcohol to accelerate the reaction, and reacting the fat material and the short chain alcohol under homogeneous phase in 15 minutes, so that the short chain alcohol usage amount is reduced, production energy consumption is reduced, reaction time is shortened and production efficiency is improved.
NOVELTY - Crystallized hybrid solid IM-22 with an organic-inorganic mixed matrix, which contains a three-dimensional structure comprising a zeolitic framework of chabazite (CHA) structural type containing an inorganic network of metal centers to base cations of zinc (Zn2+), interconnected by two imidazolate organic ligands, of 2-methylimidazolate and benzimidazolate substituted on the benzene ring, is claimed, where the solid has an X-ray diffraction pattern including at least the peaks as given in table of the specification.    USE - The hybrid solid is useful for separating multi-branched paraffins included in a hydrocarbon feedstock containing linear paraffins, mono-branched paraffins and multi-branched paraffins (claimed).    ADVANTAGE - The hybrid solid IM-22 has improved performance compared to a conventional zeolitic adsorbent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the hybrid solid, comprising (a) dissolving at least one precursor of zinc (precision zinc) in at least one polar organic solvent-S, (b) adding two ligands consisting of 2-methylimidazolate and benzimidazolate in the solution obtained in step (a), (c) heating the mixture from step (b), (d) filtering and washing the obtained solid IM-22, and (e) drying the solid IM-22 followed by a heat treatment; and    (2) separating multi-branched paraffins included in a hydrocarbon feedstock containing linear paraffins, mono-branched paraffins and multi-branched paraffins having 5-7C per molecule, comprising contacting the feedstock with the hybrid solid IM-22, so as to produce at least a first stream enriched in multi-branched paraffins and a second stream enriched in linear and monobranched paraffins.
NOVELTY - The machinery has an electrolyzer that is provided on water surface of water-tank. The water-tank aqueous solution is electrolyzed using electricity generated with generator. The metal electrically conductive substance which not builds compound with hydrogen and oxygen is given to electrolysis electrode. The regeneration oxygen gas and hydrogen gas are generated to anode and cathode, and injected through exclusive induction pipe. The explosion is raised for regenerated hydrogen gas and oxygen gas in combustion explosion chamber (1).    USE - Machine rotative power machinery used in nuclear power plat.    ADVANTAGE - Since the regeneration oxygen gas and hydrogen gas are generated to anode and cathode and injected through exclusive induction pipe, the human body can be prevented from damage at the time of repairing machine, exchange cancellation process. The energy can be generated effectively. The power apparatus with warm water storage and electrical storage function can be utilized effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the gear for machine motive power source shaft.    Combustion explosion chamber (1)    Hydrogen gas injection tip (2)    Oxygen gas injection tip (3)    Plug for ignition (4)    Rotating shaft cover (8)
NOVELTY - Method for controlling water quality in cemented shrimp pond using Bacillus and bagasse, involves removing rotten and mold infected bagasse, sieving the bagasse for separating the bagasse of suitable length, sterilizing the bagasse, adding sterilized bagasse to fermented Bacillus culture solution, continuing fermentation process, adding fermented bagasse and fermentation broth into water contained in the cemented shrimp pond, and supplying the bagasse and Bacillus into water once with continuous stirring at regular intervals.    USE - The method is useful for controlling water quality in cemented shrimp pond.    ADVANTAGE - The method decreases required quantity of water to be exchanged in shrimp pond during the whole shrimp farming process. The method reduces aquaculture wastewater pollution, hence environmentally-friendly. The method prevents loss of beneficial components from the pond, and reduces entry of the pathogens into the pond hence aquaculture water requirement and cost are saved. The method enables cultivation of the shrimps with good disease resistance and growth rate, hence yield of the shrimps becomes higher and economic benefit is better.
NOVELTY - Methane gas tank comprises a lighting part, a fermenting part, a gas storage part, a feed port, a discharge port and an air outlet. The lighting part is placed at the upper end of the device. The gas storage part and the fermenting part are connected in parallel and are placed at the lower end of the device.    USE - Used as a methane gas tank.    ADVANTAGE - The tank comprises lighting part for maintaining the fermenting time of methane gas, improves the production rate of the methane gas, and ensures low production cost.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the methane gas tank.
NOVELTY - Solar energy methane generator comprises a methane fermentation tank, a fermentation raw material input pipe, a biogas residue and biogas solution outlet, and a methane output pipe. The generator is set in a high heat-preservation sunlight greenhouse. The methane fermentation tank is set in a sealed horizontal barrel plastic tank body. The outer side of the methane fermentation is provided with deep color.    USE - Used as a solar energy methane generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the solar energy methane generator.
NOVELTY - A compound-light catalyst (3) which is supported by silica-type mineral is added to a container (1) which is provided with transparent portion (2), and photocatalyst-supported artificial fiber, and irradiated using light (4) of visible region wavelength like sunlight, and ultraviolet light. A mixed gas of carbon dioxide and water is circulated into the container, and contacted with compound-light catalyst. Thus, conversion of high valence substance is performed.    USE - Conversion of high valence substance e.g. hydrogen, methane, methanol and formic acid (all claimed).    ADVANTAGE - The conversion of high valence substance is efficiently and economically enabled with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for of high valence substance recovery utilization equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows the circuit diagram of high valence substance recovery utilization equipment.    Container (1)    Transparent portion (2)    Compound-light catalyst (3)    Light (4)    Useful substance (5)    Adjustment container (6)
NOVELTY - Bio-organic fertilizer comprises (in parts by wt.) poultry excrement (70-95), crop waste (10-30), biological strain (0.1-0.35) and microelements (0.2-1).    USE - Used as bio-organic fertilizer.    ADVANTAGE - The fertilizer is economical and environment-friendly, has strong specificity, rapid absorption rate and high fertilizing efficiency, and improves the soil bio-activity. The method utilizes active biological strain and completely decomposes and deodorizes the solid waste in a short time to obtain high-quality bio-organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-organic fertilizer comprising adding poultry excrement into a mixed fermentation tank for pre-fermentation, adding biological strain into the mixed fermentation tank, fermenting the materials until the color of the materials turns to dark brown and the manure and compost odor is absent, mixing the fermented materials with crushed crop waste, turning over the complex material, crushing and sieving the complex materials, mixing and pelletizing humic acid, microelements, mineral substance and the sieved materials, drying, cooling and sieving the granular material, and packaging to obtain the finished products.
NOVELTY - Organic fertilizer comprises (in parts by wt.) weathered coal (45-55), bran (5-10), pepper powder slag (5-10), straw (20-30), urea (1-2), water (50-60), Trichoderma culture liquid (10-12), phosphorus source (1-2), iron source (0.01-0.02), zinc source (0.01-0.02), copper source (0.01-0.02), manganese source (0.01-0.02) and boron source (0.05-0.1).    USE - The organic fertilizer is useful for walnut.    ADVANTAGE - The organic fertilizer has high bio-activity and is provided with complete nutrition; allows the walnut tree to grow healthily, improves the stress resistance and disease resistance, improves the fruit setting rate and reduces the empty shell ratio of walnut; and the preparation method is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising (i) uniformly mixing the weathered coal, bran, pepper powder slag and straw, adding the urea and phosphorus source dissolved in water, adding Trichoderma culture liquid, mixing uniformly and fermenting; and (ii) adding iron source, zinc source, copper source, manganese source and boron source, and stirring uniformly.
NOVELTY - A biomass fuel is prepared by crushing straws into strip having a length of 1-5 cm, transporting crushed straws to a bunker of a shaping machine, drying, transporting to a dry-wet detecting device to detect water content, starting a water spraying device if water content is less than 25% until water content reaches 25% or transporting to a blow-drying device controlled at 40-70 degrees C when water content is higher than 25%, extruding qualified straw material, and shaping.    USE - Method of preparing a biomass fuel.    ADVANTAGE - The method has improved production efficiency, reduces damage to machine thus prolonging service life of machine, and prepares product having improved melting point and combustibility and which does not generate slag and ash easily.
NOVELTY - Mushroom culture medium comprises (in %) Eucalyptus tree waste wooden chip (36-46), banana residue (36-46), wheat bran (10-20), calcium carbonate (0.5-1.5), gypsum (0.5-1.5) and sucrose (0.5-1.5).    USE - Used as a mushroom culture medium.    ADVANTAGE - The method utilizes common agricultural and forestry waste for preparing the culture medium, has simple production procedures, is environmental-friendly, facilitates rapid growth while culturing mushroom, and produces good quality products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for (1) preparing the culture medium, comprising drying Eucalyptus tree waste wooden chip, banana residue and wheat bran, then crushing, and uniformly mixing all the above mentioned raw materials to obtain the product; and (2) culturing mushroom, comprising (i) preparing the culture medium by uniformly mixing all the above mentioned raw materials, and placing the produced raw materials in a plastic bag packets according to specification, (ii) sterilizing the plastic bag packets, and inoculating Lentinula edodes mycelium under sterile conditions, and (iii) removing material surface of the plastic bag which is completely covered with mycelium, maintaining the moisture content in air at 75-90%, temperature at 16.5-20.7 degrees C and the amount of carbon-di-oxide in the growing environment, accounts to 1400-2000 mg/l.
NOVELTY - Use of complex microbial inocula comprising Bacillus subtilis, Bacillus licheniformis and Bacillus mucilaginosus in bio-organic fertilizer for conserving soil water, is claimed.    USE - The complex microbial inocula is useful in bio-organic fertilizer for conserving soil water (all claimed).    ADVANTAGE - The microbial inocula: improves the soil structure, increases permeability, cut off the capillary limit and reduces water transpiration; provides large specific surface area between the bacteria colloidal complex and bacteria; and has good hydrophilicity and water-retaining properties, thus saving 30% of water and improving the yield per unit.
(BR201103089-A2)   NOVELTY - The absorbent material comprises fatty acids, derived crude glycerin, vegetable oil, silicone, amines, diisocyanate and water.    USE - Absorbent material for use in removal of oily wastewater.    ADVANTAGE - The absorbent material enables removing oily wastewater in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing absorbent material, which involves mixing fatty acids, derived crude glycerin, vegetable oil, silicone, amines, diisocyanate and water.
NOVELTY - A raw material of wood powder and/or grass powder is crushed to form wood powder of 50-100 meshes. The raw material comprises trunk, branch, bark, root and/or leaf of tree and/or grass. The wood powder or grass powder is dried. The dry wood powder or grass powder is compressed and molded by an annular mold to form particles. During compression and molding, oil lubricant with animal excrement or herbal medicine dreg is mixed with wood powder or grass powder, such that the wood powder or grass powder comprises lubricant (0.5-2.5%). The particles are cooled to obtain biofuel.    USE - Production of biofuel (claimed).    ADVANTAGE - The method enables efficient production of biofuel, without environmental pollution.    DETAILED DESCRIPTION - A raw material of wood powder and/or grass powder is crushed to form wood powder of 50-100 meshes. The raw material comprises trunk, branch, bark, root and/or leaf of tree and/or grass. The wood powder or grass powder is dried to control the moisture of wood powder or grass powder to 15-25%. The dry wood powder or grass powder is compressed and molded by an annular mold to form particles. During compression and molding through annular mould, oil lubricant with animal excrement or herbal medicine dreg is mixed with wood powder or grass powder, such that the wood powder or grass powder comprises lubricant (0.5-2.5%). The particles (0.5-2.5%) are cooled to obtain biofuel. An INDEPENDENT CLAIM is included for biofuel production equipment, comprises a crushing system, a drying system, a molding system, a lubricant supply system and cooling system.
NOVELTY - The tank (10) has a main reaction bath (20) that creates the organic acid from the organic waste flowed in from the outside. An auxiliary reaction bath (30) accommodates the organic acid generated in the main reaction bath. A fluid path (40) is installed between main reaction bath and auxiliary reaction bath. A sensor (24) is installed at the main reaction bath for measuring pH value of the organic waste. A controller (50) is provided for controlling opening and closing of the fluid path according to the pH value of the organic waste.    USE - Anaerobic digestion tank for treating organic waste generated from thickened sludge and food waste.    ADVANTAGE - Since the exhaustion due to the backflow of the organic acid flowed is prevented, the production of the methane gas can be optimized. Since the controller is provided for controlling opening and closing of the fluid path according to the pH value of the organic waste, the environmental contamination can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion tank.    Anaerobic digestion tank (10)    Main reaction bath (20)    Sensor (24)    Auxiliary reaction bath (30)    Fluid path (40)    Controller (50)
NOVELTY - Waste grease is used as raw material, resin-based solid acid is used as catalyst, and ester exchange reaction is carried out with low-grade fatty alcohol. The catalyst is filtered from the reaction mixture, separated, water-washed, alkali-washed, and distilled to obtain biodiesel fuel.    USE - Manufacture of biodiesel fuel.    ADVANTAGE - The biodiesel fuel is manufactured with high catalytic efficiency and high yield.
NOVELTY - A nine-grid building block type continuous production device comprises at least one nine-grid brickwork comprising nine dry distillation tanks constructed by nine grids and interlayer partition walls arranged around the dry distillation tanks. The interlayer partition walls comprise partition walls arranged around the dry distillation tanks. An interlayer hollow cavity is formed between two adjacent partition walls. A gate valve is arranged between the two open pores on interlayer hollow cavity. A dry distillation pot is arranged in each dry distillation tank.    USE - Nine-grid building block type continuous production device for producing carbon by biomass.    ADVANTAGE - The device ensures the continuity of the production, such that the production of carbon by biomass is not limited by the device and the environment. With the flexibility of the nine grids, the influence degree of the region and the season on the production of carbon by biomass is reduced to the minimum. The selectivity of the biomass raw material is completely rejected, even if in different seasons on the same region, thus the production capacity is improved with the improvement of the adaptability of the biomass raw material.
NOVELTY - A 2', 3'-di-O-acetyl-5'-deoxy-5-gemcitabine onium salt compound (I) is new.    USE - Compound (I) used for preparing capecitabine (claimed).    ADVANTAGE - The compound (I) has high chemical purity and stable quality, can be manufactured using an environment-friendly method with reduced reaction step and controlled cost, and can synthesize capecitabine with high yield and high purity.    DETAILED DESCRIPTION - A 2', 3'-di-O-acetyl-5'-deoxy-5-gemcitabine onium salt compound (I) is new.    X=acetate ion, nitrate ion, trifluoro acetic radical ion, alkyl benzene sulfonate ion, chlorine ion, bromine ion or iodine ion.
NOVELTY - The unit (400) has plasma torches (440a-440h, 440j, 440k, 440m) located within the unit in an arrangement that causes operation of the plasma torches to create a pyrolysis zone (445) increasing efficiency of the unit in breaking atomic bonds of hydrocarbon material e.g. coal, located within the unit during plasma pyrolysis process. A carbon dioxide recycle loop recycles carbon dioxide to the unit from synthetic gas preparation process of the unit and provides the carbon dioxide to one of the plasma torches in the unit and to a pyrolysis reactor chamber (425) of the unit.    USE - Hydrocarbon pyrolysis unit for breaking atomic bonds i.e. carbon-carbon bonds, of hydrocarbon material e.g. coal, lignite and petroleum solid coke, during plasma pyrolysis process to produce synthesis gas.    ADVANTAGE - The unit increases efficiency and reduces cost during synthesis gas production in an improved manner. The unit provides a membrane wall with an external cooling source to reduce temperature of a reactor vessel. The unit produces clean synthesis gas that does not require additional processing before the gas is sent downstream to currently existing synthesis gas-to-fuel technologies and reduces need to utilize an air separator unit (ASU) in a downstream synthesis gas-to-fuel processing facility, thus reducing capital cost in the synthesis gas-to-fuel facility and reducing a number of processor units that are required to produce fuel from synthesis gas.    DETAILED DESCRIPTION - The atomic bonds are carbon-carbon bonds. An INDEPENDENT CLAIM is also included for a method for operating a hydrocarbon pyrolysis unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrocarbon pyrolysis unit.    Hydrocarbon pyrolysis unit (400)    Pyrolysis reactor chamber (425)    Plasma pyrolysis chamber (430)    Plasma torches (440a-440h, 440j, 440k, 440m)    Pyrolysis zone (445)
NOVELTY - The gasifier (1) has a vertical vat (4) comprising, in series from top to bottom, an inlet (5) for a solid carbon fuel (2), an area (10) to pyrolyze the fuel to produce pyrolysis gases and char, an area (20) to combust the pyrolysis gases, an area (30) to reduce the char, a gas outlet (6), and an ash-collecting area (40). An active transfer unit is placed between the pyrolysis and combustion areas. The unit has a transfer airlock (50) to transfer the fuel from the pyrolysis area to the reduction area with the fuel being unable to flow directly from the pyrolysis area to the reduction area.    USE - Co-current fixed-bed gasifier for use in a gas production and combustion unit (claimed) to produce fuel gas from solid carbon fuel such as solid biomass e.g. wood shavings, for supplying the fuel gas to an internal combustion engine. Can also be used for supplying the fuel gas to a gas turbine, a boiler or a furnace.    ADVANTAGE - The transfer airlock transfers the fuel from the pyrolysis area to the reduction area with the fuel being unable to flow directly from the pyrolysis area to the reduction area, thus enabling better control of the flow rate of the solid matter between the two areas so as to reduce the amount of non-pyrolyzed fuel entering into the reduction area, and hence reducing the amount of tar present in the outlet gases.    DETAILED DESCRIPTION - The transfer airlock is permeable to the pyrolysis gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a co-current fixed-bed gasifier.    Co-current fixed-bed gasifier (1)    Solid carbon fuel (2)    Vertical vat (4)    Inlet (5)    Gas outlet (6)    Pyrolysis area (10)    Combustion area (20)    Reduction area (30)    Ash-collecting area (40)    Transfer airlock (50)
NOVELTY - Recombinant microorganism comprising a metabolic pathway in which metabolites are sequentially produced in a sequence of pyruvate, acetyl-coenzyme A, malonyl-coenzyme A and malonic semialdehyde, is new. The recombinant microorganism has undergone deletion or knockout of a gene encoding at least one enzyme containing of lactate dehydrogenase, phosphotransacetylase and alcohol dehydrogenase.    USE - The recombinant microorganism is useful for producing 3-HP (claimed) which is useful as a biofuel.    ADVANTAGE - The method increases malonyl-coenzyme A pools in a microbial cell (claimed) and prevents metabolite leak of an intermediate metabolite, thus increasing 3-HP production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing 3-hydroxypropionic acid (3-HP) in a recombinant microorganism, comprising: converting pyruvate into acetyl-coenzyme A; converting acetyl-coenzyme A into malonyl-coenzyme A; converting malonyl-coenzyme A into malonic semialdehyde; and converting malonic semialdehyde into 3-HP, where during the conversion of pyruvate into acetyl-coenzyme A, an activity of at least one enzyme containing of lactate dehydrogenase, phosphotransacetylase and alcohol dehydrogenase is inhibited in the microorganism.
NOVELTY - The system has an extraction unit (20) that extracts out the liquid oil from oil containing biomass. A gasification unit (60) generates the fuel gas from extraction residue after liquid oil is pressed out. A briquette portion (30) which produces briquette is provided by mixing dry biomass in dried condition with extraction residue. The gasification unit generates fuel gas by heating the briquette produced in briquette portion in state which restricts the air quantity.    USE - Fuel generation system.    ADVANTAGE - The production of tar can be suppressed effectively, when gasifying the extraction residue after squeezing liquid oil and obtaining fuel gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel generation system. (Drawing includes non-English language text)    Electric power generation system (1)    Drying unit (10)    Extraction unit (20)    Briquette portion (30)    Gasification unit (60)
NOVELTY - Synthesizing a biodiesel from natural lipid source containing lipids, comprises introducing the natural lipid source in an enclosure, rapidly heating the natural lipid source at a temperature (To), by water vapor to a total pressure (Po), for a treatment time (tr), successively making a relaxation to a pressure lowered by instant controlled relaxation to texture the natural lipid source and performing an in-situ transesterification to convert at least a portion of lipid contained in the natural lipid source in esters.    USE - The biodiesel is useful in a motor vehicle engine (claimed).    ADVANTAGE - The method provides biodiesel with improved quality and performance of in-situ transesterification for transforming lipids in ester, obtained by a direct and faster way, and with reduced energy cost due to the absence of extracting step.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) use of microalgae as natural lipid source for carrying out the above method; and    (2) the biodiesel obtained by the above method.
NOVELTY - Phosphorus contained in wastewater, which is a phosphorus generation source is adsorbed to a phosphorus recovery material consisting of an amorphous calcium-silicate group material, and recovered. Thus, recovery of phosphorus is enabled.    USE - Method for recovering phosphorus and producing phosphoric acid fertilizer (all claimed).    ADVANTAGE - Phosphorus is efficiently and economically recovered.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of phosphorus recovery system.    Sewage work (1)    Primary sedimentation basin (2)    Biological treatment tank (3)    Concentrator (6)    Storage tank (7)
NOVELTY - A raw fluid (F2) containing a biomass (M1) is supplied from an upstream edge (22a) towards a downstream edge (22b) in a raw fluid passage (22). The raw fluid is heated from the outer side of passage through reaction tube wall (21) using a heating medium (F1). The raw fluid passage comprises a gasification area (23) where a primary gasification reaction occurs in which at least portion of the biomass is gasified by heating conducted by medium (F1), and a gasification area (25). Additional heating of fluid (F2) is conducted by a heating medium (30) at the gasification area (25).    USE - Manufacture of gas for electric power generation system.    ADVANTAGE - Load is increased in biomass treatment and quality of the gas is improved.    DETAILED DESCRIPTION - A raw fluid (F2) containing a biomass is supplied from an upstream edge towards a downstream edge (22b) in a raw fluid passage separated from the outside by a reaction tube wall. The raw fluid of the raw fluid passage is heated from the outer side of the passage through the reaction tube wall using a heating medium (F1). The raw fluid passage comprises a gasification area (23) where a primary gasification reaction occurs in which at least portion of the biomass is gasified by heating conducted by the heating medium (F1), and a gasification area (25) disposed closer to the downstream edge (22b) than to the area (23). Additional heating of the raw fluid (F2) is conducted by a heating medium (30) at the gasification area (25). The temperature of the raw fluid is raised to 900-1100 degrees C by performing additional heating using a heating medium (30). An INDEPENDENT CLAIM is included for production apparatus of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of production apparatus of gas.    Reaction tube wall (21)    Raw fluid passage (22)    Upstream edge (22a)    Downstream edge (22b)    Gasification area (23,25)    Heating medium (F1,30)    Raw fluid (F2)    Biomass (M1)
NOVELTY - The gasifier (4) has an inlet (9) arranged in an upper area (12) of the gasifier for a biomass. Another inlet (14) is arranged in a lower area (13) of the gasifier for a gasification agent. An outlet (15) is provided in the upper area of the gasifier for a gasifier product gas. A temperature sensor (19) measures temperature of the gasifier product gas in the upper area of the gasifier. A moisturization unit moisturizes the biomass. A control circuit (21) activates the moisturization unit to moisturize the biomass when the temperature of the gasifier product gas exceeds maximum temperature.    USE - Updraft gasifier for use in a biomass gasification system of a stirling plant (claimed) to generate a gasifier product gas to be burned in a combustion unit to generate heat and electricity from biomass. Can also be used for a heating system of a building.    ADVANTAGE - The control circuit activates the moisturization unit to moisturize the biomass when the temperature of the gasifier product gas exceeds the maximum temperature, so that tar and dust residues in the gasifier product are separated and converted to ash, thus reducing dust content of the product gas and flue gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a stirling plant for generating heat and electricity from biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an updraft gasifier of a stirling plant.    Updraft gasifier (4)    Inlets (9, 14)    Upper area of gasifier (12)    Lower area of gasifier (13)    Outlet (15)    Temperature sensor (19)    Control circuit (21)
NOVELTY - Production of biofuels by co-processing of biomass in a refinery thermal processing unit, involves feeding a feed material to a thermal processing unit, where the feed material comprises a mixture of hydrocarbons and a solid biomass material; thermally processing the feed material; and collecting reaction products generated from the thermal processing of the feed material. The solid biomass material is derived from plant source, animal source or aquatic source. The reaction products include carbon dioxide, ammonia and acetic acid.    USE - For production of biofuels by co-processing of biomass in a refinery thermal processing unit (claimed).    ADVANTAGE - The method removes significant amount of reaction water from the coker operation, thus simplifying processing of resultant products; reduces the impact of the total enthalpy variance compared to non-biomass operations required in the coker; removes and recover water soluble acid components for the coker; and provides segregation of the acid water from the other coker water streams simplifies corrosion and treatment of the normal water streams in and from the delayed coker.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing isotropic coke, involving combining a feed material comprising a mixture of hydrocarbons and a solid biomass material; and subjecting the combined material to a thermal process to produce an isotropic coke.    DESCRIPTION OF DRAWING(S) - The figure shows flowchart of processing of biomass.
NOVELTY - Producing biogas from a starting material by an anaerobic fermentation process, comprises: providing a simulation model which at least partially describes the biological process steps and has specified input and output variables; determining current input variables at time (t); calculating a number of output variables from the current input values in the simulation model by varying at least one process parameter in a specified increment; selecting the process parameter associated with optimal gas yield and transferring to the associated process step; and repeating the process at time (t+ Delta t).    USE - The method is useful for producing biogas from a starting material by an anaerobic fermentation process.    ADVANTAGE - The method optimizes gas yield and can be carried out in cost-efficient manner.    DETAILED DESCRIPTION - Producing biogas from a starting material by an anaerobic fermentation process, comprises: providing a simulation model which at least partially describes the biological process steps and has specified input and output variables; determining the current input variables at time (t); calculating a number of output variables from the current input values in the simulation model by varying at least one process parameter in a specified increment; selecting the process parameter associated with the optimal gas yield and transferring to the associated process step; and repeating the process at time (t+ Delta t), where the amount of biogas produced is determined by process parameters, by which the gas yield is optimized.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a control circuit with the input variables, output variables, and process parameter for the passage, which is enclosed in the simulation model (Drawing includes non-English language text).
NOVELTY - The offset control arrangement has a voltage monitoring unit (142) that monitors input voltage of the load (146) to obtain monitoring information. A control processor (120) processes the monitored information. The offsetting source performs unidirectional shifting of fuel cell array output voltage to reduce voltage window apparent to the load on the basis of monitoring information and the processed monitoring information. A disconnecting unit disconnects the fuel cell array (103) from the load, when the disconnection is detected in the fuel cell system.    USE - Offset control arrangement for controlling voltage values in fuel cell system such as sold oxide fuel cell system for producing electricity with fuel cells.    ADVANTAGE - The efficiency and controllability of the fuel cell system can be improved and hence, the physical size of the fuel cell system can be more compact. The lifetime of the fuel cells can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for offset control method for controlling voltage values in fuel cell system for producing electricity with fuel cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the offset arrangement.    Fuel cell array (103)    Control processor (120)    Monitoring unit (142)    Load (146)    Filtering stage (150)
NOVELTY - The method involves contacting gas, which is obtained from a thermochemical gasification process of carbonaceous source materials, with a catalyst. The gas is contained with tar, tar-containing hydrocarbon, olefin, and/or sulfur-containing hydrocarbon. The tar, the tar-containing hydrocarbon and/or the olefin are converted into synthesis gas, and simultaneously the sulfur-containing hydrocarbon is converted into hydrogen sulfide in a single catalyst stage with only one catalyst type. The tar is contained with a mixture of cyclic and polycyclic aromatic compounds.    USE - Method for cleaning synthesis gas e.g. carbon monoxide and hydrogen, which is obtained from a thermochemical gasification process of carbonaceous source material e.g. coal and biomass, and is used for Fischer Tropsch (FT)-fuel, methanol and synthetic methane.    ADVANTAGE - The method reduces tar-/olefin content and sulfur-containing hydrocarbon content in the gas, and avoids the need for catalytic hydrogenation of the sulfur-containing hydrocarbon downstream to the catalytic tar reformation. The method avoids reduction of a service life of the catalyst, and the need for expensive regeneration and replacing of the catalyst. The method provides a high yield, and achieves a tar cleaning rate and a sulfur-containing hydrocarbon cleaning rate from 60 to 100 percentage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reactor arrangement.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for cleaning gas.'(Drawing includes non-English language text)'
NOVELTY - A yeast strain having improved acetyl-CoA synthetase (ACS) activity and acetyl-CoA acetyltransferase (ergosterol biosynthesis protein 10 (ERG10)) activity, is new.    USE - The yeast strain is useful for producing a substance, preferably metabolite which is involved in acetyl CoA cycle, more preferably isopropanol. The yeast strain is the crabtree-negative yeast, preferably Candida utilis (all claimed). The isopropanol is useful as biofuel.    ADVANTAGE - The yeast strain enables to produce isopropanol with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for cultivating the yeast strain.
NOVELTY - Using microwave carbon thermal municipal solid waste for preparing fuel gas comprises (A) pretreating and packing bulk of 1 month to 5 years of municipal solid waste to remove stone, soil and soil back, and extruding into garbage bag; (B) first cracking; (C) selecting and forming fixed carbon residue after processing, and passing separated fixed carbon; (D) heating fixed carbon at 1000-1800 degrees C under anaerobic environment, and continuously heating to generate alkane, alkyne, hydrogen, and carbon monoxide; (E) preheating carbon stack; and (F) performing gas purification.    USE - Method for using microwave carbon thermal municipal solid waste for preparing fuel gas.    ADVANTAGE - The method obtains harmless gas of large amount and high heat value. It has lower energy consumption and low operation cost.    DETAILED DESCRIPTION - Using microwave carbon thermal municipal solid waste for preparing fuel gas comprises (A) pretreating and packing bulk of 1 month to 5 years of municipal solid waste to remove stone, soil and soil back, and extruding into garbage bag; (B) first cracking; (C) selecting and forming fixed carbon residue after processing, and passing separated fixed carbon; (D) heating fixed carbon at 1000-1800 degrees C under anaerobic environment, and continuously heating to generate alkane, alkyne, hydrogen, and carbon monoxide; (E) preheating carbon stack; and (F) performing gas purification. The step (B) comprises putting standard garbage bag into microwave heating device, cracking at 300-800 degrees C. The step (E) comprises preheating carbon stack, cooling gas, and pre-heating carbon. The step (F) comprises cooling, and purifying to obtain slag harmless combustible gas.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram illustrating a method for using microwave carbon thermal municipal solid waste for preparing fuel gas (Drawing includes non-English language text).
NOVELTY - System comprises a septic tank, a homogenizing tank and an anaerobic fermentation device, where the septic tank is connected with the anaerobic fermentation device, the anaerobic fermentation device comprises an upflow blanket filter (UBF) composite anaerobic reactor, the anaerobic fermentation device is further connected with a sedimentation tank and a methane purifying device and the methane purifying device is connected with the methane generating device.    USE - The system is useful for processing excrement.    ADVANTAGE - The system is capable of processing the excrement without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing excrement comprising (a) collecting pig manure and urine of each day to enter the septic tank, removing the inorganic impurities and entering the homogenizing tank, uniformly stirring the mixture to obtain the mixed solution, (b) removing suspended substances in a mixed solution under the action of the gravity, dissolving the mixture and pumping into the UBF composite anaerobic reactor of the anaerobic fermentation device to carry out anaerobic fermentation to obtain methane slurry and methane residue, (c) making the methane slurry to enter the sedimentation tank, generating methane and entering into the methane purifying device to purified, generating electricity by the biogas generating device, warming the UBF composite anaerobic reactor, and generating the methane residue used as organic fertilizer for vegetable, grain field, orchard and grass.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a system for processing excrement (Drawing includes non-English language text).
NOVELTY - Conversion of a pre-treated lignin feed stream into a converted lignin stream, comprises: combining the pre-treated lignin feed stream, water (supplied from the pre-treated lignin feed stream and/or a source other than the pre-treated lignin feed stream), hydrogen (having a specified hydrogen pressure range at 25 degrees C) and a first catalyst, in a lignin conversion vessel; and maintaining the combination in the lignin conversion vessel at a first temperature in a specified temperature range for a time sufficient to create the converted lignin stream.    USE - The process is useful for conversion of a pre-treated lignin feed stream into a converted lignin stream for manufacturing a polyester bottle derived from lignocellulosic biomass (all claimed) for soft drinks, beer, other food and beverages, and packaged goods.    ADVANTAGE - The process is a single step process which converts the lignin to one of several possible organic steams.    DETAILED DESCRIPTION - Conversion of a pre-treated lignin feed stream into a converted lignin stream, comprises: combining the pre-treated lignin feed stream, water (supplied from the pre-treated lignin feed stream and/or a source other than the pre-treated lignin feed stream), hydrogen (having a specified hydrogen pressure range at 25 degrees C) and a first catalyst, in a lignin conversion vessel; and maintaining the combination in the lignin conversion vessel at a first temperature in a specified temperature range for a time sufficient to create the converted lignin stream, where the pre-treated lignin feed stream comprises lignin, the converted lignin stream has a composition comprising aromatic compounds (reformate), and the total area of the aromatic compounds (reformate) under a gas chromatography (GC)/mass spectrometry (MS) curve of the converted lignin stream is 60-95%.
NOVELTY - Tert-butyl N-((2S)-3-chloro-2-hydroxypropyl)carbamate and methyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate or 4-nitrophenyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate are subjected to condensation reaction to obtain tert-butyl N-(((5S)-2-oxo-3-(4-(3-oxomorpholin-4-yl)phenyl)-1,3-oxazolidin-5-yl)methyl)carbamate. The obtained carbamate compound is deprotected, to obtain 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one.    USE - Preparation of morpholine derivative used as intermediate for preparing rivaroxaban.    ADVANTAGE - The method economically provides morpholine derivative under mild condition, without polluting the environment.    DETAILED DESCRIPTION - Tert-butyl N-((2S)-3-chloro-2-hydroxypropyl)carbamate and methyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate or 4-nitrophenyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate are subjected to condensation reaction to obtain tert-butyl N-(((5S)-2-oxo-3-(4-(3-oxomorpholin-4-yl)phenyl)-1,3-oxazolidin-5-yl)methyl)carbamate. The obtained carbamate compound is deprotected, to obtain 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one, or (2S)-1-chloro-3-((E)-(phenylmethylidene)amino)propan-2-ol and 4-nitrophenyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate are subjected to condensation reaction to obtain 4-(4-((5S)-2-oxo-5-(((E)-(phenylmethylidene)amino)methyl)-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one. The obtained morpholine compound is hydrolyzed to obtain 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one. INDEPENDENT CLAIMS are included for the following:    (1) tert-butyl N-(((5S)-2-oxo-3-(4-(3-oxomorpholin-4-yl)phenyl)-1,3-oxazolidin-5-yl)methyl)carbamate; and    (2) 4-(4-((5S)-2-oxo-5-(((E)-(phenylmethylidene)amino)methyl)-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one.
NOVELTY - An electrolyte solution contains an ionic compound having tricyano methide anion and a cation (I), and a nitrogen-containing organic compound (II).    USE - Electrolyte solution is used for electrolytic capacitor (claimed). Uses include but are not limited to battery such as primary battery and secondary battery, electrical double layer capacitor, solar cell, electrochromic display element and fuel cell.    ADVANTAGE - The electrolytic capacitor using the electrolyte solution has excellent charging/discharging characteristics, and low impedance characteristics in high frequency region and reduced product swelling at the time of solder reflow.    DETAILED DESCRIPTION - An electrolyte solution contains an ionic compound having tricyano methide anion and a cation of formula: Rs-LH+ (I), and a nitrogen-containing organic compound of formula (II).    L=carbon, silicon, nitrogen, phosphorus, sulfur, or oxygen;    R=monovalent element, functional group or organic group;    s=2,3 or 4;and    R1-R4=H, 1-8C hydrocarbyl, acetyl, alkoxy or carbonitrile.    When at least two of R1-R4 is hydrocarbyl, those hydrocarbyl optionally have structure by directly coupling. An INDEPENDENT CLAIM is included for electrolytic capacitor.
NOVELTY - A bio-component diesel fuel production method involves performing hydroconversion process on natural originated raw material containing fatty oil and/or fat in the presence of catalyst and administering hydrogen to obtain a modified material. The obtained modified material is subjected to hydroconversion of paraffin in the presence of hydrotreating catalyst, preferably nickel-molybdenum material or cobalt-molybdenum material at pressure of 2.0-9.0 MPa, space velocity of 0.5-5.0 h-1 and temperature of 300-450 degrees C and feeding hydrogen gas to the raw material to obtain finished product.    USE - Method for producing bio-component diesel fuel.    DETAILED DESCRIPTION - A bio-component diesel fuel production method involves performing hydroconversion process on natural originated raw material containing fatty oil and/or fat in the presence of catalyst comprising hydrogen form of zeolite (ZSM-5) at 150-460 degrees C under pressure of 0.1-3.0 MPa and space velocity of 0.5-5.0 h-1 and administering hydrogen at rate of 150-1000 Nm3/m3 of material to obtain a modified material. The obtained modified material is subjected to hydroconversion of paraffin in the presence of hydrotreating catalyst, preferably nickel-molybdenum material or cobalt-molybdenum material at pressure of 2.0-9.0 MPa, space velocity of 0.5-5.0 h-1 and temperature of 300-450 degrees C and feeding hydrogen gas to the raw material in an amount of 150-1000 Nm3/m3 of material to obtain finished product.
NOVELTY - A refined biogenic fuel additive composition comprises (in mole %) combustion modifier (90) and ash softening modifier (5-100), where the ash softening modifier comprises waste wood, vegetable oil pomace, straw, hay and grass seed husk and fossil fuels and the fossil fuel is granular coal, coal dust, lignite and peat. The combustion modifier comprises solid fuel biocide (10-300 mg/kg) and a solvent (0-50,000 mg/kg). The solvent comprises water soluble emulsifier or organic solvent (5-100 mg/kg) in the fuel.    USE - Refined biogenic fuel additive composition.
NOVELTY - Compost deodorizing device comprises many composting grooves, a gas distribution device, a gas collecting device, a fresh air device and a deodorizing device, which are connected to each other. An opening of each composting groove is provided with a movable cover, and a sealing bar. The sealing bar is arranged between the movable cover and composting groove. The device is further provided with a lifting mechanism for lifting the movable cover.    USE - Used as a compost deodorizing device.    ADVANTAGE - The device saves construction cost, and reduces the operation cost, while carrying out the process of compost, and thus it is economical.
NOVELTY - An aqueous solution of vinyl ether and hydrogen peroxide are oxidized in presence of a mixed catalyst containing palladium catalyst having monodentate phosphine ligand, and amines to obtain acetate ester.    USE - Manufacture of acetate ester used as intermediate for pharmaceuticals and electronic materials.    ADVANTAGE - The method safely and efficiently provides acetate ester with high yield under mild conditions by a simple and environmentally-friendly process. The usage amount of catalyst is reduced. The discharge amount of palladium metal as by-product is reduced. Since reaction can be effectively advanced only using a catalytic amount of palladium and amine, the method is economical and nontoxic with respect to environment and human body.
NOVELTY - Reaction kettle comprises a reaction kettle body and a sealing cover. The reaction kettle is wound with a coil set on the outer side of the reaction kettle wall of the reaction kettle body.    USE - The reaction kettle is useful for separating and recycling magnetic catalyst in preparing biofuel.    ADVANTAGE - The reaction kettle can separate solid-liquid phase catalyst.
NOVELTY - The device comprises a biomass raw material pre-treating system, a biomass dry distilling and cracking system, a gas and carbon powder separating and purifying system, a gas storing and transporting system, a carbon powder cooling and collecting system and a waste heat using system. The biomass dry distilling and cracking system comprises multiple rows of destructive dry distilling and cracking sleeve, a heater and a variable frequency speed regulating motor. Each row of dry distilling and cracking sleeve is provided with a spiral feeder and an exhaust passage.    USE - A device with gas channel of multi-pipe spiral biomass dry distillation cracking for preparing gas.    ADVANTAGE - The device will not cause overflow gas to influence the normal production, can realize large scale industrial production, and reduces production cost and energy consumption.
NOVELTY - The device has purifying tube whose air inlet opening is provided with a gas-guide tube. An air outlet opening of a tar pyrolysis chamber of a reaction cylinder is provided with a tar pyrolysis tube. A tar backflow control valve is placed on an oil return pipe. A separating barrel is provided with a purifying cylinder. The purifying cylinder is provided with a secondary heat air pipe. A return opening of the purifying cylinder is provided with a reflowing pipe and connected with a circulating water outlet opening of a gas separating cylinder.    USE - Tar reflux biomass fuel gas utilization device.    ADVANTAGE - The device is simple to operate, easy to use, environment-friendly and convenient to install and maintain, and has low failure rate, prolonged service life, high energy saving effect and low carbon and emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tar reflux biomass fuel gas utilization device.
NOVELTY - Processing of forest waste briquette involves mixing wood raw material particles or forest raw material particles of same particle size, extruding to cylinder or polygonal shape with irregular section.    USE - Processing of forest waste briquette.    ADVANTAGE - The method efficiently and economically processes forest waste briquette with high heat value without generating carbon monoxide and without using additive and using simple process.
NOVELTY - A substrate is provided into a plate-and-frame filter press, concentrated sludge is added to the moisture content of lime solution and ferric solution and provided to the plate-and-frame filter press, to obtain sludge filter cake. The obtained sludge filter cake piling triangle heaps is dried and dewatered, and ventilation opening is set at the lower portion of the air after the sludge stack temperature is raised. The water content of sludge is 30% or less. Garbage is provided into a double-spiral stirring mill, added and mixed in the rolling-type compression molding machine.    USE - Production of refuse-derived fuel.    ADVANTAGE - The refuse-derived fuel is efficiently and economically produced.    DETAILED DESCRIPTION - A substrate is provided into a plate-and-frame filter press, concentrated sludge (98%) is added to the moisture content of lime solution (1-2%) and ferric solution (0.5-1%) and provided to the plate-and-frame filter press, to obtain sludge filter cake. The obtained sludge filter cake piling triangle heaps is dried and dewatered, and ventilation opening is set at the lower portion of the air after the sludge stack temperature is raised to more than 55 degrees C. The water content of sludge is 30% or less. Garbage is provided into a double-spiral stirring mill, added and mixed in the weight ratio of 1:3 in the rolling-type compression molding machine. The water content of sludge filter cake is 45-50%.
NOVELTY - A self-heating type biomass quickly pyrolyzing and liquefying device comprises a combustion furnace, a spiral feeder, a fluidized bed reactor, a heating jacket, a cyclone separator, a condensing tower, a flue gas heat exchanger, a second heat exchanger and a circulating fan. The cyclone separator is connected with the fluidized bed reactor top part, and outlet is connected with the condensing tower. Upper part of the condensing tower noncondensable gas outlet is respectively connected with the first and the second heat exchangers.    USE - A self-heating type biomass quickly pyrolyzing and liquefying device.    ADVANTAGE - The device can recycle heat of high temperature flue gas, which effectively uses waste heat of flue gas, which greatly reduces operation energy consumption of equipment and saves energy. Production process is easy to control.
NOVELTY - A high-clean alcohol hydrocarbon liquid fuel for automotive comprises (in volume%) refined alcohol (20-50), raw material oil (50-80), alcohol denaturant (0.8-1.5). The refined alcohol is refined methanol of (more than 99%). The raw material oil is pyrolysis gasoline or naphtha. The alcohol denaturant is tertiary butanol (3-4), dimethyl carbonate (7.5-9.5), isobutyl alcohol (8.5-10.5), dichloroethane (1-3), mixed xylene (22-26), diethyl ether (8-9.5), butanone (15-18), tetrahydropyridine (0.5-1) or metallic corrosion inhibitor (CI-1405) (0.5-1).    USE - High-clean alcohol hydrocarbon liquid fuel is used for automotive components.    ADVANTAGE - The high-clean alcohol hydrocarbon liquid fuel is environmentally-friendly, and discharges reduced amount of harmful substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of high-clean alcohol hydrocarbon liquid fuel. Raw material of the alcohol denaturant is added to stirred vessel made of stainless steel, stirred, temperature is controlled to 10-20 degrees C for 60 minutes, sealed and stored for 12 hours after stirring. The alcohol denaturant finished product is added to alcohol denaturant storage tank with a double filter. The refined methanol is added to methanol modification stirring pot made of stainless steel, and adding alcohol denaturant (0.8-1.5%) is added, stirred for 120 minutes, sealed and stored for 2 hours. Modified methanol is added to the methanol modification storage tank standby with a single filter and raw material oil (50-80%) is conveyed to the production stirred vessel made of carbon steel. The modified methanol production stirred vessel, sealed and stored for 2 hours for 240 minutes and conveyed to the finished product pot, to obtain high-clean alcohol hydrocarbon liquid fuel.
NOVELTY - The apparatus has an absorption tower (60) that produces electricity by supplying the fuel to a generator (70). A rice hull absorption tower fills the rice hulls in the absorption tower and removes the impurity using the synthetic gas. The carbide absorption tower and sand absorption tower are provided to fill the carbide and sand in carbonization furnace (10). A condenser (30) is provided for condensing the synthetic gas ejected in the carbonization furnace to produce the rice hull charcoal by extracting pyroligneous liquor.    USE - Production apparatus of renewable energy using synthesis gas of rice hulls carbonization system.    ADVANTAGE - The renewable energy can be efficiently produced using synthesis gas of rice hulls carbonization system, so that the electric power can be produced simply and easily at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the renewable energy production apparatus.    Carbonization furnace (10)    Condenser (30)    Electrostatic dust collector (50)    Absorption tower (60)    Generator (70)
NOVELTY - The method involves mixing medical waste, biomass gasification auxiliary material and water content uniformly to get the mixed materials, where the medical waste includes absorbent cotton, an infusion bottle, an infusion tube, a blood of clothes and household rubbish. The mixed materials are poured to a medical waste gasification furnace, and a tube cover (14a) is covered. Temperature of the bottom of the gasification furnace is maintained at 900 to 1500 degrees centigrade. Water gas is conveyed into a gas burning tower (17) by a water gas conveying pipe (16) to generate raw fuel gas.    USE - Medical waste innoxious gasification and processing method.    ADVANTAGE - The method enables saving transportation and treatment cost and improving social benefit and environmental protection benefit.    DETAILED DESCRIPTION - The biomass gasification auxiliary material includes straw, waste wood particle, saw dust, rice hull, city garden branch crushed material and semi-carbonizing substance.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a medical waste gasification furnace.    Top cover (1)    Locating plate (2)    Tube cover (14a)    Water gas conveying pipe (16)    Gas burning tower (17)
NOVELTY - The method involves carrying out biomass fuel combustion and self-maintenance process, and emitting a large amount of heat in a petroleum fraction hydrogenation process to generate hydrogen, carbon monoxide, methane and combustible gas. Combustion heat is collected in the petroleum fraction hydrogenation process through heating medium. Combustible gas combustion heat is absorbed by continuously raising temperature. High temperature heat transfer agent is converted directly into electrical energy by temperature difference through carrying heat energy at shallow ground.    USE - Composite electricity generating method for a distributed energy system.    ADVANTAGE - The method enables utilizing the composite of biomass energy so as to improve the energy utilization rate. The method enables avoiding utilization of moving parts so as to realize high reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a structure for implementing a composite light generating method.
NOVELTY - An adsorbent consists of core unit and shell unit containing component having higher absorption capability than component in core unit, and in the ratio higher than the content of the component in the core unit.    USE - Adsorbent for removing acid gas e.g. hydrochloric acid gas in mixture of hydrogen and hydrocarbon gas (claimed) in petroleum refining industry.    ADVANTAGE - The adsorbent has excellent adsorption performance, high reactivity and is manufactured economically.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of adsorbent; and    (2) method for removing acid gas in mixture of gas.
NOVELTY - Heat accumulating biomass pyrolysis by processing pretreatment to biomass material to obtain raw material for biomass pyrolysis; spreading the biomass raw material after treating in a rotating bed bottom of heat accumulating type fuel gas radiant tube rotating bed; and collecting the gas, and processing condensation to separate the pyrolysis gas and condensable liquid.    USE - Method for the heat accumulating biomass pyrolysis (claimed).    ADVANTAGE - The method provides large-scale production with low operating cost and total energy consumption.    DETAILED DESCRIPTION - Heat accumulating biomass pyrolysis comprises:    (A) processing pretreatment to biomass material to obtain raw material for biomass pyrolysis; spreading the biomass raw material after treating in a rotating bed bottom of heat accumulating type fuel gas radiant tube rotating bed, where raw material is heated in an airtight apace along with the rotation of rotating bed bottom for 30-120 minutes at 200-800 degrees C, producing gas object and solid biochar, providing heat of rotating bed by heat accumulating gas radiant tube in rotating bed, and isolating the smoke in radiant tube with the gas object in the rotating bed; and    (B) collecting the gas, and processing condensation to separate the pyrolysis gas and condensable liquid, where pyrolysis gas is for fuel of heat accumulating fuel gas radiant tube; discharging the solid biochar and collecting after processing quenching and cooling.    An INDEPENDENT CLAIM is included for a heat accumulating type biomass pyrolysis system.
NOVELTY - Method for producing fuel from waste wood, involves (a) obtaining waste wood as raw material, (b) crushing the raw material using a crusher, where the crushed particle has particle size of 3 mm, (c) adding the crushed product in a feeding device, and conveying the crushed product to a pressing machine, and (d) softening the pressed product at high temperature, maintaining softening temperature at 120-130 degrees C, and extruding the obtained product using extruding machine to obtain finished product.    USE - The method is useful for producing fuel from waste wood, which is used for industrial boiler.    ADVANTAGE - The method is environmentally-friendly, convenient to perform and cost-effective, and saves energy.
NOVELTY - A biphenyl-type compound (I) is to petroleum hydrocarbon or liquid as marker.    USE - Method for marking petroleum hydrocarbon or liquid biologically derived fuel e.g. petroleum hydrocarbon, biodiesel fuel or ethanol fuel (all claimed) and additive package e.g. antiwear additive for lubricants and detergent for gasoline.    ADVANTAGE - The method of marking petroleum hydrocarbon or liquid biologically derived fuel is efficiently enabled.    DETAILED DESCRIPTION - A biphenyl-type compound of formula (I) is to petroleum hydrocarbon or liquid as marker.    R1,R2=H or 1-4C alkyl;and    G=H or substituent chosen from 1-8C alkyl or 1-8C alkoxy.
NOVELTY - An ether derivative (I) is new.    USE - New ether derivative used for marking petroleum hydrocarbon and liquid biologically-derived fuel. Uses include but are not limited to biodiesel fuel, ethanol, butanol, hydraulic fluid, brake fluid, diesel fuel, kerosene and oil.    ADVANTAGE - The marker formed using the ether derivative has excellent stability.    DETAILED DESCRIPTION - An ether derivative of formula: (Ph3C)mAr(OR)n (I) is new.    Ph=phenyl;    Ar=aromatic ring containing 6-20 carbon atoms;    R=1-18C alkyl or 7-12C aralkyl;    m=1 or 2;and    n=1-4.    An INDEPENDENT CLAIM is included for marking petroleum hydrocarbon and liquid biologically-derived fuel.
NOVELTY - Producing alcohol from a cellulosic biomass material, comprises adding a genetically modified microorganism to a fermentation mixture comprising a cellulosic biomass material and/or fermentation substrates derived from the cellulosic biomass material, where the genetic modification to the microorganism comprises introduction of an expression vector comprising the coding sequence of a protein of the Sm-like superfamily, and where the genetic modification results in elevated tolerance to stress or at least one inhibitor as compared to without the genetic modification.    USE - The method is used for producing alcohol from a cellulosic biomass material (claimed).    ADVANTAGE - Genetically modified strains of microorganisms that display enhanced tolerance to stress and/or inhibitors such as sodium acetate and vanillin are provided.    DETAILED DESCRIPTION - Producing alcohol from a cellulosic biomass material, comprises (a) adding a genetically modified microorganism to a fermentation mixture comprising a cellulosic biomass material and/or fermentation substrates derived from the cellulosic biomass material, where the genetic modification to the microorganism comprises introduction of an expression vector comprising the coding sequence of a protein of the Sm-like superfamily, and where the genetic modification results in elevated tolerance to stress or at least one inhibitor as compared to without the genetic modification; (b) allowing the microorganism to ferment and produce alcohol; and (c) recovering alcohol produced by fermentation with the microorganism.
NOVELTY - The litter has milled corn spindles with grain size of 8 mm to 12 mm, where the litter has bulk density of particularly 300 kilogram per meter cube up to 330 kilogram per meter cube. The litter contains effective microorganisms such as mixture of lactic acid bacterium, yeast and/or consists of non-sulfur purple bacterium. The litter comprises moisture of less than 14 percentage. The litter uses fermentation of metabolic products such as herb essences, organic acids, anti-oxidants and enzymes. A raw material of the corn spindles is left at a field.    USE - Litter for poultry farming or for mast flow in a poultry mast i.e. intensive livestock farming (all claimed), for a farm animal. Uses include but are not limited to chicken, cockerel, turkey, duck, goose and dove.    ADVANTAGE - The milled corn spindles have grain size of 8 mm to 12 mm, thus optimizing absorbency, minimizing development of fine particulates, and improving efficiency of the poultry mast by reducing failures based on violations and diseases of the animals. The utilization of the effective microorganisms such as mixture of lactic acid bacterium, yeast and/or consists of non-sulfur purple bacterium, prevents medicament utilization, thus avoiding growth of unwanted organisms in the litter, and strongly reducing harmful gas, and hence meeting requests of animal welfare by improving health protection of the animals during breeding of the animals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a litter for poultry farming or for mast flow in a poultry mast i.e. intensive livestock farming.
NOVELTY - Genetically enhanced cyanobacterium producing a first chemical compound comprising: a genetically enhanced genome with a first gene inactivation in a first essential or conditionally essential gene of the cyanobacterium, and a first extrachromosomal plasmid harboring the first essential or conditionally essential gene and at least one first production gene for production of the first chemical compound, where the cyanobacterium lacks a functional gene conferring biocide resistance, is new.    USE - The genetically enhanced cyanobacterium is useful for producing a first chemical compound. The first chemical compound is selected from alcohols, alkanes, polyhydroxyalkanoates, e.g. PHB, fatty acids, fatty acid esters, carboxylic acids, such as amino acids, terpenes and terpenoids, peptides, polyketides, alkaloids lactams, such as pyrrolidone, and ethers, such as THF or their combination. The first chemical compound is a biofuel selected from alkanols, fatty acids, fatty acid esters, alkenes and alkanes (all claimed).    ADVANTAGE - Genetically enhanced cyanobacteria lacking functional genes conferring biocide resistance for the production of chemical compounds are provided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing a first chemical compound, by (a) culturing a genetically enhanced cyanobacterium above in the absence of a biocide, the cyanobacterium producing the first chemical compound, and (b) recovering the first chemical compound; and    (2) a method for producing genetically enhanced cyanobacteria above.
NOVELTY - Methane fermentation waste water is denitrified by storing organic waste crushed material from acceptance tank to storage tank, collecting organic waste water produced during storage of organic waste or organic waste crushed material in acceptance tank or storage tank to collection tank, fermenting organic-waste crushed material with methane after collecting organic waste water, and adding and denitrifying organic waste water produced during methane fermentation.    USE - Denitrification of methane fermentation waste water.    ADVANTAGE - Clogging is prevented, and use of methanol as hydrogen donor in denitrifying process is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram explaining the collection location of organic waste water. (Drawing includes non-English language text).    Acceptance layer (1)    Crushing apparatus (2a)    Storage tank (3)    Collection tank (4)    Methane fermentation tank (5)
NOVELTY - A siloxane removal process involves making siloxane in source gas to contact activated alumina in presence of water, and removing by decomposing into silicon oxide and methane.    USE - Siloxane removal process for methane recovery process (claimed).    ADVANTAGE - The siloxane is easily removed. The apparatus scale can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane recovery process involving reaction removal process which the hydrogen sulfide in biogas is made to react with metal oxide, and is removed as metal sulfide, decompose-removing process by making the siloxane in biogas contact activated alumina in presence of water, and decomposing into silicon oxide and methane, and concentration process which separates the carbon dioxide in biogas and concentrating methane by pressure-swing-adsorption process.
NOVELTY - Empty fruit bunch (EFB) is crushed (S101), and lignin is added (S103) to EFB crushed material. The resultant material is aggregated, compressed and clumped (S105) to obtain biomass fuel.    USE - Manufacture of biomass fuel used in circulating fluidized-bed boiler.    ADVANTAGE - The method efficiently provides biomass fuel having excellent clumping property, by simple method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacture of biomass fuel. (Drawing includes non-English language text)    Crushing process (S101)    Lignin addition process (S103)    Clumping process (S105)
NOVELTY - Method for pre-treating organic waste, involves using at least one microorganisms which produce enzyme chosen from cellulase, protease, and amylase, and culturing the microorganisms at allowable temperature for 4 hours or less.    USE - The method is useful for isolating foreign material from organic waste for pre-treating organic waste (all claimed).    ADVANTAGE - The method pre-treats organic waste even in reduced pressure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for isolating foreign material from organic waste.
NOVELTY - A biomass is pretreated by contacting the biomass with ionic liquid under pressure for sufficient time.    USE - Pretreatment process of biomass for production of fuel alcohol.    ADVANTAGE - Glucose yields are improved while reducing energy requirement, processing temperature and processing time.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the glucose yield for selected substrate as a function of pressure.
(HU201100098-A1)   NOVELTY - Microorganisms containing preparation for biodegradation of biomass containing toxic or hazardous active agent residues of the pharmaceutical industry; and for composting biologic substances, comprises microorganisms from one or more out of mixed cultures deposited in the National Collection of Agricultural and Industrial Microorganisms under the numbers NCAIM 135/2010, NCAIM 136/2010 or NCAIM 137/2010, or one or more microorganisms belonging to these mixed cultures, expediently the mixed culture of Biomass Pharma NCAIM (P) Mix 001378.    USE - The microorganisms containing preparation is useful for biodegradation of biomass containing toxic or hazardous active agent residues of the pharmaceutical industry, biogas production and/or bioethanol-biodiesel production; for composting biologic substances; and for purposive biological treatment and transformation of optimally composed mixture of agriculture remnants (claimed).    DETAILED DESCRIPTION - Microorganisms containing preparation for biodegradation of biomass containing toxic or hazardous active agent residues of the pharmaceutical industry, biogas production and/or bioethanol-biodiesel production; for composting biologic substances; and for purposive biological treatment and transformation of optimally composed mixture of agriculture remnants, comprises microorganisms from one or more out of mixed cultures deposited in the National Collection of Agricultural and Industrial Microorganisms under the numbers NCAIM 135/2010, NCAIM 136/2010 or NCAIM 137/2010, or one or more microorganisms belonging to these mixed cultures, expediently the mixed culture of Biomass Pharma NCAIM (P) Mix 001378, optionally along with biologically compatible carrying materials.
NOVELTY - Macrocyclic compounds (I) are new.    USE - (I) are useful in catalysis for: forming oxygen gas or hydrogen gas from water; reducing carbon dioxide (all claimed); forming syngas; and oxidation of organic substrates such as methanol and carbon monoxide.    ADVANTAGE - (I): comprises at least one substituent that aids in increasing its water solubility; and exhibits enhanced hydrogen evolution reaction efficiency.    DETAILED DESCRIPTION - Macrocyclic compounds of formula (X1-Y1) (I) are new.    X1 = macrocycle having 2-7 heteroatoms positioned such that at least some of the heteroatoms are able to coordinate a metal or a semi-metal within a central binding cavity of the macrocycle, where at least one beta-position of the macrocycle is an electron-withdrawing group comprising halo, nitro or cyano; and    Y1 = optionally substituted pendent group.    INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) a method of catalysis, comprising providing (I), where at least one metal atom is coordinated by the macrocycle and/or the pendent group, and exposing the composition to a reactant, where a product is formed from the reactant following application of a voltage to the composition.
NOVELTY - The method involves providing thermosetting resin which contains an epoxy resin. A curing agent contains a phenol-type compound and the graphite particles are contained. The equivalence ratio of the epoxy resin, with respect to the phenol-type compound prepares the composition for molding, is in the range of 0.8 to 1.2. The molded object is produced by molding the composition for molding. The surface of the molded object is processed with ozone gas.    USE - Manufacturing method for fuel cell separator (claimed).    ADVANTAGE - Maintains the hydrophilic property for long period of time while providing high hydrophilic property on the surface of a separator, prevents the channel for gas supply discharge from being occluded by the water droplet, and maintains high electric power generation efficiency of fuel cell since the equivalence ratio of the epoxy resin, with respect to the phenol-type compound prepares the composition for molding, is set in the range of 0.8 to 1.2.    DESCRIPTION OF DRAWING(S) - The drawing shows a disassembled perspective view of the single cell structure of the fuel cell. (Drawing includes non-English Language Texts).    Channel for gas supply discharge (2)    Fuel cell separator (20)    Fuel manifold (131)    Oxidizing agent manifold (132)    Cooling manifold (133)
NOVELTY - Processing ammonium-containing substances of biogenic origin, comprises evaporating water from the biogenic materials e.g. liquid manure, digestate, sewage sludge etc. by uniform entry into hot alkaline model, and simultaneously hydrolyzing the organic component and converting into a true solution.    USE - The method in processing biogenic substances with low water content is useful as an alternative to biogas plant for power supply (claimed). The method is useful for processing ammonium-containing substances of biogenic origin.    ADVANTAGE - The method: produces biogas having no liquid ammonium-containing byproduct (claimed); provides a hygienically safe energy recovery from animal meal without the need for flue gas treatment; maintains the fertilizer value; and converts the fertilizer main components of phosphorus, sulfur and nitrogen into a commercially usable form.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a processing plant.    Stirrer tank (1)    Filter (2)    Heat exchanger (3)    Gasification unit (4)    Vapor compressor (6)
NOVELTY - Cucumber special bio-organic fertilizer comprises basic fertilizer and additional fertilizer. The basic fertilizer comprises rotten chicken manure, peat, weathered coal, molasses powder, urea, diammonium hydrogen phosphate, potassium sulfate and kaolin, and further comprises Bacillus megaterium, B. mucilaginosus and Paenibacillus polymyxa. The additional fertilizer comprises rotten chicken manure, peat, weathered coal, molasses powder, urea, potassium sulfate and kaolin, and further comprises B. megaterium, B. mucilaginosus and P. polymyxa.    USE - The bio-organic fertilizer is useful promoting the cucumber growth, improving the cucumber yield, and reducing the morbidity of cucumber by soil-borne diseases.    DETAILED DESCRIPTION - Cucumber special bio-organic fertilizer comprises a basic fertilizer and an additional fertilizer. The basic fertilizer comprises (in parts by wt.) rotten chicken manure (300-600), peat (50-200), weathered coal (50-200), molasses powder (50-100), urea (0-50), diammonium hydrogen phosphate (10-100), potassium sulfate (100-200) and kaolin (20-100), and further comprises (in colony-forming units/g basic fertilizer) Bacillus megaterium (200-1000 million), B. mucilaginosus (1000-5000 million) and Paenibacillus polymyxa (2000 million-1 billion). The additional fertilizer comprises (in parts by wt.) rotten chicken manure (300-500), peat (50-200), weathered coal (50-200), molasses powder (50-100), urea (100-150), potassium sulfate (150-250) and kaolin (20-100), and further comprises (in colony-forming units/g additional fertilizer) B. megaterium (100-500 million), B. mucilaginosus (500-2000 million) and P. polymyxa (1000-5000 million). An INDEPENDENT CLAIM is also included for preparing the cucumber special bio-organic fertilizer, comprising weighing each component, and mixing uniformly.
NOVELTY - Biological compound fertilizer 8-15 wt.% of powder livestock excrement, 55-65 wt.% of powder poultry excrement, 8-12 wt.% chaff, wane and straw, 2-5 wt.% of medical stone, zeolite, tourmaline, precious stones, phyllite and weathered coal, and 0.3-0.4 wt.% of brown seaweed extracting liquid.    USE - The fertilizer is useful for promoting plant growth and improving the soil texture.    ADVANTAGE - The fertilizer can be easily absorbed by the crop and has high quantity of various trace elements and amino acids.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the biological compound fertilizer comprising airing the livestock excrement, grinding and sieving the ground particle via 100-150 meshes; airing the poultry excrement, grinding and sieving the ground particle via 100-150 meshes; grinding the chaff, wane, and straw, sieving the ground particle via 100-150 meshes; grinding the medical stone, zeolite, tourmaline, precious stones, phyllite and weathered coal and sieving the ground particle via 200-300 meshes; dosing the above components in a special sitter; weighing the brown seaweed extracting liquid, introducing into the sprayer, spraying the brown seaweed extracting liquid in the stirring material via a sprayer and stirring for 20-25 minutes; mixing the above components under uniform stirring, unloading the mixture in a stacking place, piling up to about 2 m, turning the stack for once per 2 days, repeating the turning step for 5-6 times, airing the mixture and packaging.
NOVELTY - A methane is prepared from synthetic gas by placing synthetic gas into reactor with catalyst for reaction at 200-500 degrees C and 0.1-7 MPa with reaction volume space velocity of 1000-50000 to prepare methane and co-produce oil product. The catalyst comprises catalyst (1) (5-80 wt.%) and catalyst (2), prepared by physical mixing. Catalyst (1) is nickel-based catalyst and catalyst (2) is cobalt-based catalyst.    USE - Method for preparing methane from synthetic gas and co-producing oil product (claimed).    ADVANTAGE - The method makes use of synthetic gas as raw material which has extensive source. The used catalyst is of low cost, simple preparation, and high efficiency.
NOVELTY - Preparation of composite flocculant comprises dissolving chitosan (CTS) in 1 vol.% acetic acid aqueous solution so as to prepare 3 g/L storage solution, adding polysilicate aluminum ferric chloride (PSAFC) solution under magnetic stirring, dripping 10% diluted hydrochloric acid or 10% sodium hydroxide to adjust pH value, strenuously stirring the mixture to mix uniformly, slowly heating to reaction temperature, reacting, naturally cooling obtained product to room temperature, standing and curing at room temperature for 24 hours, and obtaining uniform and stable PSAFC-CTS composite flocculant.    USE - A preparation method of composite flocculant for use in bluegreen algae biogas slurry pre-treatment (claimed).    ADVANTAGE - The prepared flocculant shows quick flocculating setting effect; and has high corrosion and phosphorus removal efficiency, strong absorbing and bridging capability on colloid substance, wide use range, and low treatment cost. The preparation method is convenient.
NOVELTY - The method comprises taking the components including 80-85 wt.% of methanol (containing 99.9 wt.% of lactoalbumin), 0.3-0.35 wt.% of ammonia water, peroxyacetic acid (36-48 g/100 kg), hydrogen peroxide (24-35 g/100kg), sodium peroxide (35 g/100 kg), potassium permanganate (24 g/100 kg), ferrocene (8-12 g/100 kg), benzene copper sulfate (40-60 g/100 kg), 0.3-0.5 wt.% of gasoline, 0.005-0.01 wt.% of camphor or camphor powder, 0.3-0.5 wt.% of zinc and 0.03-0.04 wt.% of active carbon, and uniformly mixing the components.    USE - The method is useful for producing liquefied gas.    ADVANTAGE - The method is capable of economically producing the liquefied gas with high stability and improved corrosion resistance.
NOVELTY - Cobalt-based catalyst system (I) is claimed.    USE - The catalyst system is useful for preparing methane with co-production of oil product from synthetic gas.    ADVANTAGE - The catalyst system utilizes easily available raw materials, and has simple preparation process, which is economical and highly efficient.    DETAILED DESCRIPTION - Cobalt-based catalyst system represented by a formula (AB1CoO/C1) (I) is claimed. The content of cobalt in the catalyst accounts for 1.0-30.0 wt%. The content of component A in the catalyst accounts for 0.01-5 wt.%. The metal content of component B in the catalyst accounts for 0.5-15 wt.%. The content of carrier component C in the catalyst accounts for 50-95 wt.%.    A = Ru, Re or Rh;    B1 = TiO2, MnO, Cr2O3, ZrO2, La2O3 or CeO2; and    C1 = Al2O3, ZrO, SiO2, TiO2 or activated carbon.    INDEPENDENT CLAIMS are also included for:    (1) preparing the catalyst by using immersion method, comprising (i) calcining the carrier component C1 at 400-700 degrees C for 1-10 hours, purifying and cooling, (ii) using an aqueous solution containing metal ions of cobalt, components A and B1 to immerse equal volume of the solution obtained in the step (i) for 2-12 hours, and (iii) evaporating the immersed solution obtained in the step (ii) by drying at 60-90 degrees C, again drying at 100-150 degrees C, and calcining at 400-800 degrees C for 1-20 hours; and    (2) preparing methane with co-production of oil product from synthetic gas, comprising reacting synthetic gas in a reactor filled with the cobalt-based catalyst at 200-500 degrees C under a pressure of 0.1-7 MPa, where the reactant liquid flow rate/reactor volume (LHSV) is 1000-50000 per hour.
NOVELTY - Coal-based natural gas catalyst comprises a carrier, an active component and an auxiliary agent, where the carrier is aluminum oxide, the active component is nickel, and the auxiliary agent is a rare earth element.    USE - Used as coal-based natural gas catalyst. In the step (i), aluminum nitrate nonahydrate, nickel nitrate hexahydrate and lanthanum nitrate hexahydrate comprise an impurity content of 0-1%.    ADVANTAGE - The coal-based natural gas catalyst has high intensity, good activity, good thermal stability and anti-carbon property, good high temperature resistance, excellent transformation performance, simple preparation method and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the coal-based natural gas catalyst, comprising: (i) taking aluminum nitrate nonahydrate (66.87-100.29 g/l), nickel nitrate hexahydrate (17.69-35.39 g/l) and lanthanum nitrate hexahydrate (6.04-12.1 g/l) in a constant temperature reactor, stirring, heating to 50-70 degrees C, adding potassium carbonate (8-12%), maintaining the temperature, adjusting the pH to 7-8.5, washing and filtering to obtain semi-finished catalyst product; (ii) drying the semi-finished catalyst product for 2-3 hours at 100-200 degrees C under dry condition; (iii) calcining the dried catalyst product for 4-5 hours at 300-400 degrees C; and (iv) adding graphite (3-10%) and water, mixing uniformly, pressing and forming the product.
NOVELTY - Hydrogen production process via catalyzing plasma enhanced light, where the process is carried out using reaction container (1) having plasma electrodes (2,3), where the bottom of the container contains water solution (4), plasma power source (5), connection electrode (6), water vapor, a vacuum-pumping system (8), and hydrogen collecting system (10).    USE - As hydrogen production process (claimed).    ADVANTAGE - The method and apparatus effectively improves the production efficiency, the production scale and reduces the production cost and increases conversion efficiency, and suitable for industrial production.    DESCRIPTION OF DRAWING(S) - The figure shows structure of plasma-enhanced photo-catalysis hydrogen production device.    Reaction container (1)    Plasma electrodes (2,3)    Water solution (4)    Plasma power source (5)    Connection electrode (6)    Vacuum-pumping system (8)    Hydrogen collecting system (10)
NOVELTY - A biological petrol comprises (in wt.%) potato starch (90-98), modified additive (1-5), modifier (1-5) and hydrocarbon alcohol (0.01-1).    USE - Biological petrol for an engine.    ADVANTAGE - The petrol saves energy, and is environment-friendly and inexpensive. The petrol prolongs service life of an engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing petrol.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing petrol.'(Drawing includes non-English language text)'
NOVELTY - The device has a sealed fluidized bed provided in a base part of a measuring vessel (1), and a dust delivery line (3.2) comprising an end, where another end of the line is connected with a gasification burner (2.1). Pressure difference between the vessel and the burner is determined. A fixed throttle device (3.6) is arranged in the burner, and a dust flow measuring device (3.5) is arranged in the burner. The measuring device stays in effective connection with a control valve (3.3) such that the amount of supplied fluid gas (4) is measured after the measurement of dust flow.    USE - Device for constant supplying of dusts e.g. coal, coke and thermal pre-treated biomasses or waste materials from industry, trade and household, below ambient or increased pressure to a gasification burner in an entrained-flow gasification reactor.    ADVANTAGE - The measuring device stays in effective connection with the control valve such that the amount of supplied fluid gas is measured after the measurement of dust flow, thus compensating differential pressure fluctuations between the measuring vessel and consumer, and hence compensating amount fluctuations in the dust flow with reduced amount of auxiliary gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for constant supplying of dusts.    Measuring vessel (1)    Gasification burner (2.1)    Dust delivery line (3.2)    Control valve (3.3)    Dust flow measuring device (3.5)    Fixed throttle device (3.6)    Fluid gas (4)
NOVELTY - Producing a composition for processing the storage areas of biogas plant, comprises mixing bitumen with a high proportion of polyamides, heating a stone and enriching with polyamides, which melt on the stone, and adding the stone to the mixture to obtain a compact composition.    USE - The composition is useful for processing the storage areas of biogas plant, and for preventing the penetration of the acidic liquid silage into groundwater that forms a real watertight tray.    ADVANTAGE - The composition is resistant to acid and highly durable.
NOVELTY - Biomass pellet fuel is obtained by mechanically processing mixture comprising sawdust and rice husk powder.    USE - As biomass pellet fuel.    ADVANTAGE - The biomass pellet fuel is prepared without addition of any additives, and has high and stable calorific value (heat value), good combustion property, low production cost, and high economic and social benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the above-mentioned biomass pellet fuel, which involves removing impurities, stones, wood, iron and other impurities from the sawdust and rice husk, grinding the sawdust to less than or equal to 2 mm size and the rice husk hull to less than or equal to 5 mm size, mixing the grounded sawdust and rice husk in a predetermined weight ratio, heating and drying mixture in drying chamber at 40-70 degrees C until water content of the mixture reaches 15% or less, adding the dried mixture to ring shaped mold pressing equipment to obtain biomass pellet fuel, separating the un-molded crushed material and powder, again adding the separated crushed material and powder to the mold pressing equipment, testing technical specifications of the biomass pellet fuel and packaging the fuel according to the specifications.
NOVELTY - Mixing- and/or conveying device comprises at least one bearing, with which a movable, preferably rotatable part is rotatably recorded or mounted. The bearing has at least one bearing component made of a self-lubricating plastic.    USE - The mixing- and/or conveying device is useful for a fermenter.    ADVANTAGE - The mixing- and/or conveying device is durable and easy to replace in the fermenter in a cost-efficient manner. The bearing exhibits durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the fermenter for a biogas plant comprising a fermenter container and the mixing- and/or conveying device arranged on the fermenter container.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the bearing in cross cross-section.    Enclosure (61)    Bearing partners (62, 63)    Seal (64)    Agitator shaft (65)
NOVELTY - Converting solid fossil fuels (including coal, or oil tars obtained by distillation of coal, turf, grass, glucose, rubber, sapropel, sapropelites, slates and wood) to petroleum, comprises: (a) isolating a starting microorganism capable of conversion; (b) isolating genes responsible for the conversion ability from the microorganism; and (c) transfecting genes into host microorganism.    USE - The method is useful for converting solid fossil fuels (including coal, or oil tars obtained by distillation of coal, turf, grass, glucose, rubber, sapropel, sapropelites, slates, and wood) to petroleum.    ADVANTAGE - The method: provides petroleum in highly efficient and commercially viable manner; and utilizes microorganism that allows optimization of sequence production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) converting organic material or inorganic material (including such contained in water or salt water), petroleum, and the solid fossil fuels, into carbon hydrogen or oxygen, comprising steps (a) to (c) as above per se;    (2) a method of improving the conversion of the solid fossil fuels to petroleum, comprising (a) as above per se, (b1) isolating from the starting microorganism an oligonucleotide probe complementary to a gene responsible for the conversion ability, (c1) placing the probe under hybridizing conditions in contact with amplicons from other microorganisms suspected or capable of the conversion, (d1) isolating amplicons which are hybridized, and (e1) transfecting the isolated amplicons into a host microorganism and determining whether productivity improved;    (3) a method of improving the conversion of the organic material or inorganic material, petroleum, and solid fossil fuels into carbon hydrogen or oxygen, comprising steps (a), and (b1) to (e1) as above per se; and    (4) converting carbon, hydrogen and oxygen into fossil fuels, including coal and petroleum, comprising steps (a)-(c) as above per se.
NOVELTY - Sulfiding a sulfidable catalyst containing at least one metal or metal oxide under aqueous conditions, comprises: treating the catalyst with an aqueous solution (105) containing at least one water soluble sulfur-containing compound having a solubility of at least 0.2 wt.%, based on the aqueous solution to provide a treated catalyst; and heating the treated catalyst in the presence of hydrogen at 150-550 degrees C.    USE - The process is useful for sulfiding a sulfidable catalyst (claimed) which is used in a biomass process to form a liquid fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the aqueous catalyst sulfiding process.    Catalyst bed (101)    Preheater (103)    Aqueous solution (105)    Fed hydrogen (109)    Gas-liquid separator (201)
NOVELTY - Microbiological production of biogas (8), comprises using products of crude glycerol and soap water resulting in biodiesel production as the only substrates, where the ratio of crude glycerol to soap water is selected freely.    USE - The method is useful for microbiological production of biogas.    ADVANTAGE - The method produces high quality biogas that is suitable for purification and further refinement in a simple and cost-efficient manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the.    Hydrolysis (2)    Nutrients, trace elements and vitamins (3)    Fermenter (4)    External circuit (5)    Biogas (8)
NOVELTY - Method comprises (i) providing a biomass (102) containing celluloses, hemicelluloses, lignin, nitrogen and sulfur compounds, (ii) contacting the biomass with a digestive solvent (110) to form a pretreated biomass containing soluble carbohydrates, and (iii) contacting, in a reaction mixture, the pretreated biomass with hydrogen (121) at 150-300 degrees C in the presence of a pH buffering agent and a supported hydrogenolysis catalyst containing (a) sulfur, (b) molybdenum or tungsten, and (c) cobalt and/or nickel, incorporated into a suitable support, to form oxygenated hydrocarbons (130).    USE - The method is useful for hydrothermal hydrocatalytic treatment of biomass, which is useful for producing hydrocarbons and in transportation fuels such as synthetic gasoline, diesel fuel and jet fuel and industrial chemicals.    ADVANTAGE - The method is capable of directly processing the biomass into liquid fuels thus effectively preventing the poisoning of the biomass feed, and maintains the activity of catalysts for a prolonged period with minimal loss of active metal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising (ia) lignocellulosic biomass, (iia) hydrogenolysis catalyst containing the compounds (a), (b), (c), and (d) phosphorus, incorporated into a suitable support, (iiia) water, and (iva) a pH buffering agent (125).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a flow diagram of a hydrothermal hydrocatalytic treatment of biomass.    Biomass (102)    Digestive solvent (110)    Hydrogen (121)    Buffering agent (125)    Oxygenated hydrocarbons. (130)
NOVELTY - Producing hydrogen gas involves either combining aluminum, sodium hydroxide, and acetic acid with a metal selected from iron, copper, tin, gold and platinum, in the presence of light; or combining aluminum, sodium hydroxide, sodium acetate and iron in the presence of light.    USE - For producing hydrogen gas (claimed), which is used as a known non-toxic green alternative fuel.    ADVANTAGE - The acetic acid or sodium acetate prevents the formation of aluminum oxide and forms aluminum hydroxide. The gas is produced upon the reaction of aluminum and iron with sodium hydroxide and sodium acetate in the presence of direct colored natural light. The sodium acetate allows aluminum hydroxide to form, which does not occlude the surface of aluminum which would reduce the reactivity of aluminum. Iron will not react with sodium hydroxide unless the iron surface and the aluminum surface are touching each other. Hydrogen gas production occurs not only on the aluminum surface but also on the entire iron surface in this reaction.
NOVELTY - The solid oxide fuel cell (100) has cylindrical cell tubes (102) in which a fuel gas (121) is supplied. Air (122) is supplied into a fuel cell body to flow along the outer surface of each cell tube. An electrochemical reaction is generated by the fuel gas and air in the fuel cell body. A heat exchange core (14) is inserted in each cell tube.    USE - Solid oxide fuel cell for generating electric power.    ADVANTAGE - Facilitates cooling of the interior of a generator room by inserting a heat exchange core in each cell tube.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of solid oxide fuel cell. (Drawing includes non-English language text).    Heat exchange core (14)    Solid oxide fuel cell (100)    Cylindrical cell tubes (102)    Fuel gas (121)    Air (122)
NOVELTY - A hydrogen generation apparatus has modifier equipped with modification catalyst body, where raw material and modification catalyst body reacts to produce hydrogen-containing gas, and end plate provided with guide part which guides the modification catalyst powder from the modification catalyst body to discharge port, where hydrogen-containing gas is emitted to gas flow path which flows towards hydrogen utilization apparatus. Gas flow path circulates hydrogen-containing gas to an upward flow direction or through the side of the modifier, after flowing toward the end plate.    USE - Hydrogen generation apparatus for fuel cell systems (claimed).    ADVANTAGE - Decline in the conversion ratio of modification reaction during operation is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generation apparatus. (Drawing includes non-English language text).    Modifier (1)    Modification catalyst body (1a)    Catalyst support body (2)    Exhaust port (2a)    End plate (3)    Guide part (3a)    Discharge port (3b)    Gas flow path (4)    Receiving part (5)
NOVELTY - A hydrogen generating apparatus (100) has a modifier (1) provided with a modification catalyst which reforming-reacts raw material and produces a hydrogen-containing-gas, a hydrodesulfurization device (7) which removes sulfur compound in raw material and a desulfurizer. The temperature of downstream of hydrodesulfurization device is low with respect to upstream. The flow rate per unit cross-sectional area of downstream of desulfurizer is quick with respect to upstream.    USE - Hydrogen generating apparatus is used for fuel cell system (claimed) e.g. polymer electrolyte fuel cell, solid oxide fuel cell and phosphoric acid-type fuel cell.    ADVANTAGE - The hydrodesulfurization device of hydrogen generating apparatus has increased adsorption capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Flow paths (3,4)    Desulfurizing agents (3a,4a)    Hydrodesulfurization device (7)    Hydrogen generating apparatus (100)
NOVELTY - A mixed gas (G0) containing carbon dioxide and methane is hydrated to obtain a mixed gas hydrate. The hydrate is decomposed and regasified. The obtained cracked gas is hydrated and carbon dioxide is thus separated.    USE - Separation of carbon dioxide from e.g. natural gas.    ADVANTAGE - The carbon dioxide is efficiently separated from mixed gas at high separation rate, and high concentration methane gas is obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon dioxide separation apparatus (1), which has a production portion (2) for supplying carbon dioxide, mixed gas containing methane, and raw water, and producing hydrate of mixed gas at predetermined pressure and temperature, a decomposition portion (3) for decomposing and regasifying hydrate, and production portion (5) for hydrating cracked gas at predetermined temperature and pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of carbon dioxide separation apparatus.    Carbon dioxide separation apparatus (1)    Production portions (2,5)    Decomposition portion (3,7)    Carbon dioxide absorption portions (4,6)    Mixed gas (G0)    Water (L1-L10)
NOVELTY - A pellet production method involves reducing moisture content of potato pulp to 45-40%, subjecting resultant product to granulation process by using a centrifuge at humidity of 35-40%, and drying the resultant product to reduce the moisture content to 10-15% to obtain a finished product.    USE - Method for producing pellet by utilizing potato pulp.    ADVANTAGE - The method enables producing pellet in an efficient manner.
NOVELTY - Compost is manufactured by decomposing compost raw material, fermenting by mixing horse excrement with deposited compost raw material, and stirring.    USE - Manufacturing method of compost for agricultural fertilizer.    ADVANTAGE - Decomposition and fermentation periods are shortened.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory diagram of the compost raw material collection process of the manufacturing method of compost. (Drawing includes non-English language text).    Racehorse (2)    Compost raw material (6)    Chaff (10)
NOVELTY - The arrangement has an organic material and a fiber stuff mouth unit and a coarse and fine chopping units that are attached to a waste water and liquid dung storing and pre-mixing unit. The hydrodynamic disintegrating unit, ultrasound digestive unit and ultrasonic gas bubbling unit are arranged in a biogas reactor.    USE - Arrangement for producing biogas.
NOVELTY - Method for processing biomass waste, involves drying the biomass waste into granular form using combustion heat generated by carbon residue of biomass waste, distillating the dried biomass waste, separating hydrocarbon as volatile substance and carbon residue as nonvolatile substance, burning the separated carbon residue, separating carbon and hydrogen by compressing and heating hydrocarbon which is separated using combustion heat, and collecting the separated hydrogen.    USE - The method is useful for processing biomass waste which is used as dried energy source for plants. The biomass waste includes paper waste, livestock excrement, foodstuff waste material, and sewage sludge.    ADVANTAGE - The method provides combustion heat continuously to remove hydrogen from biomass waste.
NOVELTY - Producing a partially hydrolyzed lignocellulosic material, comprises pretreating a lignocellulosic material with a pretreatment solution comprising 40-99 wt.% of glycerol, 0.1-5 wt.% of an acid catalyst, and 1-60 wt.% of water thus producing a pretreated partially hydrolyzed lignocellulosic material.    USE - The method is useful for: producing a partially hydrolyzed lignocellulosic material (claimed) product, such as fermentable sugars; pretreating the lignocellulosic material (e.g. biomass); and producing a high value pulp, where the hydrolyzed lignocellulosic material product is useful to produce biofuel including ethanol and butanol.    ADVANTAGE - The method is capable of economically and easily producing the partially hydrolyzed lignocellulosic material with high efficiency and improved reaction conditions in an environmentally friendly manner.
NOVELTY - A fats-and-oils raw material is contacted with alcohol in presence of alkali metal catalyst and transesterified. The reaction liquid mixture is gravity-based-separated to light liquid and heavy liquid. The light liquid is heated. The precipitation separation of free glycerol and alkali metal in light liquid is carried out. The air-liquid contact of light liquid and recovery gas is carried out carried out, and the residual alcohol in light liquid is removed and recovery gas is recovered, to obtain biodiesel fuel.    USE - Manufacture of biodiesel fuel used as automotive fuel.    ADVANTAGE - The method enables economical manufacture of biodiesel fuel.    DETAILED DESCRIPTION - A fats-and-oils raw material is contacted with alcohol in presence of alkali metal catalyst and transesterified. The reaction liquid mixture is gravity-based-separated to light liquid and heavy liquid. The light liquid is heated without washing, to remove residual alcohol in light liquid. The precipitation separation of free glycerol and alkali metal in light liquid is carried out. The air-liquid contact of light liquid and recovery gas is carried out, and the residual alcohol in light liquid is removed and recovery gas is recovered, to obtain biodiesel fuel. The residual alcohol concentration in light liquid is 0.05 %mass or less. INDEPENDENT CLAIMS are included for the following:    (1) residual alcohol removal apparatus; and    (2) biodiesel fuel manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of apparatus for manufacturing biodiesel fuel.    Storage tank (1)    Reaction apparatus (2)    Separation apparatus (4)    Condensing apparatus (7)    Precipitation apparatus (9)
NOVELTY - An unsupported membrane comprises reaction product of silicone composition containing organopolysiloxane (A) having at least two unsaturated aliphatic carbon-carbon bond-containing groups per molecule, organosilicon compound (B) having at least two silicon-bonded hydrogen atoms per molecule, polyether (C) having at least one unsaturated aliphatic carbon-carbon bond-containing group per molecule, siliceous filler (D) and hydrosilylation catalyst (E).    USE - Unsupported membrane is used for separating gas components in feed mixture (claimed). Uses include but are not limited to purifying water, cleansing blood during dialysis, recovery of hydrogen gas in ammonia synthesis and petroleum refining, separation of methane in biogas synthesis, removal of water vapor, carbon dioxide and dihydrogen sulfide from natural gas, and removal of carbon dioxide from flue gas during combustion process.    ADVANTAGE - The unsupported membrane separates the gas components in feed mixture with high selectivity and permeability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) supported membrane; and    (2) method for separating gas components in a feed mixture.
NOVELTY - Aerobic treatment system, comprises aeration tank and secondary sedimentation tank. The aeration tank is provided with aerator, air inlet pipe, and biogas tank connected through air outlet pipe. The aerator is connected with gas compressor. The gas compressor is provided with oxygen tank through valve. The bottom and side portion of aeration tank are provided with water outlet and inlet respectively. The water outlet is connected with the secondary sedimentation tank provided with sludge well being connected with the inlet of the aeration tank.    USE - Aerobic treatment system for wastewater treatment (claimed).    ADVANTAGE - The aerobic treatment system provides good wastewater treatment effect.    DETAILED DESCRIPTION - Aerobic treatment system, comprises aeration tank and secondary sedimentation tank, where bottom portion of the aeration tank is provided with an aerator and an air inlet pipe, and top portion of the aeration tank is connected with biogas tank through air outlet pipe. The aerator is connected with gas compressor through the air inlet pipe. The gas compressor is provided with oxygen tank through valve. The biogas tank and gas compressor are connected by pipe. The bottom portion of the aeration tank is provided with water outlet, and side portion is provided with an inlet. The water outlet is connected with the secondary sedimentation tank, and bottom portion of the secondary sedimentation tank is provided with sludge well connected with the inlet of the aeration tank.
NOVELTY - Generating resources from feedstocks, comprises: receiving an organic feedstock and a rumen in a fermenter (2); and fermenting the organic feedstock with the rumen to generate the resource.    USE - The method is useful for generating resources from feedstocks, where the generated resource includes at least one of chemicals, lipids, volatile fatty acids, long chain fatty acids, acetic acid, propionic acid, isobutyric acid, butyric acid, isovaleric acid, valeric acid, lactic acid, hexanoic acid, biomass, high protein animal feed, fertilizer, phosphate fertilizer, nitrogen fertilizer, proteins, amino acids, lysine, enzymes, cellulase, alpha -amylase, histidase, lysozyme, penicillin acylase, ethanol, butanol, biogas, methane, hydrogen, carbon dioxide or water (all claimed).    ADVANTAGE - The method: is robust and capable of continuously producing chemical products and biomass, hence exhibits improved fermentation efficiency; provides greater flexibility to handle heterogeneous waste streams, when compared to conventional fermentation systems; provides the products, which are safe; and does not require sterilized feedstocks and can be operated at moderate temperatures and near atmospheric pressures, so it is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for generating resources from organic feedstocks, comprising: a grinder/mixer (1) configured to receive the organic feedstock and the rumen; and the fermenter configured to receive the organic feedstock and the rumen, where the fermenter is configured to ferment the organic feedstock to generate a resource.    DESCRIPTION OF DRAWING(S) - The figure illustrates a flow diagram of a process of generating resources from feedstocks.    Grinder/mixer (1)    Fermenter (2)    Cascade unit (3)    Biomass separation unit (4)    Metabolite separation unit (5)
NOVELTY - The tank has permanent magnet (12) positioned in between middle and bottom cell plates (11), connected to center anode shaft (5) with S or Z shaped stainless steel plate (13) in between, and that creates electromagnetic field while direct current (DC) current is passing through electrolyte solution. A stirrer set is made of S or Z shaped stainless steel plate and attached to the shaft that holds the cell plates and magnet. The stirrer set increases flow speed of electrolyte solution so that reaction to produce hydrogen gas when electrical current passes through electrolyte is increased.    USE - WDH4 hydrogen separation tank used in hydrogen system for separating hydrogen gas from water or electrolyte solution.    ADVANTAGE - Increases hydrogen gas produced since permanent magnets installed inside the tank helps create electromagnetic field and strengthen electrical current without adding another battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the cell plates, magnet and Z plate connected to the shaft.    Lid (2)    Center anode shaft (5)    Cell plates (11)    Permanent magnet (12)    S or Z shaped stainless steel plate (13)
NOVELTY - The tank has a cylinder hydrogen separation chamber with three holders. A stainless steel lid (2) is welded onto the tank. The circular/square shaped stainless steel cell plates (11) are provided with varied size holes. The holes are positioned along the circumferences of the circles on the cell. Permanent magnet (12) is completely covered in a stainless steel case and is positioned in between the middle and the bottom cell plates. S or Z-shaped stainless steel plate (13) is attached to a shaft for holding the cell plates and the permanent magnet.    USE - WDH5 hydrogen separation tank for internal and external combustion engine.    ADVANTAGE - The flow speed of electrolyte solution can be increased by the S or Z shaped stainless steel plate, thus increases the reaction to produce hydrogen gas to flow through to the hydrogen pipe and the engine combustion chamber can be increased when electrical current passes through the electrolyte solution.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen separation cell plate set.    Stainless steel lid (2)    Anode shaft (5)    Stainless steel cell plate (11)    Permanent magnet (12)    S or Z-shaped stainless steel plate (13)
NOVELTY - Conversion of a feedstock or sugar into a product, comprises wet milling a reduced recalcitrance lignocellulosic material.    USE - The method is useful for converting a feedstock or sugar into a product e.g. alcohols, organic acids, sugars and/or hydrocarbons (all claimed), where the sugars include glucose, xylose, arabinose, mannose, galactose, fructose, disaccharides, oligosaccharides and polysaccharides, the alcohols include ethanol, n-propanol, isobutanol, sec-butanol, tert-butanol or n-butanol, organic acids include methyl acrylate, methylmethacrylate, lactic acid, citric acid, formic acid, acetic acid and/or propionic acid, and the hydrocarbons include methane, ethane, propane, isobutene, pentane, biodiesel, bio-gasoline and/or n-hexane.    ADVANTAGE - The method: reduces the time required for saccharification, and increases the concentration of sugar that is obtained in a given saccharification time; and provides relatively rapid and effective processing of a relatively high solids level of feedstock, in a cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a wet milling system (S1) comprising a wet mill disposed in a fluid having a biomass material dispersed in it; and    (2) a system (S2) comprising a tank, a jet head and a wet mill.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of a saccharification system.    Vibrating device (36)    Feedstock pretreatment module (132)    Pump (139)    Viscometer (141)    Motor (150)
NOVELTY - Synthesizing bifunctional 2-6C hydrocarbon compounds, where the two functions are acid, aldehyde, nitrile, acetal or unsaturated alpha -olefin functions from biomass, comprises (a) subjecting the biomass to fermentation in a presence of a microorganism and/or an enzyme for formation of intermediate compounds of saturated acids, optionally carrying a hydroxyl function, alcohols and alpha -olefins, in liquid or gaseous form, or carbon dioxide, and then (b) transforming into gaseous phase by catalytic way using molecular oxygen intermediate compounds in the presence of carbon dioxide from step (a).    USE - The method is useful for synthesizing bifunctional hydrocarbon compounds from biomass.    ADVANTAGE - The method provides easy and energy efficient synthesis of bifunctional hydrocarbon compounds from biomass by allowing the optimization of the operating conditions without using fossil raw materials.
NOVELTY - Mounting arrangement of a ceiling of a biogas tank, comprises a tension belt, which extends from the ceiling to a wall (3) of the biogas tank, a holding device (2), which holds the wall with the tension belt, and exhibits a base body (5) attached to the wall, and two deflection axes, which are arranged parallel to each other and are spaced apart. The tension belt is guided from the ceiling to two deflection axes and clamps itself around the two deflection axes, or the tension belt is guided over the two deflection axes beyond an attachment point, at which it is clamped in a releasable manner.    USE - The mounting arrangement is useful for a ceiling of a biogas tank.    ADVANTAGE - The mounting arrangement ensures gentle attachment of the tension belt on its clamping point.    DESCRIPTION OF DRAWING(S) - The drawings 1 and 2 show a schematic representation of perspective view of the mounting assembly, and a vertical section across the wall of the biogas tank of the mounting arrangement, respectively.    Holding device (2)    Wall (3)    Base body (5)    Base surface (6)    Carriage screws (8)
NOVELTY - System (1) comprises a biogas plant (5) comprising a concentrator (3) for the concentration of low calorific liquid biomass and a cogeneration plant, which is coupled to the biogas plant for producing heat and electric current.    USE - The system is useful for utilizing energy contained in biomass.    ADVANTAGE - The accumulated condensate in the concentrator is effectively utilized for irrigating the agricultural land. The system utilizes the waste heat and supplies the same during concentration of the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for utilizing energy contained in biomass (7) comprising fermenting the biomass in the biogas plant, and generating heat and electric current with the resulting biogas in the cogeneration plant, where the low calorific liquid biomass is concentrated in a concentrator.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow for utilizing energy contained in biomass.    System (1)    Concentrator (3)    Container (4)    Biogas plant (5)    Biomass (7)
NOVELTY - Providing gas with very high methane content, comprises separating at least one portion of carbon dioxide from a gas stream containing carbon dioxide and methane, at a first processing site, where a product gas that is produced by catalytic methanation of reactant gas containing carbon dioxide and hydrogen, forms at least one portion of the gas stream, at a second processing site before it reaches the first processing site.    USE - The method is useful for providing a gas with very high methane content.    ADVANTAGE - The method produces the gas with improved quality, and is environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a plant (10) for providing the gas with very high methane content, comprising a device for separating at least one portion of the carbon dioxide from a gas stream containing carbon dioxide and methane, which is supplied to the separating device, a device for producing the product gas (6) by catalytic methanation of reactant gas containing carbon dioxide and hydrogen, and a line system for at least partial formation of gas stream by the product gas of methanation device, arranged upstream of the separating device;    (2) a methanization reactor (40) for using in the plant, preferably as a unit together with an electrolyzer for producing at least one portion of hydrogen that is converted in the methanization reactor; and    (3) a gas mixture (3) having very high methane content, which is provided by the above method and/or by the above plant.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Gas mixture (3)    Product gas (6)    Plant (10)    Methanization reactor (40)    Gas network (50)
NOVELTY - The apparatus has a modifier that produces a hydrogen containing gas by reforming reaction using water supplied from raw material supplied from the material supply device. A combustor burns the hydrogen containing gas emitted from the modifier, and heats the modifier. A control parameter setter sets (S103) one of the large value of supply amount of the raw material to the modifier, the target value if supply amount of the modifier and target value of supply amount of combustion air to the combustor.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The operation efficiency of the hydrogen generating apparatus can be improved. The damage to hydrogen generating apparatus can be redeuced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating operation of hydrogen generating apparatus.    Step for determining supply amount (S101)    Step for determining whether supply amount is larger than upper limit (S102)    Step for setting control parameter (S103)
NOVELTY - A hydrogen generating apparatus has hydrodesulfurization device which hydrodesulfurizes sulfur compound in raw material, and modifier which produces hydrogen-containing gas by modification reaction using the hydrodesulfurized raw material. The hydrodesulfurization device has 1st flow path where raw material flows, 1st desulfurizing agent provided in the 1st flow path, 2nd flow path where raw material from 1st flow path flows, and 2nd desulfurizing agent provided in the 2nd flow path.    USE - Hydrogen generating apparatus for fuel cell system used in fuel cell batteries (claimed), such as polymer electrolyte form fuel cell (PEFC), solid oxide fuel cell, or phosphoric acid fuel cell.    ADVANTAGE - Utilization factor of thermal radiation of modifier is improved, temperature lowering of desulfurizing agent is suppressed, and flow distribution of raw material is uniform.    DETAILED DESCRIPTION - A hydrogen generating apparatus has hydrodesulfurization device which hydrodesulfurizes sulfur compound in raw material, and modifier which produces hydrogen-containing gas by modification reaction using the hydrodesulfurized raw material. The hydrodesulfurization device has 1st flow path where raw material flows, 1st desulfurizing agent provided in the 1st flow path, 2nd flow path where raw material from 1st flow path flows, and 2nd desulfurizing agent provided in the 2nd flow path. Hydrodesulfurization device is connected to modifier so that heat-exchange is possible. The 2nd flow path is adjacent to 1st flow path so that heat exchange is possible between 1st and 2nd desulfurizing agents. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fuel cell system. (Drawing includes non-English language text).    Modifier (1)    Combustor (2)    1st flow path (3)    1st desulfurizing agent (3a)    2nd flow path (4)    2nd desulfurizing agent (4a)
NOVELTY - A raw material is formed by adding an additive (A) which can form II-type hydrate in high temperature side or low pressure side rather than the phase-equilibrium curve of the mixed gas hydrate (17), to water (L1-L4). The raw material is then added to raw water, and the formed mixture is reacted with mixed gas (G0) containing carbon dioxide as main component and methane as another component, to obtain II-type hydrate. Thus, gas-separation method is carried out.    USE - Gas-separation method used for separating carbon dioxide and methane from biogas and natural gas.    ADVANTAGE - The methane gas having high concentration is efficiently separated, with low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas-separation apparatus (1), which has gas supply port (2) which supplies mixed gas, raw water supply port (3) which supplies water, additive supply port (4) which supplies additives and hydrate production port (11) which produces II-type mixed gas hydrate by hydrating the mixed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of gas-separation apparatus.    Gas separation apparatus (1)    Gas supply port (2)    Raw water supply port (3)    Additive supply port (4)    Hydrate production port (11)    Mixed gas hydrate (17)    Hydrate decomposition portion (31)    Additive (A)    Mixed gas (G0)    Water (L1-L4)
NOVELTY - An alkali metal salt of aromatic hydroxy compound and carbon dioxide are reacted in presence of alcohol and/or ether compound. The amount of alcohol and/or ether compound is 0.01-1.0 moles with respect to 1 mole of alkali metal salt.    USE - Manufacture of aromatic hydroxycarboxylic acid. Uses include but are not limited to raw material for pigments and dyes, liquid-crystal molecule, pharmaceutical and agrochemical.    ADVANTAGE - The method is environmentally-friendly, and enables economical manufacture of aromatic hydroxycarboxylic acid with high yield.
NOVELTY - Preparing organic fertilizer using tobacco plant-wastes for banana trees, comprises: (i) collecting the tobacco plant wastes, cutting, spaying the fermenting Bacillus licheniformis inoculum, coating and insulating by stacking, turning pile, drying to obtain a solid product and naturally fermenting the solid product to obtain a liquid product; and (ii) uniformly mixing the fermented solid product with a dry chicken manure, spraying a fermenting inocula, stirring, filling into a sealed bag, sealing and allowing to ferment to obtain a secondary fermented organic fertilizer product.    USE - The method is useful in preparing organic fertilizer using tobacco plant-wastes for banana trees.    ADVANTAGE - The organic fertilizer is economical; improves soil structure and soil fertility; ensures less pollution; prevents tobacco plant disease; enables degradation of heavy metals; improves cold-resistant-, drought-resistant-, lodging-resistant- and disease-resistant properties of the banana plants with improved quality of the fruit.    DETAILED DESCRIPTION - Preparing organic fertilizer using tobacco plant-wastes for banana trees, comprises: (i) collecting the tobacco plant wastes, cutting, spaying the fermenting Bacillus licheniformis inoculum, where the spraying volume is 4 kg/ton of fresh tobacco plant waste, coating and insulating by stacking, turning pile, drying to obtain a solid product of the fresh tobacco plant waste and then naturally fermenting the solid product to obtain a liquid (primary) product; and (ii) uniformly mixing the fermented solid product with a dry chicken manure in a weight ratio of 35-40:65-60, spraying the fermenting inocula comprising Bacillus lacticus, yeast, and photosynthetic bacteria, where the spraying volume is 2kg/ton of organic mixture material, uniformly stirring, filling into a sealed bag, sealing and allowing to ferment naturally to obtain a secondary fermented organic fertilizer product.
NOVELTY - Liquid organic fertilizer composition prepared by adding potassium sulfate, potassium dihydrogen phosphate, urea, calcium superphosphate, magnesium sulfate heptahydrate, chelated iron and zinc sulfate heptahydrate into organic fertilizer extract with rich amino acid, trace elements and probiotic, until the nutrient elements satisfies the mass% as follows: nitrogen (21-24), phosphorus (7-8), potassium (7-8), calcium (0.6-1.2), magnesium (0.7-1.4), sulfur (1.8-2.8), iron (0.1-0.2) and zinc (0.1-0.5), is claimed.    USE - Used as liquid organic fertilizer composition.    ADVANTAGE - The composition strengthens the photosynthesis of tea plants by adding trace elements and controlling flower-spot disease; utilizes nutrient elements with combination of organic and inorganic fertilizers to process the growth of tea plants and control the proportion of trace elements, inhibits generating antagonistic effect to exhibit synergistic effect between various elements, and is efficiently absorbed by plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the liquid organic fertilizer composition, comprising (a) taking the composting of the organic fertilizer at normal temperature as raw material, using water as an extractant, where the mass ratio of the organic fertilizer and extractant is 1:5, extracting under anaerobic conditions for 72 hours; (b) adding potassium sulfate, potassium dihydrogen phosphate, urea, calcium superphosphate, magnesium sulfate heptahydrate, chelated iron and zinc sulfate heptahydrate into the extract obtained in the step (a) until the nutrient elements satisfies the mass% as mentioned above.
NOVELTY - Biologically active insecticide-fertilizer comprises (in wt.%) photosynthetic bacterial inocula with an effective active bacteria of 8-1 billion/ml (8-12), fulvic acid (8-12), urea (1-2), monoammonium phosphate (1-2), potassium sulfate (1-2), potassium silicate (0.5-1.5), azadirachtin (0.1-0.2), ammonium fluorosilicate (0.05-0.15), ammonium molybdate (0.3-0.6), radix aconiti kusnezoffii (0.2-0.5) and water (remaining). The radix aconiti kusnezoffii is added with water to prepare water extract.    USE - The fertilizer is useful as a flower foliar spray, and for promoting the flower growth and preventing the disease caused by insects.    ADVANTAGE - The fertilizer: has rapid effect; persists for a long time; is economical, and environmental friendly; increases the yield, and number of flowers; improves the flower quality, and soil property; and degrades the pesticide residues.
NOVELTY - The invention relates to a process for preparing a solid fuel. According to the invention, the process consists in mixing and homogenizing 65...84% biomass dried until a humidity content of 2% is reached and ground down to a size of 2 mm, 5...18% plastics ground down to a size of 2...3 mm, 10...25% additive consisting of a material of high energetic value which is ground down to a size of 2...5 mm and 1...2% binder, after which the mixture is subjected to pelletization, wherefrom there is obtained a fuel having sizes of 10 mm, a density in the range of 770...790 kg/m3 and a humidity content of 2%, at the most.
NOVELTY - The marsh gas recycling system has an orderly-connected anaerobic tower, a dehydrating tower and a desulphurization tower. The desulphurization tower is connected with a gas turbine unit for converting methane combustion heat energy into kinetic energy. The gas turbine unit has an internal combustion engine and a pressurizing device e.g. air compressor.    USE - Marsh gas recycling system for treating papermaking wastewater.    ADVANTAGE - The biogas can be recycled. The air pollution can be reduced and the energy can be saved.
NOVELTY - Fluidized bed biomass fast pyrolysis spiral feeding device comprises feeder shell, airlock, storage hopper, and flange vertically connected with feeding packing auger that is located in the feeder shell, fluidized bed reactor, and uniform and nonpressure air locking feeder. The airlock of sealing material has antispraying function. The storage bin of the stirring rod component is composed of straight stirring rod connected with the upper part of guide rail.    USE - Fluidized bed biomass fast pyrolysis spiral feeding device.    ADVANTAGE - The feeding device realizes uniform feeding, prevents antispraying of fluidized bed biomass, and has fast pyrolyzing effect.
NOVELTY - A biomass comprehensive switch device comprises biomass multifunctional integrated conversion device, gas separating device, liquid standing separation device, gas purifying device, gas storage device, hot water collecting box, and water storage tank. The device conducts biomass carbonizing, gasifying and dry distillation technique as a whole, thus realizing waste into resource.    USE - Biomass comprehensive switch device.    ADVANTAGE - The device can realize biomass technique, function integration, and transforms biomass into biofuel gas, tar, carbon, acetic acid and hot water product.
NOVELTY - Agricultural waste resource pyrolysis gasification comprehensive conversion and utilization system comprises a pyrolysis device, an air supply device, a multifunctional heat exchange device equipped with an insulation layer, a condensate outlet, a residual heating device, and a condensed water channel connected to the residual heating device. A gas channel of the multifunctional heat exchange device is connected with the pyrolysis device and the air supply device. The residual heating device comprises a water storage buffer tank, a pipeline pump I, a boiler and a heating pipe network.    USE - Used as an agricultural waste resource pyrolysis gasification comprehensive conversion and utilization system.    ADVANTAGE - The device produces acetic acid, which can be used as a biological foliar or biological pesticides or biological fungicides and tar as a industrial raw material, and ensures comprehensive transformation of biomass waste resources with a utilization rate of 100%.
NOVELTY - A biomass waste resource pyrolysis gasification comprehensive conversion system comprises pyrolysis device, air supply device, multifunctional heat exchange device and residual heat heating device. The multifunctional heat exchange device is equipped with insulation layer, gas channel and condensed water passage. A gas passage outlet passes through a guiding device that is connected to the air supply device. A solid separating device is connected to outer surface of afterheat heat supply device having water storage buffer tank.    USE - Biomass waste resource pyrolysis gasification comprehensive conversion system.    ADVANTAGE - The system converts biomass waste raw material into high temperature pyrolysis gas, tar gas, and mixed gas of air and water vapor. The produced acetic acid can be used as biological foliar fertilizer or insecticide or bactericide, and tar is used as industrial raw material. The biomass waste resource comprehensive conversion rate is near 100%.
NOVELTY - Biomass oil cogeneration device comprises a material crushing device, a material drying device, a feeding device, a cracking device body, a primary condensing device and a cyclone pump. A secondary condensing device bottom is connected to biomass-oil device. A tertiary condensing device bottom is connected to low-boiling point oil collecting device. The cogeneration device further comprises support, feeding hopper, spiral extruding mechanism, front and back pair of rollers with roller structure, shell, ridges and grooves, total feeding port, discharge ports, rotating shaft and power mechanism.    USE - Used as a biomass oil cogeneration device.    ADVANTAGE - The cogeneration device is capable of replacing gasoline and diesel oil by refining as fuel of internal combustion engines, and the low boiling point high quality biomass oil can replace liquefied gas as domestic fuel, and the device is suitable for biomass-oil large scale industrial production.
NOVELTY - Preparing organic fertilizer by fermenting maize straw and cow dung, comprises: (i) drying the maize straw under sunlight, and grinding, then drying cow dung under sunlight, and diluting a microbial fermentation agent; (ii) uniformly and completely mixing maize straw, cow dung and microbial fermentation agent, and adding water to the material till the moisture content reaches to 55-65%; and (iii) uniformly mixing the material, bagging, and uniformly stacking to piles, and subjecting to heating and fermentation, and obtaining the finished product.    USE - The method is useful for preparing organic fertilizer by fermenting with maize straw and cow dung.    ADVANTAGE - The method completely utilizes the agricultural wastes e.g. maize straw, which is utilized as a rich resource; is economical; has simple operation procedures; reduces the production of bad odor during the process; and prevents the discharge of harmful resources and agricultural wastes, and thus it is environmental-friendly.
NOVELTY - The method involves placing rice hulls and sawdust into a fermenter (1). The fermentation heat is generated within the fermenter, to remove the complex bacteria adhered in the rice hulls or the sawdust. A dehydration cake (2) is installed the fermenter to adjust the oxygen amount of impellers (24,24') to the steady state. The sludge in the fermenter is converted into the active substance including the soil fertilization agent, to minimize the moisturing of sludge.    USE - Sludge reduction and recycling method.    ADVANTAGE - The harmful bacteria within the dehydration cake can be annihilated and recycled at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermenter.    Fermenter (1)    Dehydration cake (2)    Hopper (20)    Opening and closing switch (21)    Impeller (24)    Air outlet (27)
NOVELTY - A composite clean liquid fuel comprises (wt.%) methanol (55-60), water (30-40), ethanol (8-10), acetic acid (0.25-30), sodium hydroxide (0.3-0.4), ammonia water (0.08-0.1), N-dimethylaniline (0.05-0.055), sodium nitrate (0.05-0.06), and bicyclic diene (0.02-0.03).    USE - A composite clean liquid fuel used in kitchen.    ADVANTAGE - The fuel is safe and environment-friendly, and has no peculiar smell, easy production, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing a composite clean liquid fuel comprising mixing bicyclic diene into methanol, mixing sodium hydroxide in water, stirring and blending the two kinds of liquid, dissolving acetic acid into the liquid to stir, dissolving and stirring ammonia water, N-dimethylaniline, and sodium nitrate, adding into ethanol, dissolving the liquids, adding in reaction pot for reaction and stirring, filtering the liquid, conducting softening treatment, and storing.
NOVELTY - An iridium coordination compound (I) is new.    USE - Compound (I) used for dye-sensitized solar cell (claimed).    ADVANTAGE - The compound (I) has a visible light response, which realizes that fast visible light catalyzes water to reduce to prepare hydrogen.    DETAILED DESCRIPTION - An iridium coordination compound of formula Ir-(L)2-4-carboxyl-4'-carboxylate radical-2-2'-bipyridyl (I) is new.    L=3-methyl trifluoride-2-phenyl benzothiazole, 2-phenyl benzothiazole, 2-phenyl-5-(methyl trifluoride) benzothiazole or 4-N, N dimethyl-phenyl-5-(methyl trifluoride) benzothiazole.    An INDEPENDENT CLAIM is included for preparation of the compound (I).
NOVELTY - A hydrogen energy device is prepared by connecting steam with a heat exchanger; connecting current with an electrolytic pipe; and connecting electrolytic chamber with hydrogen and oxygen pipe to obtain vapor electrolytic apparatus for preparing hydrogen and oxygen.    USE - Method for the preparation of hydrogen energy device (claimed).    ADVANTAGE - The method provides simple structure, is safe in using, electrolytic reaction is easy to obtain, can replace the complex solution of hydrogen production, solves the energy shortage, and prevents environment pollution.
NOVELTY - A latex substrate is conveyed by adding resistance reducing foaming agent to chemical loading tube to make the foaming agent distributed along circumferential direction of inner wall of the tube; and adding 0.005-0.2 wt.% surfactant to the foaming agent.    USE - Method for conveying a latex substrate (claimed).    ADVANTAGE - The method can be realized at 11.4 degrees C, charging speed of 40 kg/minute, transportation emulsion matrix of 50 m, and chemical loading tube pressure of 1.2-1.6 MPa.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device used for conveying latex substrate.
NOVELTY - An electrode material has diazo group, azo or hydrazino group bonded on surface.    USE - Electrode material is used for fuel battery and manufacturing hydrogen (all claimed), electrochemical sensor, oxygen reduction catalyst electrode and biosensor.    ADVANTAGE - The electrode material performs oxidation-reduction of oxygen and reduction of noble potential of oxygen without using expensive catalyst metals e.g. platinum, thus enabling economical usage. The fuel battery using the electrode material has improved oxidation-reduction characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen by electrolysis, which uses the electrode material; and    (2) manufacture of electrode material using carbon as substrate, which involves covalently bonding nitrogen-containing functional group on the surface of carbon material, carrying out electrolytic reduction process in strong acid, reacting with sulfuric acid and carrying out electrolytic reduction process in strong acid.
NOVELTY - The electric heating type biomass gasifier has an electric heating unit which is provided to heat the inner space of a reforming furnace (8). A temperature sensor detects the temperature of the measuring point in a gasifier (1). An air pressure adjustment unit adjusts the discharge amount of the gas from the gasifier and adjusts the atmospheric pressure in the gasifier. A system control unit performs drying, thermal decomposition, and gasification of biomass (2) by the superheated steam generated by electric heating generates combustible gas.    USE - Electric heating type biomass gasifier for electric power generation.    ADVANTAGE - The electric heating type biomass gasifier can generatecombustible biogas from comparatively little biomass, and is enabled for the gas electric power generation effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electric heating type biomass gasifier.    Gasifier (1)    Biomass (2)    Conductor (3)    Electromagnetic induction heating device (5)    Reforming furnace (8)
NOVELTY - The system (100) has a upward flow type tank filter (1) which filters the waste water flowed into the levitation filter medium layer from the waste water inflow port. Sludge collection equipment (4) collects the sludge in the back washing waste water discharge from the tank filter at the time of back-washing of the levitation filter medium layer. A digester (5) carries out methane fermentation treatment of the sludge collected by sludge collection equipment.    USE - Waste-water treatment system used in waste water treatment field such as sewage treatment, industrial waste water process.    ADVANTAGE - The installation cost and running cost of waste water treatment system can be reduced. The environmental impact can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the waste water treatment system. (Drawing includes non-English language text)    Tank filter (1)    Biological reactor (2)    Sludge collection equipment (4)    Digester (5)    Waste-water treatment system (100)
NOVELTY - Compost mixture comprises (in vol.%): organic nitrogenous material (1-30), broken dry matter (60-90), decomposing material (5-15) that decomposes organic material, rock material (1-5) and worm and/or worm faeces (1-30).    USE - The mixture is useful for composting process (claimed) and obtaining product used for increasing well being of plants.    ADVANTAGE - The compost mixture is peat-free and is environmentally-friendly and produces product with reduced ecological carbon footprint. The compost mixture produces product having good water retaining capacity and ensuring good oxygen supply for plant roots. The mixture avoids addition of artificial additives such as fertilizers to product as nitrogen, trace elements and other nutrients in it are generated by faeces of worms.
NOVELTY - Treating lignocellulosic material comprises subjecting the material to microwave radiation at the resonant frequency of the lignin to dissociate the lignin.    USE - The method or apparatus is useful for treating lignocellulosic material (claimed).    ADVANTAGE - Novel ways of treating lignocellulosic materials and of producing useful materials from lignocellulose that have high yields and low energy requirements are provided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) apparatus for treating lignocellulosic material, comprising microwave generating means for subjecting the material to microwave radiation at the resonant frequency of the lignin to dissociate the lignin; and    (2) a biofuel or animal foodstuff such as oilcake produced by the method or the apparatus.
NOVELTY - System for aerobic fermentation comprises at least one drum for fermenting the organic materials and/or wastes, at least one propulsion mechanism for rotating the drum, at least one entrance for feeding the material and/or waste into the drum, at least one exit to discharge the materials and/or wastes from the drum, at least one inlet providing the oxygen needed for the reaction within the drum, and at least one outlet hole to exhaust the air and gases within the drum.    USE - The system is useful for aerobic fermentation (claimed) of organic materials and/or wastes.    ADVANTAGE - New constructions comprising a drum, which provides the recovery of organic materials and/or wastes with minimum energy, does not need an extra heat insulation, resistant to corrosive effects, and has an affordable price, are provided.    DETAILED DESCRIPTION - System for aerobic fermentation comprises at least one drum for fermenting the organic materials and/or wastes, at least one propulsion mechanism for rotating the drum, at least one entrance for feeding the material and/or waste into the drum, at least one exit to discharge the materials and/or wastes from the drum, at least one inlet providing the oxygen needed for the reaction within the drum, and at least one outlet hole to exhaust the air and gases within the drum; and the system further comprises a drum for keeping the heat arising as a result of the aerobic fermentation, which is made of polymer material for protection against corrosive effects.
NOVELTY - Method for producing crude cellulase cocktail from Trichoderma asperellum UPM1 and Aspergillus fumigatus UPM2 involves (a) growing T.asperellum UPM1 and A.fumigatus UPM2, (b) performing fermentation process using the obtained fungi with substrates that have been treated to obtain enzymes, and (c) recovering the enzymes from fermented products.    USE - The method is useful for producing crude cellulase cocktail from T.asperellum UPM1 and A.fumigatus UPM2, used for hydrolyzing lignocellulosic materials for fermentable sugars and for producing enzymes chosen from one or more of cellulases, xylanases, pectinases and any of their combinations (all claimed). The cellulose is useful in various industries including food, animal feed, biofuel, brewery, textile, pulp and paper, waste management, pharmaceutical, agriculture, and in research and development.    ADVANTAGE - The method is cost-effective and sustainable as the substrates utilized for celllulase production are easily available.
NOVELTY - The gasifier (10) has a primary chamber for receiving and holding waste to be gasified. A heat transfer chamber is fixed adjacent to the primary chamber, and is heated to heat the primary chamber and the waste. The primary chamber is lined with two distinct groups of refractory bricks. The two different groups of bricks are arranged such that upper section of refractory brick is fixed over a lower section of refractory brick. The lower section is more resistant to wear and abrasion, and the upper section is both more porous and include better insulating qualities.    USE - Gasifier for gasifying biomass obtained from dead animals, dead humans and materials and objects subjected to bacteria, viruses and other disease, and other waste.    ADVANTAGE - The gasifier can be utilized to gasify the biomass and other waste products in the safe, clean and environmentally friendly way, and without releasing harmful gases such as hydrogen and oxygen which oxidize to form water vapor and carbon dioxide and other harmless constituents and toxins to the environment. The gasification and combustion process can be controlled in an effective and fuel efficient manner. The combustion process is effectively performed. The gasifier is designed to minimize particulates in the fumes produced in the primary chamber and particulates that are exhausted by the exhaust flue, and the production of fly ash. The stable temperature is maintained in the primary chamber. The gasifier is designed to throw the biomass or the waste product in the end of the gasifying process, and the white ash that is generally free of carbon is remained.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the gasifier.    Gasifier (10)    Door (50)    Sealing section (50A)    Opening (54)    Heat exchanger (70)
NOVELTY - A substituted furan is produced in a multiphase reactor by feeding biomass and a gaseous acid into a multiphase reactor; and mixing the biomass and the gaseous acid in the presence of a proton donor and a solvent to form a reaction mixture. The reaction mixture has less than 10 wt.% of water.    USE - Method of producing substituted furan comprising halomethylfurfural (108) (including chloromethylfurfural or 5-(chloromethyl)furfural), hydroxymethylfurfural (110), and/or furfural (claimed) used as intermediate in preparing biofuels, diesel additives, and plastics.    ADVANTAGE - The method can prepare substituted furans from biomass containing cellulose (102) and/or hemicellulose (120) in a fast, efficient and cost-effective way.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a reaction scheme that shows the conversion of cellulose and hemicellulose into 5-(chloromethyl)furfural, 5-hydroxymethylfurfural, and furfural by acid-catalyzed hydrolysis and dehydration.    Cellulose (102)    Halogen-based mineral acid (104)    Halomethylfurfural (108)    Hydroxymethylfurfural (110)    Levulinic acid (112)    Formic acid (114)    Hemicellulose (120)
NOVELTY - The hydrogen separation tank has a cylinder hydrogen separation chamber which is provided with holders. A permanent magnet (12) is covered in stainless steel case, and is provided between cell plates (11) and connected to shaft with Z plate in between. Permanent magnet creates electromagnetic field when DC current passes through electrolyte solution. S or Z shaped stainless steel plate (13) is attached to shaft for increasing flow speed of electrolyte solution so as to increases reaction to produce hydrogen gas when electrical current passes through electrolyte solution.    USE - WDH3 hydrogen separation tank.    ADVANTAGE - As the stainless steel plate increases the flow speed of electrolyte solution so as to increases reaction to produce hydrogen gas when electrical current passes through electrolyte solution, the adequate hydrogen gas can be generated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the WDH3 hydrogen separation tank.    Lid (2)    Cell plate (11)    Permanent magnet (12)    Stainless steel plate (13)    Sensor (14)
NOVELTY - Absorbing carbon dioxide from a gas mixture, comprises contacting the gas mixture with an absorption medium comprising water and at least two different amines containing 2,2,6,6-tetramethyl-piperidine derivatives (I).    USE - The method is useful for absorbing carbon dioxide from a gas mixture.    ADVANTAGE - The method does not make use of solvent and thus it avoids the precipitation of solid during the absorption of carbon dioxide.    DETAILED DESCRIPTION - Absorbing carbon dioxide from a gas mixture, comprises contacting the gas mixture with an absorption medium comprising water and at least two different amines containing 2,2,6,6-tetramethyl-piperidine derivatives of formula (I) and (II).    R1, R2 = 1-4C n-alkyl.
NOVELTY - Capturing acid compounds in gas, comprises: (a) contacting gas with liquid solution that comprises mixture of aqueous phase and non-water miscible phase to produce solution of acid compound hydrates and acid compound depleted gas; (b) dividing solution into hydrate-rich fraction and fraction rich in non-water miscible phase; (c) separating hydrate-rich fraction from fraction rich in non-water miscible phase; (d) heating hydrate-rich fraction to release gaseous acid compounds to produce water-rich fraction; and (e) mixing fraction rich in non-miscible phase with water-rich fraction.    USE - The method is useful for capturing acid compounds (carbon dioxide or hydrogen sulfide) contained in a gas that is a combustion fume, a natural gas, a Claus tail gas, a syngas, a conversion gas or a biomass fermentation gas (all claimed).    ADVANTAGE - The method allows continuous operation.    DETAILED DESCRIPTION - Capturing acid compounds contained in a gas, comprises: (a) contacting the gas with a liquid solution that comprises a mixture of an aqueous phase and a non-water miscible phase to produce a solution of acid compound hydrates and an acid compound depleted gas; (b) dividing the solution that comprises acid compound hydrates into a hydrate-rich fraction and a fraction rich in non-water miscible phase; (c) separating the hydrate-rich fraction from the fraction rich in non-water miscible phase; (d) heating the hydrate-rich fraction to release gaseous acid compounds by dissociating the hydrates and to produce a water-rich fraction; and (e) mixing the fraction rich in non-miscible phase with the water-rich fraction to produce the liquid solution.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of capturing acid compounds in the gas.    Separating device (B1)    Mixing device (B2)    Pump (P2)    Contactor (R1)    Reactor (R2)
NOVELTY - Catalyst comprising 5-20 wt.% of nickel and 0-10 wt.% of cobalt supported on a support having aluminum oxide, and metal oxide (I) and (II), is new.    USE - The catalyst is useful for conversion of methane-rich gaseous mixture into hydrogen (claimed), and carbon dioxide reforming of methane-rich gases such as biogas.    DETAILED DESCRIPTION - Catalyst comprising 5-20 wt.% of nickel and 0-10 wt.% of cobalt (Co) supported on a support having aluminum oxide, metal oxide of formula (M1aOb-Al2O3) (I), and (M1aOb-ZrO2-Al2O3) (II), is new.    a = 1-2;    b = 1-3; and    M1 = Mg or Ca, where M1aOb is metal oxide salt, preferably MgO or CaO.    An INDEPENDENT CLAIM is included for a process for conversion of a methane-rich gaseous mixture into hydrogen comprising activating the catalyst under reducing conditions, and contacting a reactant comprising the methane-rich gaseous mixture with the activated catalyst under conditions for the conversion of the methane-rich gaseous mixture into a product comprising hydrogen.
NOVELTY - Preparing fuel pellets, comprises: (a) subjecting a feedstock to a torrefaction and partial pyrolysis step at 250-500 degrees C to obtain a solid char, and volatile fraction comprising a tar fraction; (b) at least partially condensing the volatile fraction to obtain a tar-rich fraction, where the tar-rich fraction is condensed onto the solid char, and then the solid char is combined with at least a part of the tar-rich fraction; and (c) pelletization of the combined solid char/tar-rich fraction to obtain the fuel pellets.    USE - The process is useful for preparing fuel pellets (claimed), which are useful in power plant boilers (grate, fluid or suspension fired boilers), district heating boilers, small pellet stoves, industrial process furnaces, kilns and boilers, small-scale heating devices, and barbecue grills.    ADVANTAGE - The process provides pellets that: has a tensile strength of at least 100 kPa; can be stored under out-door conditions on moist regions of the world e.g. in the Scandinavian countries; can be easily ground in a mill e.g. a coal mill to obtain a small particle size; and exhibits a high heating value density to minimize transport costs, a high pellet stability and hydrophobic properties of the pellets which make handling simple, minimized dust problems (thus reducing the risk of self-ignition and providing the option of out-door storage even in wet climates), and acceptable pellet ash properties (thus minimizing ash deposition, corrosion and flue gas cleanings equipment interference).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel pellet comprising a solid char, a tar, and, optionally, at least one additive.
NOVELTY - The system has a demand-forecast calculating unit (85) which estimates power electricity demand and heat demanding amount. An estimation energy consumption calculating unit (86) calculates estimation consumption regarding fuel required to generate the electric power input from a supply source. An optimal operation selection unit (87) selects an operating method of an electric power feeding heat plant based on calculated estimation consumption. A control unit controls the operation of electric power feeding heat plant in accordance with selected operating method.    USE - Cogeneration system installed in home.    ADVANTAGE - The consumption, heating and lighting expenses of primary energy can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of the cogeneration system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the operation-control apparatus. (Drawing includes non-English language text)    Operation-control apparatus (80)    Electric heat demand log storage unit (81)    Demand-forecast calculating unit (85)    Estimation energy consumption calculating unit (86)    Optimal operation selection unit (87)
NOVELTY - The method involves providing estimates of irreversible voltage loss and current voltage of fuel cell stack (12). A difference between the irreversible voltage loss and current voltage is determined (58) and analyzed to determine (60) whether the voltage difference is greater than voltage threshold. The voltage recovery process of fuel cell stack is performed (62) if the difference between the irreversible voltage loss and current power loss is greater than voltage threshold.    USE - Method for determining when a voltage recovery process of fuel cell stack is to be performed in fuel cell system for vehicle.    ADVANTAGE - The voltage recovery process of fuel cell stack in fuel cell system is realized so that efficiency of fuel cell stack is improved.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic view of the fuel cell system and flowchart explaining the process of determining when a voltage recovery process of fuel cell stack is to be performed.    Fuel cell system (10)    Fuel cell system (12)    Determining difference between irreversible voltage loss and current voltage (58)    Determining whether voltage difference is greater than voltage threshold (60)    Performing voltage recovery process of fuel cell stack (62)
NOVELTY - The apparatus has a fall part i.e. rotary valve (210), for dropping a solid raw material group (A) supplied from a raw material storage part. An inclined surface part (260) is arranged along perpendicular downward direction of the fall part. A collision surface (252) collides the solid raw material group provided in the inclined surface part and fell from the fall part and comprises an insertion opening i.e. lower opening (214b), that guides the solid raw material group along the inclined surface part from the collision surface to a reaction apparatus i.e. gasifier (114).    USE - Material input apparatus for supplying raw material e.g. wood coal, petroleum coke, biomass and tire chip, into a reaction apparatus i.e. gasifier, to generate electric power and manufacture hydrogen, synthetic fuel e.g. synthetic petroleum and chemicals such as chemical fertilizer. Can also be used for supplying raw material into a combustion furnace and an incinerator.    ADVANTAGE - The apparatus allows diameter of a flow hole in a throat unit to be small so as to prevent occlusion by the solid raw material group, to decrease injection quantity of fluid by a spray nozzle and to disperse the solid raw material group reliably, thus improving gasification efficiency of the solid raw material group in the gasifier. The apparatus allows powder of the solid raw material thrown into a connecting pipe part to flow backward with water vapor from the gasifier, so that the powder of the solid raw material can adhere with condensation of water vapor, thus allowing the solid raw material to be dispersed and injected into the connecting pipe part efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a material input apparatus.'(Drawing includes non-English language text)'    Solid raw material group (A)    Gasifier (114)    Rotary valve (210)    Lower opening (214b)    Collision surfaces (252, 262)    Inclined surface part (260)
NOVELTY - A biocoke manufacturing apparatus has a reaction container (2) filled with a biomass feedstock (14) and a pressurization head (3) for pressurizing the biomass feedstock in reaction container. The pressurization head is moved in an electro-hydraulic cylinder (1).    USE - Apparatus used for manufacturing biocoke (claimed).    ADVANTAGE - The biocoke manufacturing apparatus is compact. The biocoke is economically and efficiently manufactured using the apparatus. The fillability of biomass feedstock with respect to reaction container is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biocoke, which involves filling biomass feedstock in the reaction container, pressurizing feedstock through pressurization head, heating reaction container, cooling, throwing feedstock, and repeating insertion and pressurization. The angle of center shaft of reaction container and motion axes of pressurization head in horizontal direction is 30-75 degrees .    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biocoke manufacturing apparatus. (Drawing includes non-English language text)    Electro hydraulic cylinder (1)    Reaction container (2)    Pressurization head (3)    Sheath heater (6)    Biomass feedstock (14)
NOVELTY - The gasifier (10) has a granular material supply unit (14) which directly supplies a biomass granular material (11) inside a gasifier main portion (13). A water steam supply unit (16) supplies a water steam (15) for distribution from circumferences of the granular material supply unit or lower part sides of the granular material supply unit. A heat insulation unit is provided around the granular material supply unit. The water steam supply unit is provided in an outer side of the heat insulation unit.    USE - Biomass gasifier.    ADVANTAGE - Since the required amount of the water steam can be supplied from the circumference or the lower portion side as the assist gas for the distribution within the gasifier of the biomass granular material, the requirement of the large amount of the water steam can be avoided. Hence the liquid fuel can be manufactured more by using the generated gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasifier. (Drawing includes non-English language text)    Biomass gasifier (10)    Biomass granular material (11)    Gasifier main portion (13)    Granular material supply unit (14)    Water steam (15)    Water steam supply unit (16)
NOVELTY - An apparatus using carbon dioxide comprises fuel production part (101) to produce fuel using algae absorbing carbon dioxide from waste gas via photosynthesis, wherein hydrocarbon compound is generated through photosynthesis, waste gas supply part (103) to supply waste gas discharged from fuel using apparatus (102) and produced by chemical reaction of fuel containing carbon to fuel production part, fuel isolation part (104) to isolate fuel from algae of fuel production part, and fuel supply part (105) to supply fuel isolated by fuel isolation part to fuel using apparatus.    USE - An apparatus using carbon dioxide (claimed).    ADVANTAGE - Cost reduction is attained, carbon dioxide emitted from a discharging source is reduced, and carbon dioxide is effectively utilized by the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the apparatus using carbon dioxide. (Drawing includes non-English language text).    Fuel production part (101)    Fuel using apparatus (102)    Waste gas supply part (103)    Fuel isolation part (104)    Fuel supply part (105)
NOVELTY - The power distribution system has a fuel cell power generating unit which uses the hydrogen gas produced by an air cell electric power generating unit as fuel. A direct-current power supply source comprises an object for grid connection and a secondary battery for off-peak electric power electrical storage. A reverse power-flow timer controller reverses the flow of power from the direct-current power supply source to a commercial power source (5) based on the off-peak electric power utilization and/or off-peak electric power storage.    USE - Power distribution system for use as independent power supply facility.    ADVANTAGE - Reduces scale of commercial power source. Secures solar cell electric power generation, wind power generation, wave-powered electricity generation and air cell electric power generation. Ensures safe and economical independent power supply. Reduces electrical power generation unit price.    DESCRIPTION OF DRAWING(S) - The drawing shows the systematic diagram of the implementation of a power distribution system. (Drawing includes non-English language text).    Solar cell (1)    Magnesium anode air cell (2)    Fuel cell (3)    Secondary battery (4A,4B)    Commercial power source (5)
NOVELTY - Method of preparing hydrogen storage material, involves mixing tetrahydridoborate salt and magnesium salt, dissolving obtained mixture in solvent, reacting tetrahydridoborate salt and magnesium salt, removing precipitate, removing solvent from filtrate, and applying pressure at 80 degrees C or less and 400 Mpa or more to residue.    USE - The method is useful for preparing hydrogen storage material (claimed) which is used for storing liquid hydrogen. The liquid hydrogen is used as fuel.    ADVANTAGE - The method provides improved storage and transport efficiency of hydrogen and is environmentally friendly.
NOVELTY - A hydrogen generating apparatus has a modifier (20) which reform-reacts a raw material to generate hydrogen-containing-gas, a transformer (21) which reduces carbon monoxide in hydrogen-containing-gas by shift reaction, a carbon monoxide removal device (22), and a hydrodesulfurization device (23). In the downstream, at least one portion of hydrodesulfurization device adjoins carbon monoxide removal device such that heat conduction is carried out.    USE - Apparatus is used for generating hydrogen used as fuel.    ADVANTAGE - The hydrodesulfurization device of hydrogen generating apparatus efficiently improves adsorption capacity of hydrogen sulfide.    DETAILED DESCRIPTION - A hydrogen generating apparatus has a modifier which reform-reacts a raw material to generate hydrogen-containing-gas, a transformer which reduces carbon monoxide in hydrogen-containing-gas by shift reaction, a carbon monoxide removal device which reduces carbon monoxide in hydrogen-containing-gas which passed transformer in methanation reaction and/or oxidation reaction, and a hydrodesulfurization device which removes sulfur compound in raw material. In the downstream, at least one portion of hydrodesulfurization device adjoins carbon monoxide removal device such that heat conduction is carried out.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Combustion pipe (10)    Modifier (20)    Transformer (21)    Carbon monoxide removal device (22)    Hydrodesulfurization device (23)
NOVELTY - Method for preparing anhydrosugar alcohol, involves dehydrating hexitol using mixture of acid including first acid and second acid to produce anhydrosugar alcohol, and purifying the anhydrosugar alcohol, where the first acid is sulfuric acid and second acid is at least one of sulfur-containing acid or its salt chosen from p-toluenesulfonic acid, methanesulfonic acid, ethanesulfonic acid, benzenesulfonic acid, naphthalenesulfonic acid and aluminum sulfate.    USE - The method is useful for preparing anhydrosugar alcohol chosen from isosorbide, isomannide and isoidide (all claimed) is used as adhesive in patches and drugs including mouthwash and as industrial raw material in manufacturing process of heat resistant polyethylene terephthalate, polyester fiber, high-strength sheets, films and polyethylene.    ADVANTAGE - The method simply provides excellent yield of alcohol, has low recovery cost, production cost and high conversion rate of hexitol, and utilizes environmentally-friendly plasticizers and polyesters and inexpensive catalyst.
NOVELTY - Aerosol-type skin washing substance comprises N-acylglycine or N-acyl methyl alanine amino acid type surfactant, polyglyceryl fatty acid ester, polyhydric alcohol, liquefied petroleum gas (LPG), and carbon dioxide gas.    USE - The aerosol-type skin washing substance is useful as face washing substance, cleansing cosmetics, hand soap, and body shampoo.    ADVANTAGE - The aerosol-type skin washing substance reduces irritation without impairing foam quality, provides skin lightness and refresh feel, and has excellent cleaning effect with respect to pollution.
NOVELTY - An aerosol-type cleaning material contains N-acyl glutamic acid-type surfactant, alkylamino dicarboxylic acid-type surfactant, polyhydric alcohol, liquefied petroleum gas and carbon dioxide gas.    USE - Aerosol-type skin cleaning material is used for face wash, body shampoo and hand soap.    ADVANTAGE - The aerosol-type skin cleaning material has excellent foaming quality, and reduced irritation.
NOVELTY - The apparatus has a material input section whose shredder is utilized for shredding biomass and waste products to produce a shredded material. A set of inclined pyrolysis unit housings of a pyrolysis section is arranged in tandem for pyrolizing a material to produce a pyrolyzed product. A generating section of the pyrolysis section is operably associated with the housings for producing electrical energy. A hydrogen production system (36) of a fractionating section (18) is operably associated with a closed fractionating tower (34) of the fractionating section for producing hydrogen.    USE - Apparatus for producing electrical energy and liquid hydrocarbons from oil sands/bitumen, biomass and waste products by pyrolysis process.    ADVANTAGE - The apparatus is operably associated with the pyrolysis subsystem with a gas clean-up equipment installed intermediate to a catalytic converter and the closed fractionizing tower, and a gas turbine generator and a membrane oxygen extraction subsystem, for removal of chlorine and other compounds and/or contaminates, thus cleaning the gases received by the pyrolysis subsystem without lowering the temperature to a level for initiating condensation, and hence producing clean electrical energy and liquid hydrocarbons, and obtaining by-products from biomass, waste products and oil sand.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for producing electrical energy and liquid hydrocarbons.    Fractionating section (18)    Closed fractionating tower (34)    Hydrogen production system (36)    Turbine generator (38)    Electrical sub-station (42)
NOVELTY - Magnetic catalyst comprises: a carrier consisting of strong-acid or weak-acid cationic exchange resin, metal, or surface activated non-metal; a first nano metal shell wrapping and contacting a surface of the carrier; and a second nano metal shell wrapping the first nano metal shell, where the first and second nano metal shells have different compositions, and at least one of the first and second nano metal shells consists of iron, cobalt, or nickel.    USE - As magnetic catalyst (claimed), used in hydrogen supply device.    ADVANTAGE - The magnetic catalyst with high catalyst efficiency can be applied in a hydrogen supply device, and the device can be connected to a fuel cell. Because the magnetic catalyst can be recycled by a magnet after generating hydrogen, the practicability of the noble metals such as Ru with high catalyst efficiency is dramatically enhanced.    DETAILED DESCRIPTION - Magnetic catalyst comprises: a carrier consisting of strong-acid or weak-acid cationic exchange resin, metal, or surface activated non-metal; a first nano metal shell wrapping and contacting a surface of the carrier; and a second nano metal shell wrapping the first nano metal shell, where the first and second nano metal shells have different compositions, and at least one of the first and second nano metal shells consists of iron, cobalt, or nickel, where the magnetic catalyst is contained in a hydrogen supply device to release hydrogen, and the hydrogen supply device is connected to a fuel cell, where the first and second nano metal shells are shells containing metal with a nanosize respectively.
NOVELTY - A gas permeation membrane comprises polyimide including repeating unit (I).    USE - Gas permeation membrane is used for water-ethanol separation, separation and immobilization of carbon dioxide from liquefied natural gas, and ethanol recovery for fuels.    ADVANTAGE - The gas permeation membrane has excellent gas separation characteristics, physical properties, swelling resistance, mechanical design and strength, and high gas permeability coefficient.    DETAILED DESCRIPTION - A gas permeation membrane comprises polyimide including repeating unit of formula (I).    R1=divalent organic group containing 2-hydroxy-1,1,1,3,3,3-hexafluoro isopropyl, in which OH is substituted by glycidyl group;and    R2=tetravalent organic group.    Cyclic ether portion of glycidyl group is ring-opens and crosslinks.
NOVELTY - The organic garbage processing box has separating plate that is provided with liquid passing hole of the partition board for collecting waste liquid. The collecting groove is provided with inclined structure so that waste liquid is collected in collection groove. One end of the box portion is provided with a top opening so that separate layer is taken out from the box portion and used as compost for cultivating earthworm.    USE - Organic garbage processing box for peasant family.    ADVANTAGE - The box is simple in structure, the space occupied by the box is reduced and garbage treatment efficiency is improved.
NOVELTY - The cracker has a feeding device arranged on an upper end of a pyrolysis chamber. An air blower is linked with a pyrolysis chamber and a fire cylinder. A lower end of the feeding device is provided with an air locking feeding device that is provided with a motor. The motor is installed on the feeding device. An upper end of the pyrolysis chamber is provided with an emergency discharge device and linked with a cracking chamber. An opening part of the fire cylinder is arranged with a tangential rotational flow guide device. The blower is linked with a primary air pipe and a secondary air pipe.    USE - Biomass fuel cracker.    ADVANTAGE - The cracker prevents fuel in the feeding device from leaking so as to improve cracking efficiency. The cracker is convenient to operate, and has high safety factor, strong practicability and low equipment cost, and simplifies production process, reduces tar generation rate and heat energy consumption and improves burn-off rate.
NOVELTY - The bacteria propagation device has culture box which is provided with automatic feeding and discharging device and automatic medicine-adding device. The bottom portion of the culture box is provided with a drain valve. The culture box is provided with an external circulating device.    USE - Automatic bacteria propagation device used in sewage treatment field.    ADVANTAGE - The production efficiency of the propagation device can be improved with improved culturing effect and improved operability.
NOVELTY - Bio-organic fertilizer comprises (in parts by wt.) poultry excrement (62-96), crop waste (13-40), scouring scrap (10-42), biological culture (0.2-0.5) and microelements (0.15-2).    USE - Used as bio-organic fertilizer.    ADVANTAGE - The fertilizer: has high efficiency; utilizes solid waste as raw materials and hence economical and ensures the reutilization of abandoned harmful resources; is environment-friendly; reduces the chemical fertilizer usage to 20-30%; and replaces the existing composting method by utilizing biological inoculum, poultry excrement, crop straw, scouring scrap and other organic waste. The method requires low investment, saves time, and ensures the fertilizer quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-organic fertilizer comprising adding poultry excrement into a mixed fermentation tank for pre-fermentation, adding biological culture into the mixed fermentation tank, fermenting the materials until the color of the materials turns puce and the manure and compost odor is absent, mixing the fermented materials with crushed crop waste and scouring scrap, turning over, crushing and sieving the complex materials, mixing and pelletizing humic acid, microelements, mineral substance and the sieved materials, and drying, cooling, sieving the granular material, and packaging to obtain finished products.
NOVELTY - Fermenting organic fertilizer by using effluent containing ammonia tail gas, comprises (i) composting, and fermenting the organic fertilizer raw material, inoculating zymophyte, and ensuring the complete decomposition of the organic fertilizer raw material; (ii) pressing effluent ammonia tail gas, and conveying to air injection pipelines; (iii) injecting the effluent ammonia tail gas to the organic fertilizer raw material pile by air holes, and injecting; and (iv) reducing the carbon nitrogen ratio of completely decomposed organic fertilizer raw material to 20-25:1.    USE - The method is useful for fermenting organic fertilizer by using effluent containing ammonia tail gas.    ADVANTAGE - The method utilizes the effluent ammonia tail gas as a regulator to increase the nitrogen content in the organic fertilizer, which thoroughly decomposes the organic fertilizer raw material.    DETAILED DESCRIPTION - Fermenting organic fertilizer by using effluent containing ammonia tail gas, comprises (i) composting, and fermenting the organic fertilizer raw material with carbon nitrogen ratio (C/N) of 28-40:1 in a composting tank, inoculating zymophyte, and ensuring the complete decomposition of the organic fertilizer raw material; (ii) pressing the effluent ammonia tail gas with a draught fan after completing the first fermentation, and then conveying to many rows of air injection pipelines which are horizontally arranged at the bottom of the composting tank, where the air injection pipelines are drilled with air holes at intervals; (iii) injecting the effluent ammonia tail gas to the organic fertilizer raw material pile by the air holes from bottom to top, and injecting for 2-3 times every day for 60-70 minutes; and (iv) reducing the carbon nitrogen ratio of completely decomposed organic fertilizer raw material to 20-25:1.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for carrying out the above mentioned method.
NOVELTY - Purifying a biogas slurry by illumination intensity adjusting strategy, comprises: (a) providing and testing a growth condition and purification effect of micro-algae culture under a condition of constant LED lamp light sources with different quality; (b) gradually increasing the illumination intensity of the experiment, testing growth condition and purification effect of the micro-algae, and determining the different growth period under optimal illumination intensity; and (c) selecting the micro-algae with good illumination intensity and purifying effect.    USE - The method is useful for purifying biogas slurry by illumination intensity adjusting strategy.    ADVANTAGE - The method is capable of purifying biogas slurry in a simple, cost-effective and less energy consuming manner.
NOVELTY - Fully-mechanical solar fermentation device comprises an organic fertilizer raw material pre-processing device, a solar energy high-temperature fermenting and drying front section, and a solar energy high-temperature fermenting and drying rear section. The piling height of the raw materials fermented in the two sections is respectively adjusted by a lifting baffle plate. The materials in the two sections are fermented during their mechanical transportation into a discharging pushing mechanism by a plate-type conveyor belt (has integral width of 4-6 m and total length of 40-100 m).    USE - The device is useful for producing organic fertilizers.    ADVANTAGE - The device: utilizes solar energy and fermentation to adjust the material piling and fermentation period without using an external heat source; ensures complete mechanical operation from the feeding step to the discharging step; saves energy; and reduces emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the fully-mechanical solar fermentation device.
NOVELTY - Insecticidal fertilizer comprises (in parts by wt.) Chrysanthemum (6-10) and a fertilizer composition (90-94). The Chrysanthemum comprises all types of natural Chrysanthemum plants. The fertilizer composition comprises nitrogen, phosphorus and potassium raw material fertilizer, trace element fertilizer and organic fertilizer.    USE - The insecticidal fertilizer is useful for controlling underground pests.    ADVANTAGE - The insecticidal fertilizer: ensures strong insecticidal effect, high efficiency, broad insecticidal spectrum and simple preparation; is ecofriendly; and does not leave any residue in plant body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the insecticidal fertilizer, comprising (i) completely drying Chrysanthemum plants, cutting into fragments, and crushing into 120-200 meshes, (ii) mixing the product (6-10 parts) obtained from the step (i) with the fertilizer composition (90-94 parts), (iii) granulating the mixture obtained from the step (ii), and sieving, and (iv) mixing the sieved powder obtained from the step (iii) with the powder obtained from the step (ii), and granulating.
NOVELTY - Macromolecule degradable coating material reactor comprises a reactor cylinder body and an enclosure on the upper end. The enclosure is provided with a feeding opening. The lower end of the reactor cylinder body is provided with a material outlet. The sidewall of the reactor cylinder body is provided with a steam inlet and a steam outlet. The inner cavity of the reactor cylinder body is provided with a heating coil pipe. Two ends of heating coil pipe are respectively connected with steam inlet and steam outlet. The heating coil pipe comprises small and large curvature sections at intervals.    USE - Macromolecule degradable coating material reactor.    ADVANTAGE - The small and large curvature sections can carry out heat at different positions, and self-generated heat circulation in the inner cavity of the reactor cylinder, which improves the heating efficiency, and is good for uniformly dispersing heat, thus improving the heat efficiency and reducing the energy consumption.
NOVELTY - Device comprises sludge feeding machine, sludge discharge hole, inclined conveyor belt provided with fermented auxiliary material at lower side of the sludge discharge hole, spiral conveyer, transmission belt provided with sludge filter cake, crushing stirrer, and fermentation tank.    USE - The device is useful for preparing organic fertilizer using organic sludge.    ADVANTAGE - The device is environmentally-friendly.
NOVELTY - The apparatus has fermentation unit having mixture which is ejected in cyclone discharger to allow mixture in transfer pipe. A transfer pipe transfers the mixture ejected in mixed unit and blower infuses air inside transfer pipe to transfer the mixture. A water control agent is provided for injecting organic waste in which microorganism is contained for injecting water control agent to discharge inside dispersion conveying unit. A compost return unit returns a portion among compost which is shipped from compost shipment unit to carrier input unit.    USE - Apparatus for composting treatment of organic wastes.    ADVANTAGE - The diffusion of the bad smell can be prevented. The air heated by the fermentation unit is supplied to rot unit, so the organic waste can be efficiently composted. The diffusion of the bad smell can be suppressed and the cost for composting treatment apparatus can be reduced.
NOVELTY - A cultivable viable but nonculturable (VBNC) arthrobacterium DSC4 strain (CCTCC No: M2011406) is recovered.    USE - Recovery of cultivable viable but nonculturable arthrobacterium DSC4 strain used in denitrification method for biological sewage treatment system (claimed).    ADVANTAGE - The recovery of cultivable VBNC arthrobacterium DSC4 strain provides for nitrate nitrogen conversion rate of 54.7% and total nitrogen depletion rate of 52.9%, with no residue of ammoniacal nitrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an activation medium of the arthrobacterium DSC4 strain comprising 1-3 g of the nutrient-broth-medium, 0.2-0.5 g of yeast extract, 1.5-5 g of glucose, 1-4 vol.% of agar, 2-20 vol.% of recovery culture liquid containing resuscitation promoting factor, and 1000 ml of de-ionized water; and    (2) preparation of the activation medium comprising weighing the nutrient-broth-medium, yeast extract, glucose, and de-ionized water, adjusting the pH to 7, adding agar, performing high temperature sterilization for 10-30 minutes at 110-130 degrees C, cooling to room temperature, adding recovery culture liquid after filtration, uniformly stirring, drying to solid, and preserving at 4-10 degrees C.
NOVELTY - Method for treatment of antibiotic pharmaceutical wastewater, involves (a) treating pharmaceutical wastewater by adsorption and precipitation, controlling chemical oxygen demand (CODCr) to below 10000 mg/l, and adjusting pH, (b) introducing pretreated pharmaceutical wastewater to reactor with immobilized biological enzyme, maintaining waste water for predetermined time, controlling pH and temperature, and (c) introducing the obtained water to fluidized bed with immobilized activated sludge, aerating, and controlling the temperature.    USE - The method is useful in treatment of antibiotic pharmaceutical wastewater.    ADVANTAGE - The method reduces formation and proliferation of superbugs, and does not use antibiotic resistance effects of genetically engineered bacteria or by pure cultures of separation of natural bacteria.    DETAILED DESCRIPTION - Method for treatment of antibiotic pharmaceutical wastewater, involves (a) treating pharmaceutical wastewater by adsorption and precipitation, controlling chemical oxygen demand (CODCr) to below 10000 mg/l, and adjusting pH to 6-6.5 using sodium carbonate, (b) introducing pretreated pharmaceutical wastewater to reactor with immobilized biological enzyme, maintaining waste water in reactor for 2-3 hours, controlling pH to 6-6.5, and controlling temperature to 50-60 degrees C, and (c) introducing the obtained water to fluidized bed with immobilized activated sludge, aerating for 12-15 hours, and controlling the temperature at 15-35 degrees C and pH at 7-10, where the volume ratio of activated sludge and wastewater is 1:4-7.
NOVELTY - A common Chlorella vulgaris, where the C. vulgaris is C. vulgaris C9-JN2010, the preservation number is: CCTCC NO: M2010373, is new.    USE - The common C. vulgaris is useful in sewage treatment; and in lipid production (all claimed).    ADVANTAGE - The common C. vulgaris is highly efficient and effective in sewage treatment and in lipid production. Also, it is cost effective and environment friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of culturing the common C. vulgaris, comprising: in a photoreactor, taking the secondary effluent of the municipal wastewater and/or the industrial wastewater after treated by the wastewater treatment plant as the culture medium, inoculating the common C. vulgaris, the initial inoculation density is 1.0x107 to 6.0x107 cfu/ml, the culture condition is as follows: the photoperiod is from 10:14 hours to 16:8 hours, the photoperiod density is 5000-15000 lux, the culture temperature is 20-30 degrees C, the pH value is 6.5-8.5, the aeration rate of the carbon dioxide (CO2) gas is 0.01-0.2 VVm, the CO2 concentration is 15.0-30.0% (v/v).
NOVELTY - Producing methane by ammonia-biological combined treatment of wheat straw fermentation comprises performing mixed anaerobic fermentation of wheat straw by successively performing ammonia and biological preprocessing to produce methane.    USE - The method is useful for producing methane by ammonia-biological combined treatment of wheat straw fermentation.    ADVANTAGE - The method ensures efficient and stable preparation of methane from wheat straw, has short fermentation period, produces large volume of gas with high methane content, solves the problem of producing gas by anaerobic digestion of wheat straw waste, and ensures recycling of energy and wheat straw.
NOVELTY - Treating agriculture and forestry waste with cellulose, hemicelluloses and lignin, comprises grinding the agriculture and forestry waste, steam blasting, washing and separating to get the solid phase and liquid phase; delivering the liquid phase of hydrolysate with hemicelluloses to the methane fermentation room to generate methane; performing enzymolysis to the solid phase with cellulose and lignin, alcohol fermenting, distilling and rectifying to get ethanol product.    USE - The method is used for treating agriculture and forestry waste with cellulose, hemicelluloses and lignin (claimed).    ADVANTAGE - The treatment method above has low cost.
NOVELTY - Producing fuel butanol using kitchen wastes comprises adding 0-1% of mixed enzyme preparation into the kitchen waste, controlling the temperature at 30-50 degrees C to conduct enzyme treatment, adding zymocyte liquid (1-5 mass%) of the kitchen wastes for 0-20 hours after adding the mixed enzyme preparation, controlling the temperature at 30-50 degrees C to seal, fermenting for 48-80 hours, after finishing the fermentation, and extracting the solution using the ethyl acetate to obtain butanol.    USE - The method is useful for producing fuel butanol using kitchen wastes.    ADVANTAGE - The method reduces pollution of kitchen wastes on the environment, recycles the kitchen wastes and solves the problems of oil shortage, food shortage and environmental deterioration.
NOVELTY - Using comprehensively spirit vinasse to produce high performance white carbon black and succinic acid comprises using vinasse after fermentation liquor as raw material, washing the residue and rice hull separating, a slag pressing, filtering, drying, pulverizing, sieving through 80-100 meshes, fermenting Actinobacillus, filtering, then decoloring with active carbon to obtain the butane diacid, acid cleaning, filtering, alkali dissolving, filtering, adding chelating agent, aging, washing, spraying and drying to obtain high performance white carbon black.    USE - The method is useful for using comprehensively spirit vinasse to produce high performance white carbon black and succinic acid (claimed).    ADVANTAGE - The method develops high performance white carbon black, and has high popularization value in industry.    DETAILED DESCRIPTION - Using comprehensively spirit vinasse to produce high performance white carbon black and succinic acid comprises using vinasse after fermentation liquor as raw material, washing the residue and rice hull separating, a slag pressing, filtering, drying, pulverizing, sieving through 80-100 meshes, fermenting Actinobacillus, filtering, then decoloring with active carbon to obtain the butane diacid, the rice separated by burning the rice hull ash to crush 80-100 mesh sieve, acid cleaning, filtering, alkali dissolving, filtering, adding chelating agent, aging, washing, spraying and drying to obtain high performance white carbon black.
NOVELTY - Saccharomyces cerevisiae engineered fungus AY-510B24M has a preservation number of CGMCC No.5843, is new.    USE - The fungus is useful for producing ethanol fuel by using lactose.    ADVANTAGE - The ethanol produced has high tolerance fungus which is not affected during fermentation process.
NOVELTY - Ethanol-gasoline mixture comprises ethanol, gasoline, and fuel additive. The fuel additive comprises acetone, isopropyl alcohol, fatty acid ester, polyglycol ether, fatty acid polyglycol ether and surfactants.    USE - As ethanol-gasoline mixture.    ADVANTAGE - The fuel additive increases torque by 15-25% at low speed of revolutions, thus enables to reduce the proportion of the gasoline component while keeping the safety of start and without increasing fuel emissions, where the ethanol-gasoline mixture contains more gasoline component than required for normal operation to improve cold start characteristics.
NOVELTY - The apparatus has an infrared radiation burner (6) that heats material to be cracked. The carbonized substance is moved from tube (4) to lateral portion of reactor (1) to form soot ash that is moved to chamber (19) for transforming into methane, carbon dioxide and carbon-free ash. The hydrocarbons (C5-C35) are obtained by condensing produced vapors. The heterogeneous gases are transformed to homogenous methane in pyrolysis chamber (7) to form neutral ash as by-product, and mixture of liquid hydrocarbons and pure methane, pure carbon dioxide and nitrogen gas as main product.    USE - Apparatus for recycling organic and inorganic hydrocarbons such as biomass, rubber, rubber wastes such as wired rubber, plastics, and plastic waste, using infrared cracking process.    ADVANTAGE - The organic and inorganic hydrocarbons recycling apparatus is operated continuously. The organic and inorganic hydrocarbons are recycled efficiently by the hydrocarbons recycling apparatus by universal energetic process such as thermal cracking process through infrared radiation.    DETAILED DESCRIPTION - A base stock of recycling apparatus is attached to cracking reactor through vertical reactor screw (3). The soot ash is moved to the oxidation chamber through discharging screws (12) and feeding unit (18).    DESCRIPTION OF DRAWING(S) - The drawing shows the organic and inorganic hydrocarbons recycling apparatus.    Cracking reactor (1)    Vertical reactor screw (3)    Vertical reactor tube (4)    Infrared radiation burner (6)    Pyrolysis reaction chamber (7)    Discharging screw (12)    Feeding unit (18)    Oxidation chamber (19)    Liquid hydrocarbons (C5-C35)
NOVELTY - Loading cefazolin and chitosan composite drug membrane on microarc oxidation titanium implant comprises placing titanium implant into stainless steel groove; controlling micro-arc oxidation electric parameter; forming micro-arc oxidation coating on surface of titanium; adding cefazolin solution into chitosan solution, stirring and preparing mixed solution of cefazolin, and chitosan; soaking titanium matrix into mixed solution of cefazolin and chitosan; and taking out micro-arc oxidation titanium implant, and drying in drying oven.    USE - Method for loading cefazolin and chitosan composite drug membrane on microarc oxidation titanium implant.    ADVANTAGE - The method is simple to operate, low in cost and environment-friendly, and introduces harmless substances into micro-arc oxidation coating and composite drug membrane.    DETAILED DESCRIPTION - The method comprises:    (A) placing titanium implant into stainless steel groove with alkaline electrolyte; controlling micro-arc oxidation electric parameter by using double-electrode pulse power supply; and forming micro-arc oxidation coating on surface of titanium through disruptive discharge, where pulse voltage is 200-500 V, frequency is 400-800 Hz, duty ratio is 4-20%, solution temperature is 0-50 degrees C and oxidation time is 5-30 minutes;    (B) adding cefazolin solution into chitosan solution, then stirring and preparing mixed solution;    (C) soaking Ti matrix into mixed solution of cefazolin and chitosan; and    (D) taking out micro-arc oxidation Ti implant, and drying in a drying oven.
NOVELTY - Incarvine is prepared by using horned Artemisia herbs as raw materials, crushing, adding 60-80% methanol solution, performing microwave extraction for 2-3 times, and recovering methanol under reduced pressure; and adding hydrochloric acid into concentrated liquid, adjusting pH to 3, filtering, adding into nanofiltration membrane system and performing nanofiltration, and adding into macroporous resin.    USE - Method for the preparation of incarvine (claimed).    ADVANTAGE - The method has low energy consumption and low pollution, is safe and practical.    DETAILED DESCRIPTION - Preparation of incarvine comprises:    (A) using horned Artemisia herbs as raw materials, crushing, adding 60-80% methanol solution, performing microwave extraction for 2-3 times, and recovering methanol under reduced pressure;    (B) adding hydrochloric acid into concentrated liquid, adjusting pH to 3, filtering, adding into nanofiltration membrane system and performing nanofiltration, and adding into macroporous resin;    (C) adding into nanofiltration membrane system and performing nanofiltration, adjusting pH of concentrated liquid to 9-12, adding petroleum ether chloroform and extracting, collecting organic layer and concentrating, refrigerating and crystallizing, refluxing for 2-3 times, and drying at low temperature to obtain incarvine.
NOVELTY - Organic sewage collected in a sewage collection tank is supplied to a sewage adjusting pool, and microorganisms are added for purifying and deodorizing wastewater. The microbial preparation comprises pesticide, deodorant and vanillin. The pretreated sewage is subjected to fungi acid fermentation at room temperature and atmospheric pressure under anaerobic conditions. The sewage is then passed through a 6-filter reactor and processed with phosphoric acid bacteria, carbon bacteria, fire fungus, and microbial fungus to obtain a composite liquid fuel.    USE - Manufacture of composite liquid fuel.    ADVANTAGE - The method is simple, economical and environmentally-friendly.
NOVELTY - The invention consolidates the flow-through hydrothermal and relieving pressure/steam-explosion to a pretreatment apparatus and method related to the production of cellulosic ethanol. The process can remove monosaccharide and oligosaccharide extracted from hemicellulose and cellulose immediately in avoiding their degeneration at high pretreatment temperature. The integrated process of flow-through hydrothermal and relieving pressure/steam-explosion pretreatment successfully is able to improve the sugar recovery in hydrolysate up to 70% and apply relieving pressure/steam-explosion to facilitate the subsequent enzymatic hydrolysis efficiency to reach 90% at the same time. Thus, the apparatus and method can increase the utility of holocellulose (cellulose and hemicellulose) in the feedstock and improve the competitiveness of cellulosic ethanol industry.
NOVELTY - A metal glaze ceramic tile has a metal cover glaze layer and a printing glaze layer sequentially arranged on a blank layer as a ground glaze layer.    USE - Metal glaze ceramic tile.    ADVANTAGE - The metal glaze ceramic tile has excellent glossiness, and suppressed precipitation and fogging defects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of metal glaze ceramic tile, which involves feeding raw materials to hopper, ball milling ground glaze for 8-9 hours and screening milled glaze by sieve of 325 meshes to obtain powder, ball milling cover glaze for 3-4 hours and screening milled glaze by sieve of 325 meshes to obtain powder, spray granulating, compressing, pressing and molding raw materials of blank, glaze spraying ground glaze, spraying cover glaze for 35-40 seconds, screen printing, glaze firing at 1120 degrees C for 110 minutes, packaging and warehousing.
NOVELTY - Solid particles in domestic sewage are crushed. Seawater and sewage are mixed and subjected to electroflocculation treatment. Then, resultant sewage is subjected to electrolysis, oxidized, and at same time, sodium hypochlorite is produced. The electrolyzed sewage is continuously sterilized, and produced hydrogen is discharged. A controlled release agent is automatically added into sewage, and residual chlorine in sewage is processed by neutralization. Processed sewage is discharged outside ship. Thus, domestic sewage treatment of composite ship is carried out.    USE - Domestic sewage treatment of composite ship.    ADVANTAGE - The domestic sewage of composite ship is safely and effectively treated by simple method. The water obtained by treating domestic sewage of composite ship has high quality.    DETAILED DESCRIPTION - Solid particles of domestic sewage are crushed using crushing pump and collected in a tank. Predetermined amount of seawater and sewage are mixed and the mixture is passed into electric coagulation device for electroflocculation treatment, to remove flocculation slag floating and sinking solids. Then, the resultant sewage is pumped into electrobath for electrolysis using a water pump (A), the sewage is oxidized in electrolytic groove, and at same time, sodium hypochlorite is produced to kill colon bacillus. The electrolyzed sewage is flown into oxidation collecting tank, continuously sterilized, and hydrogen produced in the collecting tank is discharged. The sewage is passed into neutralization unit, residual chlorine analyzer in the neutralizing unit automatically detects residual chlorine in sewage, controlled release agent is automatically added into the sewage, and residual chlorine in the sewage is processed by neutralization. The processed sewage is discharged outside ship through water pump (B). Thus, domestic sewage treatment of composite ship is carried out.
NOVELTY - A controller (1001) controls flow speed and microwave power of fuel and water. A power supply regulator (1019) adjusts the power of microwave generation magnetron (1020) which converts the electric energy to the microwave having the frequency of 2.45 GHz. The microwave generation magnetron cools the liquid cooling agent (1006). The liquid fuel and water are entered into evaporator (1008) to evaporate and form steam to enter into microwave resonant cavity (1018). A spark ignition device (1017) is controlled by controller to excite chemical substance in inner cavity of reforming device.    USE - Low temperature plasma reforming system for producing hydrogen of vehicle.    ADVANTAGE - The structure of the plasma reforming system can be simplified. The efficiency of the plasma reforming system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plasma reforming system.    Controller (1001)    Liquid cooling agent (1006)    Evaporator (1008)    Spark ignition device (1017)    Microwave resonant cavity (1018)    Power supply regulator (1019)    Microwave generation magnetron (1020)
NOVELTY - The method involves obtaining a liquid component in an analytical separation station (10). A more valuable fraction liquid is treated in a generic anaerobic reactor (17). A less valuable fraction liquid is treated in a composting plant (13). A high-grade organo-mineral fertilizer is obtained. A solid component obtained by a squeezing process in an integrated generation of Solid fuel and biogas from biomass (IFBB) technology plant is dried in a drying room (7) and pelletized in a pelletizing press (8). A screw press is provided with a sieve to separate liquid and solid components.    USE - Method for processing a biodegradable organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method processing biodegradable organic waste.    Drying room (7)    Pelletizing press (8)    Analytical separation station (10)    Composting plant (13)    Generic anaerobic reactor (17)
NOVELTY - Producing hydrogen by solar photocatalytic water splitting, comprises using oxalic acid as a sacrificial agent.    USE - The method is useful for producing hydrogen by solar photocatalytic water splitting.    ADVANTAGE - The method improves photoelectric conversion efficiency, improves the photocurrent and increases the quantity of hydrogen produced per unit time; and has stable hydrogen production rate by the photocatalytic hydrogen production system containing oxalic acid.
NOVELTY - The gasifier has a coolant conduit surrounding a portion of a slurry tube. An atomizing gas conduit is placed in fluid communication with atomizing gas apertures to contact atomizing gas with material exiting an outlet of the slurry tube. A tubular shaped reactor vessel is placed in fluid communication with the outlet of the slurry tube and the atomizing gas apertures. A heating conduit surrounds a portion of the vessel. The vessel is placed in fluid communication with an ash recovery system. A source of microwave radiation heats material placed within the vessel.    USE - Tunable catalytically heated gasifier for gasifying fossil/naturally-occurring fuel e.g. coal, biomass and atomized coal slurry.    ADVANTAGE - The gasifier allows a catalytic combustor to include platinum-based catalyst that reacts with carbon monoxide and oxygen to evolve heat in a catalytic converter, so that the converter can convert the carbon monoxide and the oxygen to carbon dioxide. The gasifier ensures high pressure operation, and has high throughput with reduced capital cost.    DETAILED DESCRIPTION - The gasifier includes fluid, which is selected from a group consisting of carbon monoxide, hydrogen and methane. An INDEPENDENT CLAIM is also included for a method for gasifying fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an arrangement illustrating a method for gasifying fuel.
NOVELTY - Collapsible cylindrical composter is constructed using flexible fabrics, where the composter can be opened to add or remove material, and can be rolled along a surface or ground when closed.    USE - The composter is useful for composting of organic materials.    ADVANTAGE - The composter does not require large space, is cost-effective, can be collapsed without any disassembly and stored away in seconds, can be easily closed , allows greater air circulation that aids composting process, and contains drainage holes that allow excess fluid to drain out.    DESCRIPTION OF DRAWING(S) - The drawing shows composter with flap open.    Door (4)    Strips (5)    Toggles (6)    Drainage holes (7)    Hooks (9)
NOVELTY - The splitter (20) has a tube (26) provided with an inside diameter and coupled at the outlet end (24) to divide flow from another tube (22). The inside diameter of the former tube satisfies the parameters such as true solids density inherent, a Bingham coefficient of rigidity, a Bingham yield stress inherent, an average particle diameter, a predetermined void volume fraction of a fuel material in a fuel mixture, viscosity and gas pressure of carrier gas in the mixture, and wall friction angle between flow direction of the material and axes (A2) of the latter tube.    USE - Flow splitter for use in gasification reactor system (claimed) for dividing flow of a dual-phase fuel mixture i.e. carbonaceous particulate material such as pulverized coal, petcoke and biomass.    ADVANTAGE - The splitter provides a lower predetermined velocity of fluid flow for maintaining uniform flow splitting effect and avoiding plugging effect, thus reducing wear on the flow splitter and other components in the gasifier system, and enabling different reactor vessels to operate under identical operating parameters. The splitter provides uniform division of the flow of the fuel mixture for improving the performance of the gasification reactor system.    DETAILED DESCRIPTION - The carrier gas is nitrogen or carbon dioxide. An INDEPENDENT CLAIM is also included for a method for delivering a fuel mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a flow splitter.    Axes of tube (A2)    Splitter (20)    Tubes (22, 26)    Outlet end of tube (24)    Bracket (27)
NOVELTY - The mixer has an injector main portion that includes a passage extending between the faces, and having a central axis. An impinging passage extends between the two faces and having an associated axis having an angle with the other axis. The impinging passage makes an angle with the central axis of injector main portion satisfying mixing efficiency equation relating mass flow rates of oxidant reactant and fuel material reactant, densities of oxidant reactant and fuel material reactant, and cross-sectional areas of two passages, such that the angle is not equal to 30 degrees .    USE - Injector mixero?=for use ino?=gasification reactor system (claimed) utilizing fuel material such as pulverized coal, petcoke and biomass.    ADVANTAGE - The performance efficiency of the mixer can be improved. The reliability and sensitivity of the mixer can be increased. The cost involved in the manufacture of the mixer can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gasification reactor system;    (2) method of maintaining mixing efficiency between reactants injected through injector mixer; and    (3) method of establishing targeted mixing efficiency between reactants injected through injector mixer.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating relationship between rupe mixing efficiency and mixing efficiency equation.
NOVELTY - The system (10) has a water-electrolysis apparatus (12) which electrolyzes water, and generates oxygen and high-pressure hydrogen. A gas-liquid separator (22) separates moisture content in hydrogen from apparatus (12) via hydrogen piping. A high-pressure hydrogen derived line (24) derives high-pressure hydrogen from gas-liquid separator. A drain line (26) discharges water from gas-liquid separator. A differential pressure type water-electrolysis apparatus (28) electrolyzes water discharged from gas-liquid separator, and generates oxygen and high-pressure hydrogen.    USE - Water-electrolysis system for generating hydrogen used for power generation reaction of fuel cell.    ADVANTAGE - The high-pressure hydrogen is generated by electrolyzing the water introduced from drain line. By providing the second water-electrolysis apparatus to use directly the water discharged from gas-liquid separation apparatus for electrolytic treatment, the amount of hydrogen production with respect to water supply-amount to water-electrolysis system can be increased favorably, and efficient use of water is performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water-electrolysis system. (Drawing includes non-English language text)    Water-electrolysis system (10)    Water-electrolysis apparatus (12)    Gas-liquid separator (22)    High-pressure hydrogen derived line (24)    Drain line (26)    Differential pressure type water-electrolysis apparatus (28)
NOVELTY - Method for culturing microalgae, involves using sterilized nutrient solution containing salt as culture medium, obtained by waste water treatment using activated sludge method using pulse electrolysis method.    USE - The method is useful for culturing microalgae e.g. Chlorella and Botryococcus braunii, which is useful as foodstuff or raw material for producing biofuel.    ADVANTAGE - The method is cost-effective, and prevents decline in culture efficiency as contamination by various microorganism is suppressed as the culture solution is sterilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for algae culture apparatus.
NOVELTY - The apparatus (10) has a cation exchange membrane (12a) and an anion exchange membrane (12b). Electric power feeding portions (22a,22b) clamp the cation exchange membrane. Electric power feeding portions (22c,22d) clamp the anion exchange membrane. An elastic element (26) is located between a mutually opposing electric power feeding portions (22c,22d). A high pressure side separator forms the high-pressure hydrogen chamber to accommodate electric power feeding portions (22b,22c). A low pressure side separator accommodates electric power feeding portions (22a,22b).    USE - Differential pressure type water-electrolysis apparatus used for manufacturing high-pressure hydrogen used as fuel gas for generating fuel battery.    ADVANTAGE - The water supplied to the cation exchange membrane is supplied to anion exchange membrane, and is electrolyzed by the high-pressure hydrogen chamber after permeating the cation exchange membrane, while high-pressure hydrogen is generated. Hence the water can be utilized efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the high-pressure water-electrolysis apparatus. (Drawing includes non-English language text)    Differential pressure type water-electrolysis apparatus (10)    Cation exchange membrane (12a)    Anion exchange membrane (12b)    Electric power feeding portions (22a-22d)    Elastic element (26)
NOVELTY - A cellulase derived from Thermosporothrix hazakensis and having enzymatic activity on at least beta -glucan, soluble cellulose, crystalline cellulose, phosphoric acid swollen cellulose and xylan, is new.    USE - The cellulase is useful in detergent composition, for saccharification of carbohydrate containing raw materials, manufacturing foodstuff or feed and manufacturing ethanol (all claimed) used as fuel, and for synthesizing sugar fatty acid ester.    ADVANTAGE - The cellullase saccharifies carbohydrate containing raw materials efficiently and cost-effectively, has substrate-specificity, has stability with respect to heat processing and transglycosylation activity, and maintains high activity in the presence of organic solvent, ethanol and salt.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide encoding the above-mentioned cellulase;    (2) expression vector comprising the above-mentioned polynucleotide;    (3) transformant transformed by the above-mentioned expression vector;    (4) culture obtained by culturing the above-mentioned transformant;    (5) detergent composition comprising the above-mentioned culture or cellulase;    (6) method for saccharification of carbohydrate containing raw material involves processing carbohydrate containing raw material using the above-mentioned transformant, culture or cellulase;    (7) method for manufacturing foodstuff or feed involves processing carbohydrate containing raw material using the above-mentioned transformant, culture or cellulase; and    (8) method for manufacturing ethanol involves (i) processing carbohydrate containing raw material using the above-mentioned transformant, culture, or cellulase, and (ii) fermenting the processed material.
NOVELTY - Preparation of iloperidone involves: (i) reaction of 4-hydroxy-3-methoxy acetophenone (IV) with 1-bromo-3-chloropropane (V) in the presence of a base and phase transfer catalyst to obtain 1-(4-(3-chloro/bromo propoxy)-3-methoxyphenyl)ethanone (IIIa/IIIb); (ii) reaction of 6-fluoro-3-(piperidine-4-yl)-1,2-benzisooxazole hydrochloride (II) with compound (IIIa) or (IIIb) in the presence of base and phase transfer catalyst in an autoclave; and (iii) isolation of iloperidone.    USE - For preparation of iloperidone (claimed) useful for the treatment of schizophrenia.    ADVANTAGE - The process for preparation of iloperidone, utilizes less toxic and less hazardous solvents such as dimethyl formamide thereby making ecofriendly process.
NOVELTY - The method involves supplying hydrogen gas to a hydrogen separating membrane (12) that is provided with a proton conductivity material. The proton conductivity material is placed in an inner side of fixed space. A proton (H+) is dissociated by the hydrogen separating membrane. The proton is obtained from a raw material. The proton is formed in a surface of a reaction catalyst (14). A carbon duplication combination is removed from the raw material. The reaction catalyst is arranged with a reactant movable part (18). A hydrogen supply part (16) is provided with the hydrogen separating membrane.    USE - Method for producing hydrocarbon for a diesel vehicle.    ADVANTAGE - The method enables reducing high-class biofuel consumption, emission quantity and contaminant of a diesel vehicle. The method enables providing echo-friendly biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for producing hydrocarbon for diesel vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a method for producing hydrocarbon for a diesel vehicle.    Porous scaffold (10)    Hydrogen separating membrane (12)    Reaction catalyst (14)    Hydrogen supply part (16)    Reactant movable part (18)
NOVELTY - A system for the processing at least one biomass source comprises: an anaerobic digester (40) suitable for the digestion of low solid content biomass; at least one thermochemical reactor (10) suitable for the controlled degradation of high solid content biomass; a fractional condenser (20) system suitable to separate fractions produced by the thermochemical reactor; and a transfer system (30, 50) to transport at least one fraction produced in the thermochemical reactor into the anaerobic digester.    USE - As system for the processing at least one biomass source (claimed); and for integrating thermochemical processing of biomass (e.g. lignocellulosic materials) and anaerobic digestion.    ADVANTAGE - The system is efficient and cost effective for processing the light organic materials produced from thermochemical processing. The systems can serve to spur economic development and adoption of alternative fuel technologies. This is especially valuable in rural farm settings and/or in rural bio-oil refineries, where the elimination of waste and opportunities to increase agricultural profits are a prime concern. The system incorporates both thermochemical processing capabilities and anaerobic digestion capabilities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass conversion involving: thermochemical treatment of a high solid biomass to yield a biomass solid and an aqueous fraction comprising oxygenated organic compounds; and anaerobic digestion of a low solid biomass and the aqueous fraction to yield methane.    DESCRIPTION OF DRAWING(S) - The figure shows view of combined thermochemical processing and anaerobic digestion system.    Thermochemical reactor (10)    Fractional condenser (20)    Transfer system (30, 50)    Anaerobic digester (40)
NOVELTY - The system (EE) has a hydrogen producing unit (FF) whose oxygen outlet is connected to an oxygen inlet of a fuel cell unit (HH) via an oxygen pipe. A water outlet of the fuel cell unit is connected to a water inlet of the hydrogen producing unit via a water pipe. A hydrogen outlet of the hydrogen producing unit is connected to a hydrogen inlet of a hydrogen storage unit (GG) via a first hydrogen pipe. A hydrogen outlet of the hydrogen storage unit is connected to a hydrogen inlet of the fuel cell unit via a second hydrogen pipe.    USE - Hydrogen energy-based integrated system for energy storage and energy supply.    ADVANTAGE - The system jointly conducts the three processes of production, storage, and utilization of hydrogen energy, thus allowing the hydrogen, oxygen, and water of the entire system to be recycled for reuse.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hydrogen energy-based integrated system.'(Drawing includes non-English language text)'    Solar energy (AA)    Hydrogen energy-based integrated system (EE)    Hydrogen producing unit (FF)    Hydrogen storage unit (GG)    Fuel cell unit (HH)
NOVELTY - The apparatus (1) has a cylindrical modifier (2) which generates a hydrogen-containing gas by a reforming reaction using a source gas. A carbon monoxide (CO) reducing device (4) reduceses CO in hydrogen-containing gas generated by modifier. A cylindrical hydrodesulfurization device (3) is arranged around modifier and removes a sulfur compound in source gas. A source gas supply channel (331) is configured so as to be heat exchangeable with CO reducing device, and a source gas feed port (341) of hydrodesulfurization device is provided on an end face that is closer to CO reducing device.    USE - Hydrogen generating apparatus used in fuel cell system (claimed).    ADVANTAGE - The hydrodesulfurization device can improve the utilization efficiency and the thermal efficiency of hydrogenation catalyst. The transformer reduces CO in hydrogen-containing-gas by transformation reaction. The selective-oxidation device reduces CO in hydrogen-containing-gas by selective-oxidation reaction.    DETAILED DESCRIPTION - The source gas supply channel through which the source gas is supplied to the hydrodesulfurization device flows. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Cylindrical modifier (2)    Cylindrical hydrodesulfurization device (3)    CO reducing device (4)    Source gas supply channel (331)    Source gas feed port (341)
NOVELTY - The apparatus has two paths (31,32) in which raw material passes through respective desulfurizers (2,3), and is supplied to a modifier (1). A distribution controller selectively enables or prevents distribution of hydrogen-containing-gas generated by modifier, from flowing towards secondary desulfurizer. A controller (12) performs process for switching a switching device (6) to primary path and allows the gas to flow to distribution controller while gas is generated by the modifier, when generation of gas is stopped or started.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The amount of carbon monoxide in the hydrogen-containing-gas generated is reduced. The amount of non-hydrogenated sulfur compound provided on the hydrodesulfurization catalyst of the secondary desulfurizer is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) 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)    Modifier (1)    Desulfurizers (2,3)    Switching device (6)    Controller (12)    Paths (31,32)
NOVELTY - The apparatus has a gas mixture separation unit (CPU) that separates a gas mixture comprising carbon dioxide and another gas in order to produce carbon-dioxide enriched and depleted gases. An air separation unit (ASU) separates air by a cryogenic distillation in order to produce a nitrogen-enriched gas stream (17). A line delivers water to a top of a water cooling tower. A cooled water pipeline (15) is connected with an air-cooling unit (1) that cools the air upstream to the air separation unit. The pipeline is connected to an inlet and/or to an outlet of the gas mixture separation unit.    USE - Integrated apparatus for separation of a mixture of carbon dioxide and another gas e.g. nitrogen, oxygen, argon, hydrogen, carbon monoxide, methane and nitrogen dioxide, and for separation of air by a cryogenic distillation in a gas turbine (all claimed).    ADVANTAGE - The cooled water pipeline is connected with the air-cooling unit that cools the air upstream to the air separation unit, and to the inlet and/or to the outlet of the gas mixture separation unit, thus enabling simple and cost-effective separation of the air and the mixture of carbon dioxide and the other gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an integrated method for separation of a mixture of carbon dioxide and another gas and for separation of air by a cryogenic distillation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an integrated apparatus for separation of a mixture of carbon dioxide and another gas and for separation of air by a cryogenic distillation.    Air separation unit (ASU)    Gas mixture separation unit (CPU)    Air-cooling unit (1)    Cooled water pipeline (15)    Nitrogen-enriched gas stream (17)
NOVELTY - The equipment has a quantity increase unit that increases the amount of water sprinkling which corresponds to a carrier filled layer (10a). A control unit (60) detects the differential pressure at preset timing which is below the preset standard pressure, when the water sprinkling is performed at the carrier filled layer based on the water sprinkling algorithm. The water sprinkling is performed to the specified carrier filled layer, when predetermined quantity increase is carried out by sending signal to the quantity increase unit corresponding to specified carrier filled layer.    USE - Equipment for treating to-be-processed gas e.g. biogas, odor gas and volatile organic compound (VOC) gas (all claimed) emitted from anaerobic digestion treatment of organic waste water such as sewage and industrial waste water, kitchen and waste material dump place of restaurant.    ADVANTAGE - Since the water is sprinkled to the carrier filled layer, the pressure loss at the time of passing biogas and odor gas to carrier filled layer can be reduced. The treating efficiency, operability, reliability and usability of the gas treatment equipment can be improved.    DETAILED DESCRIPTION - The carrier filled layer is filled with a carrier which is adhered to the microorganisms in which the inside of a bioreaction tower (1) is segmented into several division areas by a separation wall (2). A comparison unit compares the predetermined standard pressure value, to compute differential pressure by subtracting the exit side pressure from the entrance-side pressure. An INDEPENDENT CLAIM is included for operating method of gas treatment equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view illustrating the operation of gas treatment equipment. (Drawing includes non-English language text)    Bioreaction tower (1)    Separation wall (2)    Carrier filled layers (10a-10f)    Nozzles (50a-50f)    Control unit (60)
NOVELTY - Producing (M1) an engineered fuel feed stock from a processed municipal solid waste (MSW) stream involves combining a waste stream and an additive; compressing to form a densified intermediate material; grinding the intermediate material; mixing the ground intermediate material with a second waste stream; and compressing the intermediate material and the second waste stream.    USE - For producing engineered fuel feed stock from processed municipal solid waste (MSW) stream (claimed).    ADVANTAGE - The engineered fuel feed stock burns efficiently and cleanly and can be used for the production of energy and/or chemicals. The systems and methods provide sorting waste material and reclaiming a resource value from components of the waste material. By harnessing and using the energy content contained in waste, the method reduces green house gas emissions and/or emissions generated during the processing of wastes, thus effectively uses the waste generated by commercial and residential consumers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for producing an engineered fuel feed stock involving processing MSW to remove non-combustible waste; sorting the processed waste stream based on density into a first material of a first density classification having a bulk density greater than 15 lb/ft3, a second material of a second density classification having bulk density 4-15 lb/ft3, and a third material of a third density classification having bulk density less than 4 lb/ft3; and combining first material, second material, third material and additive in predetermined proportions to form an engineered fuel feed stock.
NOVELTY - The method involves judging a freezing air-conditioning machine to be abnormal when a specific compound produced by disassembly of a hydrochlorofluorocarbon (HFC) type refrigerant is detected inside the refrigerant of the freezing air-conditioning machine. The specific compound is determined from a result of a refrigerant disassembly test done by sealing only the refrigerant hermetically in a heating container, and the result of the refrigerant disassembly test done by sealing the refrigerant and air hermetically in the heating container.    USE - Method for diagnosing abnormality of a freezing airconditioning machine. Can also be used for judging age-deterioration of refrigerant and refrigeration oil of a freezing air-conditioning machine, and presence or absence of sludge generation in a refrigerant circuit of the machine.    ADVANTAGE - The freezing air-conditioning machine to be abnormal or not is judged before generation of a halogen ion by easily analyzing the refrigerant extracted from the machine without dismantling the machine.    DETAILED DESCRIPTION - The refrigerant is selected from one among HFC410A refrigerant, HFC407C refrigerant or HFC32 refrigerant. An INDEPENDENT CLAIM is also included for a defect cause estimation method for a freezing air-conditioning machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating a relationship between a refrigerant degradation product and deterioration of refrigeration oil.'(Drawing includes non-English language text)'
NOVELTY - Livestock farm wastewater is recycled by separating livestock farm wastewater into solid and liquid, culturing microalgae by liquid, adding flocculant (14) which has radiation-crosslinked body of gamma -polyglutamic acid or gamma -polyglutamic acid salt as main component to microalgae growth liquid while purifying liquid, aggregating microalgae, adding carbohydrate (12) and lactic acid bacteria (11) to mixture of wet microalgae and liquid, performing lactic acid fermentation, and supplying resulting mixture to livestock as feed.    USE - Recycling method of livestock farm wastewater (claimed).    ADVANTAGE - Livestock farm wastewater can be purified and recycled, and spread of different microorganisms in a pig pen can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining the recycling method of livestock farm wastewater.    Supernatant (10)    Lactic acid bacteria (11)    Carbohydrate (12)    Water (13)    Flocculant (14)
NOVELTY - The apparatus (100) has modifier (10) that generates hydrogen-containing-gas using raw material (AA) and water vapor. A hydro-desulfurization device (13) is provided downstream of most downstream valve (11) of material flow path (21), and removes a sulfur compound in raw material. A sealing device (15) blocks communication between modifier and atmosphere. A pressure relief device (16) connects the hydro desulfurization device and modifier, and releases the pressure of modifier that rises after sealing device is closed into atmosphere.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The discharging of the hydrogen sulfide which remains in the hydro desulfurization device to the exterior of the apparatus can be effectively suppressed. The malfunction occurred in the pressure-relief operation of the pressure-relief device can be reduced. Thus the maintenance cost of the apparatus can be greatly reduced and the service life of the apparatus can be prolonged.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (10)    Valve (11)    Hydro desulfurization device (13)    Sealing device (15)    Pressure-relief device (16)    Material flow path (21)    Hydrogen generating apparatus (100)    Raw material (AA)
NOVELTY - Extraction of squalene (I) without using organic solvent comprises (a) preparing a biomass of microalgae belonging to the family of Thraustochytriales species in order to reduce the concentration of soluble interstitial to obtain a purity of greater than 95%; (b) treating the obtained biomass with an enzyme such as alcalase to break the cell wall of the microalgae to prevent the formation of the emulsion produced by the enzymatic treatment; (c) centrifuging the reaction mixture to separate oil phase from the aqueous phase; and (d) extracting crude oil enriched with squalene.    USE - (I) is useful as an intermediate product for the biosynthesis of cholesterol. (I) is useful as antioxidant, antistatic and emollient in cosmetic fields, and as additive with vaccines.    ADVANTAGE - (I) is nontoxic and does not cause any irritation to the human skin. (I) exhibits high purity.
NOVELTY - Amphiphilic copolymer comprising at least two keto-amine structural units (I) and (II), excluding keto-amine diblock copolymers (III), where (I) is hydrophilic, and (II) exhibits more hydrophobicity than (I), is new.    USE - The amphiphilic copolymer is useful as non-ionic soaps, emulsifiers, membrane structures, defoamers, viscosity reducers and auxiliaries for pharmaceutical formulations, pesticides and detergents (claimed).    ADVANTAGE - The amphiphilic copolymer is completely biodegradable and non-toxic, and does not release environmentally harmful degradation products.    DETAILED DESCRIPTION - Amphiphilic copolymer comprising at least two keto-amine structural units of formula (-(C(=O)-CH(R2)-N(R1))n-) (I) and (-(C(=O)-CH2-N(R3))m-) (II), excluding keto-amine diblock copolymers of formula (X-((C(=O)-CH(R2)-N(R11))n1-(C(=O)-CH2-N(R13))m1)blk-Y1) (III), where (I) is hydrophilic, and (II) exhibits more hydrophobicity than (I), is new.    R1 = CH3 or ethyl;    R2 = CH3 or H;    R3 = 2-21C alkyl (optionally branched or cyclic), or aryl;    n, m = greater than 1;    n1 = 30-70;    m1 = 10-40;    R11 = CH3;    R13 = n-butyl;    X = n-butylamine; and    Y1 = H.
NOVELTY - Glass fiber reinforced plastic biomass pool comprises an upper tank body and a lower tank body. The upper tank body and the lower tank body is semi-spherical structure of glass steel. The upper tank body is connected with a feeding hopper through a feeding pipe. The upper part in the tank body is connected with an air outlet pipe. The air outlet pipe is provided with a valve. The lower tank body is connected with a discharging pipe.    USE - Used as a glass fiber reinforced plastic biomass pool.    ADVANTAGE - The reinforced plastic biomass pool: has resistance to corrosion, aging and water, prolonged service life, and has good air tightness on the surface; does not leak air feeding pipe set on the tank body; is convenient for feeding; and comprises a discharging pipe set on the lower tank body which prevents the leakage of upper half part of slag.
NOVELTY - The reaction chamber has a main portion that is provided with a transverse air outlet port. A vertical baffle plate is arranged on the main portion. Several through-holes are formed in the baffle plate. A main chamber is formed in the main portion. The main chamber is connected with the main portion. The front end of main chamber is provided with an outlet port.    USE - Reaction chamber used for generating hydrogen and methane.    ADVANTAGE - The production capacity of hydrogen and methane can be improved effectively.
NOVELTY - An automatic control device comprises a methane generator, a solar heater and an operation controller. The methane generator is provided with a feeding port at the lower part of the tank body and is connected with a disperser at the upper part of the tank. The bottom of the device is provided with a mud discharging port of the collector. A heating coil is provided in the tank. The inlet and the outlet of the heating coil are connected to inlet and outlet of solar heater by the tank. The tank is provided with a methane outlet.    USE - Automatic control device for solar energy heating to produce methane.    ADVANTAGE - The device realizes greatest degree of utilization of effective resources, so it has a practical significance for low-carbon life of conservation-oriented society.
NOVELTY - Sunlight warming insulation biogas pit comprises tank unit, insulation pit bag which is provided in the interlayer structure of the pit tank unit which is filled with heat preservation material layer, a liner seal cellar bag which is provided in the insulation pit bag, a warming glass top cover which is provided on the pit tank unit, and a stirring device which is provided with the pit tank unit by warming glass top cover.    USE - As sunlight warming insulation biogas pits.    ADVANTAGE - The pit is cost-effective and allows rapid fermentation and increases quality of fertilizer.
NOVELTY - Insecticidal composition comprises an active ingredient A comprising cyflumetofen and an active ingredient B comprising spirodiclofen, fenpyroximate and/or bromopropylate, where the weight ratio of the active ingredient A and B is 1:80-80-1.    USE - The insecticidal composition is useful in preventing and treating various insects (e.g. Panonychus ulmi, Phyllocoptruta oleivora, wheat leaf Panonychus, yellow spider, red leaf Panonychus, Polyphagotarsonemus latus, Tetranychus cinnabarinus, Tetranychus urticae, Tetranychidae, stars cream and Aceria litchi Keifer) on the wheat, cotton, fruit tree, vegetable, tea tree and ornamental flower (claimed).    ADVANTAGE - The composition has good synergistic effect; reduces the dosage of the pesticide; and is safe to the human and the livestock, which is free of phytotoxicity; is environmental friendly; has strong adhesiveness; and is resistant to rain erosion.
NOVELTY - The system has oxygen distribution pipes which distribute oxygen in an oxygen supply pipe to the food waste. An oxygen tank for supplying oxygen is connected to the oxygen distribution pipe. The air supply from an air supply unit is controlled when oxygen content is below standard value. An air feeder is provided to supply air to the food waste. The food waste and quicklime loaded in a microorganism ferment tank are mixed using a mixer.    USE - Food waste disposal system.    ADVANTAGE - The food waste can be disposed easily and generation of bad smell during fermented process can be reduced. The system is environment-friendly.
NOVELTY - The apparatus has inlet port (10) through which sewage and sludge are passed into an inflow pump (20). An influx unit (41) is connected to a heater (30) which is provided to heat the sludge and sewage. An exhausting unit (42) is provided to eject washing acid from a washing acid fermenter (40) to the sewage and sludge. A circulation pump (50) is connected to overflow structure (43) of washing acid fermenter. A waste sludge vent (60) discharges the waste sludge and sewage processed in washing acid fermenter to outside.    USE - Processing apparatus of sludge and sewage from sewage disposal plant.    ADVANTAGE - By using washing fermentation process, the sludge and sewage can be processed easily with simple process. The cost of the processing apparatus is reduced and installation space of the apparatus is reduced. The production of volatile fatty acid is optimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of sludge and sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing apparatus of sludge and sewage. (Drawing includes non-English language text)    Inlet port (10)    Inflow pump (20)    Heater (30)    Washing acid fermenter (40)    Influx unit (41)    Exhausting unit (42)    Overflow structure (43)    Circulation pump (50)    Waste sludge vent (60)
NOVELTY - The device has water outlet pipe that is connected with the water pump. A biomass interception ball is provided through the circulating liquid. A circulating pump is connected with the methane bubble-free aeration membrane component which is connected with the exhaust pipe. The exhaust pipe is connected with the liquid sealing device. A filling material is supported by a bracket. The membrane component is provided with a hollow fiber membrane and bubble-free aeration membrane component. The membrane component is provided with a water inlet pipe and the water pump.    USE - Device for oxidizing enrichment of bacteria.    ADVANTAGE - The methane in the water phase of the dissolution rate can be improved by improving the operation efficiency of the reactor.
NOVELTY - The bed has left end, middle part and right end of rotating bed which are respectively connected with left shaft, middle ring and right shaft to construct a horizontal cylindrical barrel main body ferment mechanism. Fermentation plow is provided on inner wall of the rotating bed. The rotating bed is provided with transmission gear on outer wall of left end. A motor, a speed reducer and a transmission gear are connected with each other in turn. Right end of the revolving bed is provided with feeding port. Discharge switch and discharge port are arranged below the left end of the rotating bed.    USE - A solid organic fertilizer rotary biological fermentation bed.    ADVANTAGE - The bed makes fermenting mixed straw materials fully fermented in the process of fermentation, which improves production efficiency. It has continuous process, is automatic, and is suitable for producing and processing all kinds of solid organic fertilizer. The product quality is stable.
NOVELTY - A fertilizer preparing device and oxygen supply and heat collecting insulation system comprises a cyclone dust remover, a biological deodorizing device, a sludge fermentation cylinder frequency conversion rotary motor, and a solar fermentation tent. A central controller signal receiving end wirelessly receives monitoring data of temperature sensing probe and an oxygen concentration sensing probe. The central controller controls signal output end to be connected with air inlet electric valve, variable frequency drive motor, discharging electric valve, oxygen supply fan and sludge cylinder.    USE - A totally-enclosed sludge cylinder fertilizer preparing device and deodorization oxygen supply and heat-collecting insulation system.    ADVANTAGE - The system decreases sludge, odor and dust pollution in the process of fermenting the compost, improves the working efficiency, and has good practicability and market popularization value.
NOVELTY - Preserving water-chestnut slag, comprises adding 0.01-0.05 wt.% of microorganism fermentation preservative into water-chestnut slag with water content of 55-70%, where each ton of the water-chestnut slag is added with 100-500 g of the preservative, uniformly mixing the mixture and then sealing to preserve, where the water-chestnut slag comprises leftovers of chestnuts, such as processed water-chestnut peel and water-chestnut, and the preservative is a mixture of bacteria and main active ingredients comprising Lactobacillus plantarum, Bacillus subtilis or yeast.    USE - The method is useful for preserving water-chestnut slag.    ADVANTAGE - The method preserves the water-chestnut slag with reduced energy consumption in a simple, cost-effective and environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water-chestnut slag culture medium comprising 25-40 parts by weight (pbw) of water-chestnut slag, 13-18 pbw of sawdust, 8-12 pbw of corn cob, 8-12 pbw of wheat bran, 25-38 pbw of cottonseed, 1-2 pbw of lime and 1-2 pbw of gypsum.
NOVELTY - The device has a gasification melting furnace whose bottom is formed with a slag discharging opening and top is provided with a gas guide outlet. A melt combustion chamber, a gasification chamber, a drying chamber and a gas positive pressure cabin are arranged in turn from bottom to top of the gasification melting furnace. A slag bin is arranged between a plasma torch and the melt combustion chamber and connected with an opening upper part of the drying chamber. The gasification chamber is provided with an air inlet. The gas negative pressure cabin is provided with a thermoelectric couple.    USE - Household rubbish and incineration fly ash co-processing device.    ADVANTAGE - The device can completely break domestic rubbish, burn the toxic and harmful waste in mixture, melt the generated synthesized gas to generate electricity for an internal combustion engine, and realize continuous feeding and discharging material. The device has simple and reliable structure and better economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a household rubbish and incineration fly ash co-processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a household rubbish and incineration fly ash co-processing device.
NOVELTY - Obtaining lipase involves selecting industrial waste from Jatropha cake, castor, babassu meal, soybean cake and then processing the selected materials in presence of filamentous fungi selected from Aspergillus, Penicillium simplicissimum, Rhizopus or Trichoderma by solid state fermentation. Molasses, glycerin and vegetable oils are also provided for processing the selected materials.    USE - Method for obtaining lipase used as biocatalyst for obtaining biodiesel (Claimed).    ADVANTAGE - The method enables to obtain lipase and reduces the toxicity of agro-industrial waste, which is applied as fertilizer or feed for animal.
NOVELTY - Method for preparing biofuel using microalgae, involves separating hydrogen from gasoline.    USE - The method is useful for preparing biofuel using microalgae.
NOVELTY - Organic fertilizer comprises (in parts by wt.) dry cow dung as main material (200-250), humic acid powder (10-15), clay (20-25) and microorganism strains (certain amount), where the organic content is greater than or equal to 45 %, the humic acid content is greater than or equal to 35 %, and the moisture content is less than or equal to 20 %. The organic fertilizer is prepared by mixing and granulating the above materials.    USE - Used as an organic fertilizer.    ADVANTAGE - The organic fertilizer is rich in beneficial microorganism content and convenient to use, does not destroy the available nutrients, and has high fertilizing efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising: (i) anaerobic fermenting the wet cow dung in a sealed state; (ii) drying the fermented and decomposed cow dung by naturally dehydrating or mechanically dehydrating to obtain the dry cow dung, where the moisture content of the dry cow dung is less than 20 %; (iii) mixing the obtained dry cow dung, humic acid and microorganism, completely stirring, adding clay into water to prepare the mud, spraying on the mixed material, uniformly mixing, and drying until the moisture content is less than 20 %; (iv) conveying the mixed material to a granulator, granulating, and molding to obtain the organic fertilizer primary product; (v) conveying the organic fertilizer primary product to a polisher, and polishing; (vi) drying the polished granules at 150-250 degrees C for 18-22 minutes; (vii) sieving the dried granules; and (viii) measuring the dried organic fertilizer, and packaging into qualified product.
NOVELTY - The device has a photo-catalytic oxidization device (104) that is connected with the depositing device (108). The depositing device comprises a water tank and a channel that are connected with the water tank (110). The agent storage chamber is stored with an alkaline agent. The depositing device is connected with the pH value adjusting device (114). The pH value adjusting device comprises water tank and the channel that are connected with storage chamber (116) stored with acid.    USE - Sewage processing device.    ADVANTAGE - The environment pollution can be avoided efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage processing device.    Photo-catalytic oxidization device (104)    Depositing device (108)    Water tank (110)    PH value adjusting device (114)    Storage chamber (116)
NOVELTY - The device has a bag-type dust removing unit provided with multiple spray nozzles, a water ring compressor, a steam-water separator, a gas storage cylinder and an equipment control system. A gasification furnace is provided with a plasma torch and a fluidized bed top smoke outlet, where core temperature of the plasma torch is more than 300 degrees Celsius. A slag discharging system is fixed at a tail part of an ash plasma processing chamber. An absorption tower i.e. active carbon device, sprays active carbon powder.    USE - Fluidized-bed plasma gasification rubbish processing device.    ADVANTAGE - The device is environment-friendly, and saves energy and consumes less power.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fluidized-bed plasma gasification rubbish processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fluidized-bed plasma gasification rubbish processing device.
NOVELTY - A desulfurizing agent comprises an activated charcoal support of three-dimensional structure having a large specific surface area and including fine pores on its surface and inside, and an aluminosilicate layer which is uniformly permeated on and into surface of the activated charcoal support, as a surface layer. The aluminosilicate layer has thickness of 1-10 mu m.    USE - Desulfurizing agent is used for hydrogen generator for fuel cell.    ADVANTAGE - Since the specific surface area of the activated charcoal support is increased, the active site of sulfur compound in the fuel cell reforming process is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of desulfurizing agent, which involves preparing activated charcoal support, preparing aluminosilicate precursor solution, coating the aluminosilicate precursor solution on the surface of activated charcoal support, heating and drying.
NOVELTY - Irradiation reactor comprises a nozzle (2) and an irradiation container (4), where the irradiation container is set below the scanning window of an electron accelerator. The lower part of the irradiation container is provided with a discharge port (5). The nozzle is set on the irradiation container on the side wall of the waste water (1) sprayed out by the nozzle.    USE - The irradiation reactor is useful for treating industrial waste water by electronic accelerator.    ADVANTAGE - The reactor has simple structure, consumes less energy and is easy to control; maintains uniform dosage and is matched with all types of electron accelerator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating the waste water by the irradiation reactor comprising, (i) spraying waste water through the nozzle to form a parabolic water film (3); and (ii) irradiating the water film through an electron beam by scanning window and discharging through the discharge port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the irradiation reactor for treating industrial waste water by electronic accelerator.    Waste water (1)    Nozzle (2)    Parabolic water film (3)    Irradiation container (4)    Discharge port (5)
NOVELTY - Production of biodiesel comprises refining biomass oil using a process of filtering, hydrating and degumming, absorbing and decolorizing, and dewaxing via solvent method; adding the refined biomass oil and low-carbon alcohol into a catalysis rectifying tower which uses strong acid cation exchange resin loaded with aluminum chloride as a catalyst bed layer and uses kieselguhr as inertia layer of the catalyst bed layer; performing catalysis ester exchange reaction under normal pressure for 2-3.5 hours to obtain aliphatic ester; and adding the aliphatic ester into an evaporator.    USE - A production method of biodiesel.    ADVANTAGE - The method has simple process route. The product and the catalyst are separated easily. The catalyst can be used repeatedly, thus saving cost for catalyst usage. Large amount of polluted water is not generated, thus avoiding environment pollution.    DETAILED DESCRIPTION - Production of biodiesel comprises:    (A) refining biomass oil physically and chemically using a process of filtering, hydrating and degumming, absorbing and decolorizing, and dewaxing via solvent method to refine the biomass oil as colorless, odorless and transparent mixture of triglyceride fatty acid;    (B) producing aliphatic ester with different carbon chain lengths by adding the refined biomass oil and low-carbon alcohol into a catalysis rectifying tower in a feeding mole ratio of 1-6:1, in which the catalysis rectifying tower uses strong acid cation exchange resin loaded with aluminum chloride (AlCl3) as a catalyst bed layer and uses kieselguhr as inertia layer of the catalyst bed layer, the reaction temperature of the refined biomass oil and low-carbon alcohol is at 50-120 degrees C; and    (C) performing catalysis ester exchange reaction under normal pressure for 2-3.5 hours to obtain aliphatic ester; and adding the aliphatic ester into an evaporator to decompress, distill, separate and purify.
NOVELTY - Blended fuel comprises 0# diesel oil (50-84.5 vol.%), ethyl levulinate (5-20 vol.%), biodiesel (10-25 vol.%), and cosolvent (0.5-5 vol.%).    USE - Used as a blended fuel.    ADVANTAGE - The blended fuel has good physical and chemical properties, and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing blended fuel, comprising taking and mixing the ethyl levulinate, biodiesel and the cosolvent to prepare mixed liquor, and putting the mixed liquor into 0# diesel oil, mixing well under the condition of stirring to obtain the blended fuel.
NOVELTY - A biomass derivative fuel is prepared by after removing impurities in a raw material, crushing the raw material to 30-135 mm, stirring and mixing; drying the raw material until the moisture content is 10-25%; mixing dried raw material, waste liquid in a sugarcane factory, and a sulfur-fixing agent at a weight ratio of 90-70:5-25:5; and pressing and forming the mixture into a forming machine, and drying at 50-150 degrees C for 0.5-2 hours.    USE - Method for preparing a biomass derivative fuel.    ADVANTAGE - The method has refined technology, easy operation, wide raw material source, low cost, and environmental friendliness. The combustion cannot corrode the acid and base, and the maintenance cost of the device is reduced. The utilization rate of crop solid wastes is improved, and the fuel has good stability and high heat value.
NOVELTY - An aquatic biomass i.e. duckweed processing method involves homogenizing biomass in water, followed by centrifuging, filtering and/or performing hydro-cyclone on homogenized product to obtain supernatant-I containing proteins, carbohydrates and/or dyes and solid fraction-I containing cellulose.    USE - Method for processing aquatic biomass i.e. duckweed that is utilized for manufacturing industrial raw materials and food products.
NOVELTY - Pollution free simultaneous preparation of nano silicon dioxide, potassium fulvate, and fuel ethanol by using sugar cane, comprises utilizing a device comprising sugarcane squeezer, a bioreactor, a distillation device, a molecular sieve, a catalytic converter and a condensation device, silicon dioxide separation device, potassium fulvate purifying device and nano silicon dioxide purification device.    USE - The method is useful for pollution free simultaneous preparation of nano silicon dioxide, potassium fulvate, and fuel ethanol by using sugar cane.    ADVANTAGE - The method: is ecofriendly in comparison with the conventional methods which utilizes non-renewable minerals to extract nano-silica, utilizes low quality coal and potassium hydroxide for producing potassium fulvic acid, and utilizes oil raw material for preparing fuel ethanol; completely utilizes the raw material; and consumes less energy with low carbon emission.
NOVELTY - Passivator prepared by crushing medium low-grade rock phosphate containing 20-30% of phosphorus pentoxide, (b) sieving the rock phosphate into a 100 meshes to obtain powdered rock phosphate according to solid and liquid ratio of 1:1-1:20, (c) mixing the powdered rock phosphate with 0.1-0.7 mole/l of oxalic acid, (d) activating the mixture at 28 degrees C for 6 days and (e) drying the mixture at 50 degrees C for 20-24 hours, is claimed.    USE - The passivator is useful for treating soil polluted by heavy metal, such as copper, lead and cadmium (claimed).    ADVANTAGE - The passivator is cost-effective and free of secondary pollution, and treats polluted soil without damaging physicochemical property of the soil in less-time consuming manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of passivator in in-situ treatment of soil heavy metal copper, lead and cadmium pollution, where the in-situ treatment comprises applying the prepared passivator or into soil polluted by heavy metal according to a use level of 3.97 g/kg, harvesting lettuces after planting for 120 days and sampling the lettuces for measuring absorptive amount of heavy metal by the plant.
NOVELTY - Liquid mulching film comprises 20-30 wt.% of methyl silicate, 1-5 wt.% of strong alkali and balance amount of water.    USE - The liquid mulching film is useful for grapes planting application in drought and semi-drought and high salt alkali areas.    ADVANTAGE - The liquid mulching film is simple to operate, cost-effective and environment friendly, saves water consumption, and improves grapes yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the liquid mulching film comprising: (a) adding the methyl silicate, the strong alkali and the water into an agitating kettle; (b) agitating till the strong alkali is completely dissolved and (c) adding the colorizing agent.
NOVELTY - Fusarium sp. TG-9 having a conservation number of CGMCC No.5528, is new.    USE - The Fusarium sp. TG-9 is useful for preparing podophyllotoxin (claimed).    ADVANTAGE - The Fusarium sp. TG-9 is capable of simply, rapidly and economically preparing the podophyllotoxin with high productivity and strong operability in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing podophyllotoxin comprising fermenting the Fusarium sp. TG-9 with a conservation number of CGMCC No.5528 at rotating speed of 100-150 (preferably 120) revolution per minute, rotating radius of 2 cm and a temperature of 26-30 (preferably 28) degrees C for 5-9 (preferably 7) days, collecting the fermentation product, filtering the fermentation product and then collecting filtrate, adding chloroform into the filtrate, where a volume ratio of the filtrate to the chloroform is 1:1, and collecting an organic phase to obtain the podophyllotoxin.
NOVELTY - A high-purity saligenin is prepared by taking willow bark or willow branch as raw material, and extracting by water or alcohol solution, filtering extract, absorbing and separating filtrate by resin1, decoloring, and crystallizing. Filtering of extract is carried out by ultrafiltration. Extract firstly passes through ultrafiltration film of 100-500 kD, and ultra-filtration film of 5-10 kD. Average membrane flux is respectively controlled to 100-190 liters/m2-hour (LMH) and 20-24 LMH.    USE - Method for preparation of high-purity saligenin (claimed).    ADVANTAGE - Content of saligenin is 99.0%. The method has high yield and low cost, and is easy to realize industrialization. Water and less alcohol in production can be recycled to reduce cost and pollution of organic solvent on environment.
NOVELTY - Preparation of high-purity capecitabine comprises separating impurities in capecitabine crude product using organic solvent and water.    USE - Preparation of high-purity capecitabine (claimed).    ADVANTAGE - The method has low cost, high yield, and no three-waste pollution; and is suitable for mass industrial production. It provides high-purity capecitabine with total impurity content of lower than 0.5% and single impurity content of lower than 0.1%.
NOVELTY - Waste gypsum and food waste are dried and pulverized to obtain a crushed material. 100-Mesh crushed materials of waste coal, red clay, barley stone, zeolite, germanium stone, and feldspar are prepared by pulverization. The crushed material of red clay, barley stone, zeolite, germanium stone, and feldspar are all mixed in the same amount. Crushed waste gypsum, crushed waste coal, crushed food waste, waste oil, and the crushed-material mixture are mixed. The obtained mixture and water are kneaded, molded into pellets, and dried to obtain solid type fuel.    USE - Manufacture of solid type fuel (claimed).    DETAILED DESCRIPTION - Waste gypsum and food waste are dehydrated and dried in a dehydrator and dryer to a water content of 30-50% and pulverized separately to obtain a crushed material of 100 mesh. 100-Mesh crushed materials of waste coal, red clay, barley stone, zeolite, germanium stone, and feldspar are prepared by pulverization. The crushed material of red clay, barley stone, zeolite, germanium stone, and feldspar are all mixed in the same amount. (In wt.%) crushed waste gypsum (40-60), crushed waste coal (5-25), crushed food waste (10-40), waste oil (2-10), and the crushed-material mixture (2-6) are mixed well. The obtained mixture (90-95) and water (5-10) are kneaded, molded into pellets, and dried to obtain solid type fuel.
NOVELTY - Stock effluent treatment system, comprises first filter, first storage tank, second filter, second storage tank, and third filter, where the above-mentioned respective tanks are provided with stirrers, and stock effluent is sequentially passed through the above-mentioned components.    USE - As stock effluent treatment system.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is included for a method of treating stock effluent.
NOVELTY - The method involves mixing the brine into buffer tank according to predefined proportion. The fresh brine solution is introduced into mining area (4) by high output halogen-free channel. The solution for dissolving ore is prepared. The length of channel is set to 39 km and width of channel is set to 8-12 m according to the low-grade solid potassium chloride ore. The dissolved brine potassium chloride more than 1.2% is conveyed to the raw ore by introducing channel according to mine selecting requirement. The ore is dried for preparing qualified fertilizer product.    USE - Method for dissolving low-grade solid potassium chloride ore obtained from mining area and salt lake, for use in manufacturing of fertilizer product.    ADVANTAGE - The repeated utilization rate of water is improved so that the water can be conserved effectively. The service life of mine is improved. The discharging of waste water is avoided so that the environment is protected.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process for dissolving low-grade solid potassium chloride ore. (Drawing includes non-English language text)    Fresh water river channel (1)    Halogen channel (2)    Halogen-free gate (3)    Mining area (4)
NOVELTY - Sustained-release safe sheet for preventing or treating fish disease, obtained by placing and drying a raw material liquid on a specific shape of sheet, where the raw material liquid comprises dissolved olibanum solution, natural medicine mixture containing active ingredients containing hot-water extraction of Terminalia chebula and Rhus japonica, distilled water, zeolite and gelatin.    USE - The sustained-release safe sheet is useful for preventing or treating fish disease.    ADVANTAGE - The sustained-release safe sheet is environmentally-friendly, as it improves tolerance to release of an antibiotic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the sustained-release safe sheet, which involves dissolving an amount of olibanum using distilled water, adding gelatin to the mixture, extracting natural medicines separately at 120 degrees C for 6-10 hours using hot water extraction, injecting fiber into the mixture, injecting zeolite into extract, and drying the mixture and preparing into sheet form.
NOVELTY - A special DYD (not defined) catalyst for producing biodiesel by a one-step process, composed of multicomponent solid super acid and mixed solid base, is new.    USE - As special DYD catalyst for producing biodiesel by one-step process (claimed).    ADVANTAGE - The DYD catalyst produces biodiesel in one-step process using waste animal and plant oil, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the special DYD catalyst for producing biodiesel by a one-step process involving: (1) dissolving salt which is converted into metal mol ratio of iron to aluminum to zinc of 2:1:1 into water, neutralizing the salt by ammonia water with mass.% of 20% until the pH value is 4-5, filtering, washing the filter residue for obtaining a filter cake of hydroxides of iron, aluminum and zinc, immersing the filter cake by concentrated sulfuric acid for 1 hours at room temperature, then filtering the filter cake and drying, roasting the filter cake at 500-600 degrees C until the activity reaches more than 95% and no sulfate radical is detected by a barium chloride solution with mass.% of 10%, when the index is qualified, diluting by swill-cooked dirty oil, grinding the filter cake for obtaining a cake-shaped substance with mass.% of super acid of 68%, to obtain multi-component super acid catalyst, where the salt of iron, aluminum and zinc is sulfate or chloride; (2) preparing a metal oxide mixture or a hydroxide mixture from oxides or hydroxides converted into metal mol ratio of calcium to magnesium to aluminum of 2:2:1, roasting the mixture at 800-900 degrees C until the activity is more than 95%, when the mixture is qualified, diluting by swill-cooked dirty oil, grinding into a cake-shaped substance with mass.% of solid base of 68%, to obtain mixed solid base catalyst; and (3) mixing the multi-component solid super acid catalyst with the mixed solid base catalyst, grinding for preparing the DYD catalyst.
NOVELTY - The structure has a positive electrode and a negative electrode, where one of the positive and negative electrodes is covered with an insulating medium and directly in contact with a contact point. Two ends of an electrode unit are not directly suspended to a circuit. The electrodes are positioned in parallel to each other. The electrodes are made from stainless steel, copper, graphite material or tungsten material. The insulating medium is PTFE.    USE - Discharging electrode structure for a plasma air purifying device.    ADVANTAGE - The structure can generate a large amount of low temperature plasma with glow type plasma properties at electrode crossing point, so that power consumption can be reduced, thus ensuring better gas permeability by increasing the actual plasma action region while improving sterilizing rate of plasma.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a discharging electrode structure.
NOVELTY - Use of 2-glycosylquinoline compound (I) for preparing anti-acetylcholinesterase medicines is claimed.    USE - (I) is useful for preparing anti-acetylcholinesterase medicine (claimed).    ADVANTAGE - (I) is strongly soluble in water; and has high bioavailability, and strong inhibiting activity for acetylcholinesterase. The preparation of (I) is simple, and economical; produces less environmental pollution; and is suitable for industrial production.    DETAILED DESCRIPTION - Use of 2-glycosylquinoline compound of formula (I) for preparing anti-acetylcholinesterase medicines is claimed.    R1-R4 = -H, -OCH3 or -Br.    An INDEPENDENT CLAIM is also included for preparing (I), comprising (i) reacting D-glucose and acetylacetone in the presence of sodium bicarbonate to obtain beta -D-acetonyl glycoside; and (ii) dissolving o-amino benzaldehyde or substituted o-amino benzaldehyde and beta -D-acetonyl glycoside in methanol, and reacting in the presence of pyrrolidine to obtain compound (I).
NOVELTY - A carrier gas is purified and injected at 25-195 ml/minute and 10-40 degrees C, into a gas chromatographic column with a to-be-detected sample, adsorbed and desorbed at 20-250 degrees C, nitrous oxide, carbon monoxide, methane and carbon dioxide in the sample supplied into an electron capture detector, a methanator and a hydrogen flame ionization detector are detected at 90-350 degrees C. Data from both electron capture detector and hydrogen flame ionization detector are synchronously input to a chromatography workstation of gas chromatograph, and chromatogram analysis result is obtained.    USE - Gas chromatographic method for analyzing nitrous oxide, carbon monoxide, methane and carbon dioxide in sample.    ADVANTAGE - The gas chromatographic method for analyzing nitrous oxide, carbon monoxide, methane and carbon dioxide in sample is easily and effectively enabled.    DETAILED DESCRIPTION - A carrier gas having purity of less than 10-5 is passed through a purifier at an output pressure of 0.2-0.6 Mpa, and purity of purified carrier gas is less than 10-6% or 10-7%. The purified carrier gas is injected at 25-195 ml/minute and 10-40 degrees C, into a gas chromatographic column with a to-be-detected sample, adsorbed and desorbed at 20-250 degrees C, nitrous oxide, carbon monoxide, methane and carbon dioxide in the sample supplied into an electron capture detector, a methanator and a hydrogen flame ionization detector are detected at 90-350 degrees C. Data from both electron capture detector and hydrogen flame ionization detector are synchronously input to a chromatography workstation of gas chromatograph, and chromatogram analysis result is obtained.
NOVELTY - Device for preparing liquefied natural gas from coke oven gas comprises a master heat exchanger inside a cold box, where the master heat exchanger is respectively connected with a mixed coolant compression cooling system and a nitrogen compression cooling system. A condenser is installed on the top part of a rectifying tower connected with the master heat exchanger via a pipeline. A reboiler is installed on the bottom part of the rectifying tower. An output pipeline of the condenser is connected with the master heat exchanger via a sub-cooler to connect with a fuel output pipeline.    USE - Used as a device for preparing liquefied natural gas from coke oven gas.    ADVANTAGE - The device can solve problem of freezing probability of methane because of low temperature, which is caused by using mixed coolant as a cold source in traditional liquefied natural gas device.    DETAILED DESCRIPTION - Device for preparing liquefied natural gas from coke oven gas comprises a master heat exchanger inside a cold box, where the master heat exchanger is respectively connected with a mixed coolant compression cooling system and a nitrogen compression cooling system. A condenser is installed on the top part of a rectifying tower connected with the master heat exchanger via a pipeline. A reboiler is installed on the bottom part of the rectifying tower. An output pipeline of the condenser is connected with the master heat exchanger via a sub-cooler to connect with a fuel output pipeline. The reboiler is connected with the sub-cooler via the pipeline and then connected with a liquefied natural gas storage tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for preparing liquefied natural gas from coke oven gas.
NOVELTY - The invention relates to a process for treating a lignocellulosic biomass employed for obtaining a bioethanol fuel. According to the invention, the process is carried out by enzymatic hydrolysis, by mixing homogenization of 80...90% by weight lignocellulosic material consisting of hardwood, softwood and grassy lignocellulose, in a slightly acid or basic medium, with 10...20% 0.1N HCl solution or 1% NaOH solution, at a temperature of less than 0 degrees C and a pressure of less than 760 torr, during a time interval of 1...24 h, to obtain a product having a content of 55...75% homo-polymers of the cellulose and hemicellulose type and mono-saccharides of the pentose and hexose type.
NOVELTY - The invention relates to a generator of hydrogen produced from water by using microwaves and to an aquaplane-type vehicle using said generator. According to the invention, the generator consists of: a microwave generator (A) with a waveguide (1) and an oscillator (2) of the diode-generator or magnetron type proportioned for a frequency of 2...3 GHz, an electrolyser (B) for steam electrolysis, a collector/igniter (C, C') for collecting the oxygen and hydrogen produced by an electrolyser (B) or for the ignition and burning of hydrogen, a power supply circuit (F) with a transformer (F') and a casing (G) made of heat resistant plastic, an electrically-operated valve (D) incorporated in a plastic handle (H) attached to the casing (G) and actuated by an electric switch (18) for the controlled water intake, and a heat-resistant nozzle (3) for water supply inside the waveguide (1) wherein some heat-resistant balls (a) are introduced for the conversion of water into steam, up to the level of a perforated ceramic separator (4) placed at the non-obturated end of the waveguide (1). The electrolyser (B) is mechanically coupled with the waveguide (1) and comprises a secondary waveguide (5) having inside a ceramic or glass electrical insulator (6) and two contact electrodes (7, 7') having at the end facing the igniter (C) some extensions (g, g') for fixing some ignition electrodes (12), between the contact electrodes (7, 7') there being placed in a medial position a solid electrolytic sandwich (19) comprising an electrolytic layer (x) fixed between two layers of cermet or porous metal, while, in the intermediate space, some electrically conductive balls (d) are placed either freely or between some metal plates (d'). The voltage transformer (F') is wound on a Pertinax case (8) fixed on the exterior of the secondary waveguide (5) and using the metal part therein as a metal core.
NOVELTY - The invention relates to a catalyst and a process for preparing C3-C4 alkanes, which uses said catalyst. According to the invention, the catalyst is of modified zeolite type ZSM-5, enriched in alumina, simply or doubly promoted with zinc. According to the invention, the process consists in contacting the bioethanol resulting from the biomass with the catalyst modified at a temperature of 450 degrees C, at a pressure of 4 bar in the presence of hydrogen at a flow rate of 40ml /h and a volume rate of 0.5 h-1, thereby resulting over 40% of C3 fraction and 28...30% of C4 fraction.
NOVELTY - Copper-cobalt-silica catalyst (I) comprises (in wt.%) copper (0-20), cobalt (5-25) and silica (balance amount).    USE - (I) is useful for preparing low-carbon alcohol by using synthesis gas.    ADVANTAGE - (I): has high catalytic activity; produces low-carbon alcohol with high space-time yield; and improves space-time yield of C2+ alcohol.    DETAILED DESCRIPTION - Copper-cobalt-silica catalyst (CuiCoj-SiO2) (I) comprises (in wt.%) copper (0-20), cobalt (5-25) and silica (balance amount).    i, j = 0-3, (i and j are atom mole numbers of Cu and Co respectively).    An INDEPENDENT CLAIM is also included for preparation of (I), comprising (a) adding cupric nitrate trihydrate and cobalt(II) nitrate hexahydrate into absolute ethyl alcohol solution of citric acid monohydrate, where molar ratio of copper to cobalt to citric acid monohydrate is i:j:2(i+j), and performing ultrasonic treating for 5-15 minutes to fully dissolve the ingredients to adjust concentration of copper ion and cobalt ion in ethanol to 0-0.05 mol/l and 0.012-0.071 mol/l respectively, then agitating it for 3-4 hours at 50-70 degrees C, and adjusting pH of reaction solution to 0.5-3, then (b) adding deionized water according to ratio of water to ethanol of 1:4-8, adding tetraethoxysilane while agitating, and continuing to agitate for 0.5-1 hours, evaporating it on water bath at 75-85 degrees C, drying for 1-2 hours in an oven at 110-120 degrees C, and sintering at 350-450 degrees C for 4-6 hours to obtain a catalyst precursor, and (c) heating the catalyst precursor under hydrogen/argon air flow with a volume percent of 5% at normal pressure in a speed of 2-5 degrees C/minute, and reducing it for 8-16 hours.
NOVELTY - Copper-iron based catalyst (I), is new, where carrier of the catalyst is silica and/or alumina.    USE - The catalyst is useful for preparing high carbon alcohol from synthetic gas (claimed).    ADVANTAGE - The catalyst has high selectivity for C5+ alcohol, low cost, and simple preparation; is stable; and has mild reaction condition for synthesizing high carbon alcohol from synthetic gas, which has low requirement of reaction device and suitable for industrial production.    DETAILED DESCRIPTION - Copper-iron based catalyst of formula (CuxFeyMz/SiO2), (CuxFeyMz/Al2O3) or (CuxFeyMz/(SiO2 + Al2O3)) (I), is new, where carrier of the catalyst is silica and/or alumina.    M = transition metal, alkali metal, alkaline-earth metal or rare-earth metal;    y/x = 0.5-2;    z/x = 0.001-0.4; and    x + y + z = 20-85 mass.%.    INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) use of (I) for preparing high carbon alcohol from synthetic gas.
NOVELTY - Preparing aluminum borohydride-ammonia (I) hydrogen storage material with high hydrogen storage quantity, comprises: mixing borohydride, anhydrous aluminum salt and aluminum powder under waterless and oxygen-free atmosphere, heating and reacting to release aluminum borohydride gas, contacting and reacting the gas and the aluminum borohydride-hexa ammonia for 4-8 hours, reducing ammonia coordination number; and ball-milling the obtained product.    USE - The method is useful for preparing hydrogen storage material of I with high hydrogen storage quantity.    DETAILED DESCRIPTION - Preparing aluminum borohydride-ammonia of formula (Al(BH4)3.nNH3) (I) hydrogen storage material with high hydrogen storage quantity, comprises: mixing borohydride, anhydrous aluminum salt and aluminum powder under waterless and oxygen-free atmosphere, heating and reacting to release aluminum borohydride gas at 10-80 degrees C, contacting and reacting the gas and aluminum borohydride-hexa ammonia for 4-8 hours, reducing ammonia coordination number; and ball-milling the obtained product, where the molar ratio of borohydride to the aluminum ion is 1:2-1:5; and the aluminum powder is 5-50% of the total weight of the borohydride, the anhydrous aluminum salt and the aluminum powder.    n = 1-5.
NOVELTY - Producing natural gas by magnetized hematite and coke oven gas comprises: adding hematite powder of particle size /~ 2 mm in a mixing reactor, passing the coke-oven gas, allowing to react by heating, decarbonizing, dehydrating the coke-oven gas and magnetizing to obtain the natural gas, replacing the non-weak magnetic iron oxide in the hematite powder into magnetite with strong magnetic properties, magnetizing the ore, pulping directly or wet grinding the pulp, sorting through a magnetic separator and dehydrating the magnetic mineral to obtain concentrated ferrous ore.    USE - The method is useful for producing natural gas by magnetized hematite and coke oven gas.    ADVANTAGE - The method: integrates the restoration of magnetized hematite and coke-oven gas and methane enriched artificial gas removal; is simple in process, economical and has wide adaptability for each hematite; easily sorts the magnetized mineral and hence obtains high-level iron ore concentrate.
NOVELTY - Medium-proportion methanol gasoline additive comprises (in vol.%) a mixture of ethanol (5- 10), isopropanol (10-15), tertiary butanol (10-15), benzene (5-10), dimethylbenzene (1-5), ethylbenzene (2-5), petroleum ether (5-10), hydrogen peroxide (1-5), 3-ethyl-methylbenzene (5-10), isobutyl alcohol (5-10), diethyl ether (1-5), isoamyl alcohol (1-5) and 120# solvent oil (25-30), where the sum of the vol.% of the components is 100%.    USE - Used as a medium-proportion methanol gasoline additive.    ADVANTAGE - The additive comprises different components with physicochemical properties, thus improving comprehensive properties e.g. phase separation resistance, corrosion resistance, anti-detonation property, anti-oxidation stability and a prominent phase separation resistance, when added with medium-proportion methanol gasoline.
NOVELTY - The machine has a combustion furnace provided with an outer wall and an inner wall to form a water cooling chamber. The water-cooling chamber is equipped with water inlet and outlet pipes. The inner wall is provided with a combustion chamber. The combustion chamber is provided with a furnace bridge. A lower part of the furnace bridge is provided with a slag collecting chamber. A de-occlusion device is connected with a pushing device by a linkage device. An air outlet pipeline is connected with the collecting chamber. A fan is connected to the combustion chamber through an air pipe.    USE - Flat-push type biomass gasification combustion machine.    ADVANTAGE - The fan is connected to the combustion chamber through the air pipe, which is capable of effectively pushing dust slag for stable and efficient combustion. The machine is environmental-friendly and energy-saving. The machine enables reaching 95 percent of heat energy utilization rate and reducing ash residue of about less than 2 percent so as to realize free control for adjusting and feeding air quantity, so that industrial continuous range power is adjusted according to actual requirements. The machine can bear stable high power, and replaces diesel or gas.
NOVELTY - Electrolyzer comprises a housing, an electrode, and an electrical power source, where the electrode comprises a conducting material coated with a nanoporous oxide.    USE - The electrolyzer is useful: for producing gases comprising hydrogen, oxygen (both preferred), chlorine, bromine and/or fluorine (all claimed); and in hydrogen on demand systems.    ADVANTAGE - The electrolyzer: reduces the over potential required to produce a gas from an aqueous solution by electrolysis; does not require rare and costly precious metals, thus are cost effective; and reduces the carbon monoxide and hydrogen carbon emissions in vehicles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a gas by electrolysis, comprising contacting an aqueous solution with the electrode connected to an electrical power source, and applying a voltage from the electrical power source to the electrode.
NOVELTY - Sight glass assembly on a fermentation container (2) of a biogas plant, comprises a sight glass armature (8) arranged in a container wall region of the fermentation container, to observe inner side (12) of the fermentation container. The sight glass armature is inserted into side wall portion (3) that extends vertically in the fermentation container-vertical axis direction. The sight glass armature is formed and arranged such that that a portion of sight glass (9) or sight glass with respect to outer side of side wall portion, is displaced inwardly in direction of container inner side.    USE - Used as a sight glass assembly.    ADVANTAGE - The sight glass assembly ensures very good and functionally reliable observation of circumstances inside the fermentation container, and exhibits wide viewing angle with respect to the fermentation container.    DETAILED DESCRIPTION - Sight glass assembly on a fermentation container (2) of a biogas plant, comprises a sight glass armature (8) arranged in a container wall region of the fermentation container, to observe inner side (12) of the fermentation container. The sight glass armature is inserted into a side wall portion (3) that extends vertically in the fermentation container-vertical axis direction. The sight glass armature is formed and arranged such that at least one portion of at least one sight glass (9) or the sight glass with respect to an outer side of the side wall portion, is displaced inwardly in the direction of the container inner side and/or inclined inwardly and downwardly in the direction of the container.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a portion of the fermentation container having a foil roof with the sight glass assembly.    Fermentation container (2)    Side wall portion (3)    Sight glass armature (8)    Sight glass (9)    Container interior (12)
NOVELTY - The system (1') has rotary kiln (2) which heat-processes process target object such as waste material and produces thermal decomposition residue and pyrolysis gas. A combustion melting furnace (3') produces a molten slag by burning pyrolysis gas and the thermal decomposition residue. The molten slag is put into the thermal decomposition apparatus with a process target object.    USE - System for performing pyrolytic process to waste material such as municipal solid waste, industrial waste and car shredder dust generated from sheet of motor vehicle and instrument panel.    ADVANTAGE - Since the combustion melting furnace is provided to produce molten slag by burning pyrolysis gas and the thermal decomposition residue, the plastics adhesion and solidification in the rotary kiln can be suppressed without preparing adhesion prevention media such as sand separately when pyrolytic-processing car shredder dust.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pyrolytic process method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for performing pyrolytic process to waste material. (Drawing includes non-English language text)    System for performing pyrolytic process to waste material (1')    Rotary kiln (2)    Combustion melting furnace (3')    Waste heat boiler (5)    Sorting apparatus (7)
NOVELTY - The apparatus has electrolysis chamber (11) into which electrolyzed raw water (12) is introduced. Several diaphragms (13) divide the inside/exterior of electrolysis chamber. A dilution gas supply device (3) dilutes the hydrogen gas emitted from electrode plate (14,15). The hydrogen gas concentration of cathode vicinity is always maintained at predetermined value at the time of electrolysis by ventilating the cathode in dilution gas supplied from dilution gas supply device. The mixed gas containing hydrogen gas and the dilution gas is supplied to a biological body.    USE - Hydrogen gas supply apparatus for biological bodies such as human and animal, used in medical field and home.    ADVANTAGE - hydrogen gas can be used safely on the health. The health maintenance can be improved. The convenience at the time of biological body supply and the stability of the mixed gas supply can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen gas supply apparatus for biological bodies. (Drawing includes non-English language text)    Dilution gas supply device (3)    Electrolysis chamber (11)    Electrolyzed raw water (12)    Diaphragm (13)    Electrode plate (14,15)
NOVELTY - Processing of used cooking oil involves passing used cooking oil through a filter (115) to remove solid contaminates, heating at 120 degrees F used cooking oil that passed through the filter (115), transferring used cooking oil, passing used cooking oil processed by a centrifuge mechanism (165) through a filter (150) to remove solid contaminates to produce recycled cooking oil and transferring recycled cooking oil output by the filter (150) in at least one storage tank (125). The storage tank is capable of agitating and heating the recycled cooking oil.    USE - Processing of used cooking oil used as feedstock for production of biodiesel.    ADVANTAGE - The method enables processing of used cooking oil with high quality.    DETAILED DESCRIPTION - Processing of used cooking oil involves passing used cooking oil through a filter (115) to remove solid contaminates, heating at 120 degrees F used cooking oil that passed through the filter (115), transferring used cooking oil, passing used cooking oil processed by the centrifuge mechanism through a filter (150) to remove solid contaminates to produce recycled cooking oil and transferring recycled cooking oil output by the filter (150) in at least one storage tank (125). The storage tank is capable of agitating and heating the recycled cooking oil. The method is continuous process. The size of solid contaminates removed from the filter (150) are smaller than the solid contaminates separated from the filter (115). An INDEPENDENT CLAIM is included for device (100) for processing used cooking oil, which has a filter (115), a heating mechanism (135), a centrifuge mechanism, a filter (150) and storage tank(s).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of device for processing used cooking oil.    Device (100)    Filters (115,150)    Pumps (120,145)    Storage tank (125)    Agitating mechanism (130)    Heating mechanism (135)    Boiler (140)    Centrifuge mechanism (165)
NOVELTY - The electric field generator (100) has electrically conductive parallel cathode plates (108) and anode plates (110) that are supported by a non-electrically conductive framework (106), and provided at opposite ends of each plate array (102). Neutral plates (104b,104d-104g,104i) are interposed between the cathode and anode plates, and arranged in interleaved subsets (112,114). Each subset has at least three neutral plates that are electrically connected together, and electrically isolated from the cathode and anode plates and other neutral plates.    USE - Electric field generator for producing cleaner combustible fuel.    ADVANTAGE - Commingling of produced gases from the anode and cathode is prevented since the membrane forms a barrier. Operation of aqueous reactor is enhanced by using applied electric field to initiate or sustain chemical reaction or creation of plasma in the reactor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method of disassociating hydrogen and oxygen from water in reaction vessel; and    (2) a method of preparing combustible fluid.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the electric field generator.    Electric field generator (100)    Plate array (102)    Neutral plates (104b,104d-104g,104i)    Non-electrically conductive framework (106)    Cathode plates (108)    Anode plates (110)    Subsets (112,114)
NOVELTY - The sewage-treatment system has a solid-liquid separator (2) which is provided with a main filter material-filled layer. The sewage (W1) is passed into main filter material-filled layer with upward flow to separate sewage into solid components and a filtrate (W2). A percolating filter (3) is provided with an auxiliary filter material-filled layer. Filtrate is spread on top of auxiliary filter material-filled layer, and allowed to flow down into auxiliary filter material-filled layer. The treated water (W3) is obtained by bio-treating filtrate using microorganisms.    USE - Sewage-treatment system.    ADVANTAGE - The generation of the offensive odor from the percolating filter is suppressed. The clogging of the sprinkler nozzle is prevented. The space consumption of the sewage-treatment system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage-treatment system. (Drawing includes non-English language text)    Solid-liquid separator (2)    Percolating filter (3)    Sewage (W1)    Filtrate (W2)    Treated water (W3)
NOVELTY - The method involves forming a carbon layer in a base-material surface (S1), bonding the formed carbon layer to a base material (S2), and forming a gas flow path. The base material is molded by a press molding process (S3), and the base-material surface is covered by the carbon layer, where the base material consists of unalloyed titanium or a titanium alloy. The material is heat-processed (S4). The carbon layer is provided in a surface of a fuel cell separator. Thickness of the base material is 0.05-1.0 mm. The carbon layer and the base material are adhered through an intermediate layer.    USE - Method for manufacturing a fuel cell separator of a fuel cell that is utilized for a fuel cell electric vehicle, mobile telephone and a personal computer. Uses include but are not limited to a polymer electrolyte fuel cell (PEFC), alkali electrolyte-type fuel cell (AFC), phosphoric acid fuel cell (PAFC), molten carbonate fuel cell (MCFC), solid oxide fuel cell (SOFC) and bio-fuel cell.    ADVANTAGE - The method enables molding the base material, thus improving producibility and adhesiveness of the base material and the carbon layer, and hence reducing manufacturing cost of the separator, and possibility of peeling of the carbon layer from the base-material surface.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing a fuel cell separator.'(Drawing includes non-English language text)'    Step for forming carbon layer in base-material surface (S1)    Step for bonding formed carbon layer to base material (S2)    Step for molding base material (S3)    Step for hest-processing base material (S4)
NOVELTY - Producing selective hydrocarbons from plants, comprises providing a feed material of plant biomass containing aliphatic polymers, subjecting the plant biomass to water at a subcritical temperature for a predetermined period of time in a reactor, collecting an aqueous liquid phase product from the reactor, and separating the hydrocarbons from the aqueous liquid phase product.    USE - The selective hydrocarbons are useful as biofuels.    ADVANTAGE - The method allows economical production of selective hydrocarbons from plants with high yield.
NOVELTY - Preparation of 3-amino-4-(2,4,5-trifluorophenyl)butanoate intermediates (I) involves: reacting 2,4,5-trifluoro-phenyl intermediate (II) with an amine (III), either in protic solvent (particularly water), or in a mixture of protic solvents (particularly comprising water), or without adding of solvents.    USE - For the preparation of 3-amino-4-(2,4,5-trifluorophenyl)butanoate intermediates which are useful for the preparation of anti-diabetic agents, particularly (R)-3-amino-1-(3-(trifluoromethyl)-5,6,7,8-tetrahydro(1,2,4)triazol(4,3-a)pyrazin-7-yl)-4-(2,4,5-trifluorophenyl)butan-1-on (sitagliptin) (claimed).    ADVANTAGE - The process is conducted under mild reaction conditions by using non-hazardous reagents, particularly under environmentally friendly reaction conditions using water as green solvent or without using solvent at all, and also is carried out without using special equipment. Thus the process is simple, economical, industrially amenable and environmental friendly.    DETAILED DESCRIPTION - Preparation of 3-amino-4-(2,4,5-trifluorophenyl)butanoate intermediates of formula (I), involves: reacting 2,4,5-trifluoro-phenyl intermediate of formula (II) with an amine of formula HNR1R2 (III), either in a protic solvent (particularly water), or in a mixture of protic solvents (particularly comprising water), or without adding of solvents.    R1, R2=H, optionally chiral 1-12C alkyl, or optionally chiral 6-24 aryl (both optionally substituted by aryl and/or aryloxy), optionally chiral 1-12C alkyloxy (optionally substituted by aryl), optionally chiral 6-24C aryloxy (optionally substituted by alkyl substituted), benzyl, optionally chiral 2-13C alkaloyl or optionally chiral 7-25C aroyl (both optionally substituted by aryl), optionally chiral 2-13C alkoxycarbonyl, optionally chiral 7-25C aryloxycarbonyl, tosyl, optionally chiral 3-15C silyl, or optionally chiral 3-15C silyloxy;    R3=1-6C alkyl
NOVELTY - A metal complex consists of alkylene dicarboxylic acid compound, II group, VII-X group and XII group metal ion, and organic ligand (I) in which bidentate coordination is enabled.    USE - Metal complex is used for adsorbent and separation material for adsorbing and separating carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor or organic vapor (all claimed).    ADVANTAGE - The metal complex has high gas adsorption characteristics and gas separation characteristics.    DETAILED DESCRIPTION - A metal complex consists of alkylene dicarboxylic acid compound, II group, VII-X group and XII group metal ion, and organic ligand of formula (I) in which bidentate coordination is enabled.    X,Y'=CH2, CH(OH), NH, O or S;and    R1-R8=H, halo, or alkyl, alkoxy, formyl, acyloxy, alkoxy carbonyl, nitro, cyano, amino, monoalkyl amino, dialkylamino, or acylamino (all optionally substituted).    An INDEPENDENT CLAIM is included for manufacture of metal complex, which involves reacting organic ligand with alkylene dicarboxylic acid compound and metal salt chosen from II group, VII-X group and XII group metal, in a solvent, and depositing metal complex.
NOVELTY - Producing an agent, comprises: grinding a biomass feedstock to produce ground biomass particles; subjecting the ground biomass particles to sequential or concurrent ramps of temperature and pressure shocks; selectively collecting at least one volatile component as it is released from the ground biomass particles; collecting a last remaining nonvolatile component comprising biomass fractionator (BMF) char; rendering a surface of the BMF char hydrophilic; exposing the BMF char to microorganisms; and adding the BMF char to soil.    USE - The method is useful for producing an agent, which is useful for enhancing soil growth (claimed).    ADVANTAGE - The method: utilizes the pressure shocks that increase thermal conductivity of formed nonvolatile carbonaceous material within the ground biomass particles and decrease the effective density of the ground biomass particles; and provides the agent (i.e. BMF char) that not only enhances soil growth but can sequester carbon for long periods of time.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram depicting a process for rendering biochar suitable as a soil enhancing agent.    Creating biomass fractionator (BMF) char from biomass (600)    Removing detrimental hydrocarbons from BMF char (610)    Removing absorbed gases from BMF char pores (620)    Adding compost agent to BMF char (640)    Mixing BMF char into soil (660)
NOVELTY - Night soil aerobic composting device comprises an air inlet pump, an insulating heat-exchange tank, a flowmeter, a perforated baseplate, a sampling port, a temperature probe, a gas pipeline, an air outlet, a purifying tank, a leachate outlet, a composting tank, a leachate storage tank and a computer. The air inlet pump is connected with the insulating heat exchange tank. The flowmeter located in the insulating heat exchange tank is connected with the leachate storage tank via pipeline. The composting box is located on the upper part of the leachate storage tank.    USE - Used as a night soil aerobic composting device.    ADVANTAGE - The device occupies small space, ensures convenient maintenance and is safe; reduces the discharge of agriculture waste, maintains the cleanliness in soil and groundwater, and reduces pollution of drainage network when applied to urban area.
NOVELTY - A biological carrier comprises biological carrier with two connection ends that are fixed and provided with three dimensional butterfly wings.    USE - Biological carrier for sewage treatment.    ADVANTAGE - The biological carrier is provided with butterfly wings, so it will automatically float in sewage. The addition of three dimensional butterfly wings can increase the unit number of biological carrier specific surface area, thus increasing the bearing of microorganism, adding bridging effect of microorganism film-hanging, increasing absorbing and degrading microorganism function, and accelerating the film hanging speed. After the end of the carrier is fixed into the sewage to be processed, the two ends of the biological carrier are fixed into the sewage. If sewage tank is deep, every one meter is provided with a connecting belt, which can make the biological carrier prolonged to 4-5 long, without the phenomenon of winding the impact of aeration, so as to improve the surface area of the biological carrier for processing sewage.
NOVELTY - Sewage treatment power supply comprises high voltage pulse power supply comprising a power frequency rectifying filter circuit. An output end of the power frequency rectifying filter circuit is connected with an input end of high frequency converter. The output end of the high frequency converter, the input and output ends of high frequency inverter are provided with a high frequency boosting transformer or a boosting transformation rectifier module.    USE - Used as a sewage treatment power supply.    ADVANTAGE - The sewage treatment power supply: utilizes the high frequency boosting transformer to produces high voltage pulse wave for sewage treatment, and utilizes the high voltage pulse power supply i.e., pulse power supply utilizes high voltage and high energy density to change the molecular structure of the processing object e.g. as industrial waste water and initiates a series of aqueous phase chemical processes for degrading organic matter in water, and electronic transition generates high energy electron radiation, ozone oxidation, ultraviolet light decomposition action and ultrasonic action to realize waste water treatment set effect in the electrochemical process due to molecule ionization.
NOVELTY - Aerobic sludge compositing by using conditioning agent processed by acidification comprises (i) preparing potassium bisulfate solution as an oil acidifying liquid, taking a conditioning agent, soaking the conditioning agent in the oil acidifying liquid, taking out the conditioning agent, and drying to obtain a pre-treated acidified conditioning agent, (ii) mixing the pre-treated acidified conditioning agent and dehydrated sludge to obtain a mixture, where the weight of the dehydrated sludge is dry basis weight, and adjusting pH of the mixture, and (iii) performing high temperature composting.    USE - The method is useful for aerobic sludge compositing.    ADVANTAGE - The method: ensures repetitive use of the oil acidifying liquid; reduces the implementation cost; effectively controls ammonia volatilization; and reduces the nitrogen loss.    DETAILED DESCRIPTION - Aerobic sludge compositing by using conditioning agent processed by acidification comprises (i) preparing potassium bisulfate solution (1 wt.%) as an oil acidifying liquid, taking a conditioning agent (60-80 g; particle size 10-30 mm), soaking the conditioning agent in the oil acidifying liquid (1 l) for 22-25 hours, taking out the conditioning agent, and drying until the water content becomes 4-6% to obtain a pre-treated acidified conditioning agent, (ii) mixing the pre-treated acidified conditioning agent obtained from the step (i) and dehydrated sludge according to a weight ratio of 1:1 to obtain a mixture, where the weight of the dehydrated sludge is dry basis weight, and then adjusting pH of the mixture to 5-6, and (iii) performing high temperature composting of the mixture of the conditioning agent and dehydrated sludge obtained from the step (ii) at a ventilation rate of 0.05-2 m3/minute for 3-5 days at a high temperature, and then continuously stacking until the stack temperature is reduced to room temperature to complete high temperature composting.
NOVELTY - The device comprises a semi-sealed cavity movably connected to one side of granulator, and connected with a drying system, a screening system, a cooling system, a packaging system and a packing system. A gas outlet provided on top of the cavity is connected with dust remover, washer, acid distribution tank and other side of the granulator. The acid distribution tank is connected with dilute sulfuric acid spraying pipe. The device includes gas ammonia storage tank and liquid ammonia storage tank. A batching system is connected with other side of the granulator.    USE - A production device of compound fertilizer without filling agent.    ADVANTAGE - The device has simple structure, stable operation, high pelletizing rate, and no wastewater discharge and no filling agent. It produces compound fertilizer with good solubility, dissolved without residue, low water content, low cost and will not cause pollution to the environment.
NOVELTY - The furnace has an end enclosure placed between adjacent parts. A side air outlet of a lower part of a cylinder body is provided with a liquid slag discharging port. A side wall of a lower part of the cylinder body is provided with a plasma torch nozzle and a gun inlet. A middle section is provided with the side wall of the cylinder that is uniformly distributed along a circumferential direction of an air inlet. A middle cone cylinder is symmetrically arranged on a side wall of a feeding port. A sealing head is provided with an air outlet and a material level measuring opening.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace utilizes external heat source strengthening the gasification process and gasification temperature, and fast reaction speed. The furnace has better fuel adaptability, high carbon conversion rate and effective gas component.
NOVELTY - A citrus fruit fly attracting device comprises a cup body inserted with tapered round tube(s), where larger end diameter of tapered tube is installed on peripheral wall of the cup body, and smaller end diameter of tapered tube is extended into inner cavity of the cup body. The cup body is set with cotton plant extract solution.    USE - Citrus fruit fly attracting device.    ADVANTAGE - The device can reduce use of chemical agent and decrease cost in agricultural pest control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for attracting citrus fruit fly by using plant extraction liquid, comprising sealing opening of cup body of citrus fruit fly attracting device, volatilizing cotton plant extract liquid to lure citrus fruit fly and allow fly to climb through inner cavity of the cup body along the tapered round tube, and opening the opening of the cup body.
NOVELTY - The system has a reaction bath (202,204,206) having exhaust gas valve (220a-220c) that is provided for inhaling organic waste in gas discharged from an agitation portion (100). A compressor (500) is made to eject gas to reaction bath, so as to stir the organic waste on bottom surface of reaction bath. The organic waste is vanished, while cultivating microorganism and strain for acid fermentation and methane fermentation. The water is filled to preset height, while blocking agitation portion, reaction bath and liquefied fertilizer production tub (300) by partition wall.    USE - Treatment system for organic waste matter such as livestock excretions, sewage sludge and food waste.    ADVANTAGE - The recycling process of organic waster can be performed easily. The operation maintenance of treatment system can be facilitated. By producing the biogas through anaerobic digestion of organic waste, the running cost of treatment system can be reduced. The cause of environment civil application can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the treatment system for organic waste matter. (Drawing includes non-English language text)    Agitation portion (100)    Reaction bath (202,204,206)    Exhaust gas valve (220a-220c)    Liquefied fertilizer production tub (300)    Compressor (500)
NOVELTY - Organic fertilizer for red jujube, comprises (in part by wt.) weathered coal (45-55), wheat bran (5-10), cottonseed cake (5-10), straw (20-30), urea (1-2), water (50-60), Bacillus fermentation liquor (10-12), iron source (0.01-0.02), zinc source (0.01-0.02), boron source (0.05-0.1) and calcium source (0.1-0.2).    USE - The organic fertilizer is useful for red jujube.    ADVANTAGE - The organic fertilizer: has trace elements and organic substances with high biological activity, and no chemical residuals; is ecofriendly; provides synthetic nourishment while supplying organic substances to the jujube tree, hence the jujube tree grows vigorously and healthy; enhances the disease-resistance and stress resistance; improves the fruit setting rate and fruit weight; reduces the rate of the flower and fruit drop, and fruit cracking; and increases production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising mixing the weathered coal, wheat bran, cottonseed cake and straw, adding into the fermentation tank, dissolving urea in water, adding into the Bacillus fermentation liquor, stirring after mixing uniformly, adding the iron source, zinc source, boron source and calcium source after fermenting, and stirring uniformly.
NOVELTY - Preparing organic fertilizer comprises (i) completely mixing the organic material containing carbon and nitrogen in a ratio of 20-30:1, placing the mixed material in a fermentation tank, inoculating microbial inoculum and performing anaerobic fermentation to obtain anaerobic fermentation liquid, (ii) mixing the anaerobic fermentation waste residue with the organic material of carbon and nitrogen ratio 25:1 and performing facultative windrow composting for 30 days, and separating the upper part of the stack as nitrogenous fertilizer and the bottom part of stack as carbon-enriched fertilizer.    USE - The method is useful in preparing organic fertilizer for organic farming; and the organic fertilizer is useful as a base fertilizer for crop cultivation, as an additional fertilizer for crop growth, and as complete fertilizer.    ADVANTAGE - The fertilizer increases the carbon fixation and improves the utilization rate of the nutrient.    DETAILED DESCRIPTION - Preparing organic fertilizer for organic farm comprises (i) completely mixing the organic material containing carbon and nitrogen in a ratio of 20-30:1, adjusting the solid mass percentage in the mixed material to 17-22%, placing the mixed material in a fermentation tank, inoculating microbial inoculum and performing anaerobic fermentation for 10-15 days by controlling the temperature at 25-35 degrees C to obtain anaerobic fermentation liquid, (ii) mixing the anaerobic fermentation waste residue with the organic material containing carbon and nitrogen in a ratio of 25:1 and performing facultative windrow composting for 30 days, and subjecting 1/2 of the windrow from top to bottom for forcible ventilation, allowing the stack temperature to reach ambient temperature, and separating the upper part of the stack 2/3 as nitrogenous fertilizer and 1/3 of the bottom part of the stack as carbon-enriched fertilizer.
NOVELTY - Mixed culture matrix comprises 2-4 vol.% of garden soil, 1-3 vol.% of river sand or sandy soil, 1-2 vol.% of coconut residuum or decomposed sawdust, 1-3 vol.% of decomposed cow dung, 2-3 vol.% of pond silt, 1-2 vol.% of combusted soil and 3-5 vol.% of carbendazim or chlorothalonil.    USE - The mixed culture matrix is useful for raising cashew seedlings.    ADVANTAGE - The mixed culture matrix is capable of protecting the soil from being hardened after the seedlings are raised, and increasing disease-resistant capability, and improves germination of the cashew seedling in a simple, safe, cost-effective and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the mixed culture matrix, comprising: (a) taking a silt from a fish pond, exposing the slit under blazing sun for 2-3 days, and breaking the slit into granules with a size of 0.5-1 cm3 to obtain pond silt; (b) covering a surface soil on the cashew or other fallen leaves of other crops, and piling up shovelled grass billets to form a combustion pile like a grave mound to prepare combusted soil; (c) mixing 2-4 vol.% of the garden soil, 1-3 vol.% of the river sand or 1-3 vol.% of the river sand or the sandy soil, 1-2 vol.% of the coconut residuum, 1-3 vol.% of the decomposed cow dung or the decomposed sawdust, 2-3 vol.% of the pond silt and 1-2 vol.% of the combusted soil, and agitating the mixture to obtain a preliminarily mixed culture matrix; and (d) spraying 1000-1500 times of 50% carbendazim or chlorothalonil onto the agitated preliminarily mixed culture matrix to control moisture level to 60%, and covering the agitated preliminarily mixed culture matrix using a film for 2-3 days.
NOVELTY - A hydrogen-producing arrangement (20) consists of a plate-shaped or cylindrical hydrogen-developing component (21), in the electrolyte-contacting surface of which regions formed from magnesium, zinc or their alloys alternate with regions formed from iron (alloy), and a unit for accumulating hydrogen developed on the surface of hydrogen-developing component.    USE - Arrangement is used for producing hydrogen from electrolyte solution and in arrangement used for producing hydrogen and electrical power in drive systems of vehicles, aircraft, boat, and submarine (all claimed). Can also be used for electronic devices and toys.    ADVANTAGE - The arrangement is constructed in a simple manner and is highly efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of hydrogen from electrolyte solution;    (2) electrochemical arrangement for producing hydrogen and generating electrical power;    (3) power supply system; and    (4) production of hydrogen and generation of electrical power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the hydrogen-developing component.    Arrangement (20)    Hydrogen-developing component (21)    Magnesium cylinder core (21a)    Steel helix (21b)
NOVELTY - The device has a partition wall that is formed on the center of a deodorization case (701). A water outlet (702) is arranged inside the deodorization case for discharging the condensed water generated in the deodorization process to the outside. A heat rod temperature sensor is installed at a heat rod protective cover to sense the heat-generating temperature of the heat rod. An aid temperature sensor is installed at low-end of fermentation tank (200). An automatic outlet door automatically exhausts the remnant exceeding in the fermentation tank after food waste process.    USE - Device for treatment of food waste remaining in home and dining room.    ADVANTAGE - The installation of the device can be facilitated easily. The exchanging of the device can be performed accurately. The service life of the heater can be prolonged. The delivery of heat can be raised. The steam generated in the fermentation tank inside the exhaust system can be exhausted rapidly. The moisture remaining inside the blower can be water-leaked. The phenomenon of disturbing the flow of air can be prevented. The ventilation effect of the steam flowed through the exhaust system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the device for treatment of food waste.    Inlet portion (105)    Fermentation tank (200)    Exhaust pipe (504)    Deodorization case (701)    Water outlet (702)
NOVELTY - The apparatus (1) has a plasma generating device (20) that is provided for forming a plasma flame by the discharge of plasma to a portion of hydrogen sulfide supply chamber (10). A plasma decomposition chamber (30) is connected in bottom surface of waveguide (22) of plasma generating device. The lower portion of recombination chamber (40) is connected with lower portion of the plasma decomposition chamber. A cyclone (50) is provided for separating synthetic gas and combustible gas of solid sulfur, and is installed at lower portion of recombination chamber.    USE - Apparatus for removing hydrogen sulfide.    ADVANTAGE - Since the cyclone is provided for separating synthetic gas and combustible gas of solid sulfur, the hydrogen sulfide can be removed easily and the corrosion of removing apparatus can be prevented. The maintenance cost and production cost of hydrogen sulfide removing apparatus can be reduced. The structure of hydrogen sulfide removing apparatus can be simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for removing hydrogen sulfide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for removing hydrogen sulfide. (Drawing includes non-English language text)    Apparatus for removing hydrogen sulfide (1)    Hydrogen sulfide supply chamber (10)    Plasma generating device (20)    Waveguide of plasma generating device (22)    Plasma decomposition chamber (30)    Recombination chamber (40)    Cyclone (50)
NOVELTY - Pre-processing and improving organic compound sludge anaerobic fermentation marsh gas comprise pre-treating the concentrated sludge and dewatered sludge to prepare mixed sludge, feeding the mixed sludge for anaerobic digestion, discharging sludge with the same volume, and collecting marsh gas.    USE - Method for pre-processing and improving organic compound sludge anaerobic fermentation marsh gas (claimed).    ADVANTAGE - The method shortens low organic compound sludge anaerobic starting time, improves organic compound sludge anaerobic digestion gas amount and promotes low organic compound sludge resource utilization.
NOVELTY - Agricultural fungicide comprises mixed dibasic acid, waste copper wire hydrogen peroxide, and aqueous ammonia.    USE - Used as an agricultural fungicide.    ADVANTAGE - The fungicide is economical and ecofriendly. The preparation method saves energy and increases the conversion rate of copper (up to 100%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the agricultural fungicide, comprising reacting the mixed dibasic acid, waste copper wire, hydrogen peroxide and aqueous ammonia as raw material at room temperature to obtain the product.
NOVELTY - The device has a main control unit for receiving a diesel engine start signal from a power input end of a drive power supply of a main control unit. An output end of a drive power supply of a plasma generating unit comprises an airflow pipeline. A ring-shaped support is provided with the airflow pipeline and a plasma discharge unit, where the plasma discharge unit is provided with multiple plasma generators. Plasma generating sheets i.e. ceramic discharge elements, are arranged on a support frame.    USE - Ultra-low temperature starting device for use in a diesel vehicle.    ADVANTAGE - The device is convenient to install and use, simple in structure and environmental-friendly. The device ensures better safety, better magnetic property procedure for a diesel engine and better low-temperature starting performance, and has better performance.    DETAILED DESCRIPTION - The support frame is made of an epoxy resin glass fiber cloth, an aluminum alloy and a light metal material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an ultra-low temperature starting device.'(Drawing includes non-English language text)'
NOVELTY - The generator has a center electrode (11) formed in a vortex flow generating nozzle (13), which is arranged between torch nozzles (12, 14). A gas chamber (15) is formed in the torch nozzles and connected to an electric power unit. The power unit is connected to the torch nozzles. Openings (18-1, 18-2) are utilized for supplying a cooling agent in a cooling compartment (CM), which is connected to a cooling part. An inner wall (14-2) of the generator is connected with a plasma jet. The openings supply working gas inside the generating nozzle.    USE - Plasma jet generator for conversion of reactant i.e. water (claimed) for production of energy. Uses include but are not limited to plasma cutting industry, welding industry, ceramic industry and metallurgy.    ADVANTAGE - The generator is inexpensive, and consumes less energy. The generator has high transformation efficiency, and improves capacity and energy efficiency of a reactant.    DETAILED DESCRIPTION - The gas chamber is arranged in another inner wall (13-1) of the generator. The center electrode is made of copper, tungsten or an alloy. An INDEPENDENT CLAIM is also included for a method for converting reactants and waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a plasma jet generator.    Cooling compartment (CM)    Center electrode (11)    Torch nozzles (12, 14)    Vortex flow generating nozzle (13)    Inner walls of generator (13-1, 14-2)    Gas chamber (15)    Openings (18-1, 18-2)
NOVELTY - The device has an alternating current (AC) torch pyrolysis gasification furnace provided with a temperature expansion reaction chamber. The pyrolysis gasification furnace, the temperature expansion reaction chamber, a quench tower and a turbulence tower are connected with each other to form a lower alternating curve manifold air channel. An upper part of the pyrogenation gasification furnace is provided with a feeding opening. A bottom part of the pyrogenation gasification furnace is provided with a pipe. Top of the pyrolysis gasification furnace is provided with an explosion-proof device.    USE - Plasma gasification urban domestic rubbish processing device.    ADVANTAGE - The device is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plasma gasification urban domestic rubbish processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a plasma gasification urban domestic rubbish processing device.
NOVELTY - The incinerator has a furnace body whose inner side is provided with a combustion chamber (1). The furnace body is connected with an inlet pipe (2) and an exhaust channel (3). A tail gas treatment furnace unit is arranged in another combustion chamber (4). A bottom part of the furnace body is provided with a grate (5). A plasma torch (6) is arranged above the grate. The fire grate is provided with a cooling tank (7). A cooling channel is arranged between an inner sleeve (8) and an outer sleeve (9). An upper part of the outer sleeve is connected with a gas barrier plate (10).    USE - Plasma rubbish incinerator.    ADVANTAGE - The furnace body is utilized for decomposing rubbish at high temperature. The incinerator reduces harmful substance discharging rate while burning rubbish.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a plasma rubbish incinerator.    Combustion chambers (1, 4)    Inlet pipe (2)    Exhaust channel (3)    Grate (5)    Plasma torch (6)    Cooling tank (7)    Inner sleeve (8)    Outer sleeve (9)    Gas barrier plate (10)
NOVELTY - The purifier has a waste gas inlet and a purified gas outlet located on two sides of a plasma reaction chamber. Metal pipelines are distributed in the plasma reaction chamber in an axial direction. A tubular electric wire is passed through center of each pipeline and connected with an external high pressure power supply. A gap is formed between the tubular electric wire and a wall of the pipeline.    USE - Macromolecular intelligent waste gas purifier.    ADVANTAGE - The purifier can reduce the power consumption of the plasma, control the formation of the harmful bya product, and improve the cost performance. The purifier activates, ionizes and cracks peculiar and smelly harmful gas molecules by the low temperature plasma formed by the high energy ion generated by the low temperature discharge technique to be oxidized and decompressed to be smell-less and harmless substances. The purifier kills mycete and pathogenic bacteria in the air. The purifier has 98 percentages of sterilization rate and the removing rate of the peculiar smell, so that the clean and fresh air is provided to the human.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a macromolecular intelligent waste gas purifier.
NOVELTY - Recycling oxygen and chlorine comprises oxidizing hydrogen fuel mixture with water to absorb the remaining hydrogen chloride, dehydrating the mixture with concentrated sulfuric acid and separating the remained mixed gas using pressure swing adsorption device, where the pressure swing adaptation device comprises at least two absorption tower units, the absorbent in the absorbing tower is at least one of the two absorbents such as active carbon or silicon and the active carbon's volume ratio is 0-50%, after absorbing, pressure, washing and desorption.    USE - The method is useful for recycling oxygen and chlorine.    ADVANTAGE - The simple process is capable of recovering oxygen and chlorine with high rate and hydrogen and oxygen with high purity in an environmental-friendly manner.    DETAILED DESCRIPTION - Recycling oxygen and chlorine comprises oxidizing hydrogen fuel mixture with water to absorb the remaining hydrogen chloride, dehydrating the mixture with concentrated sulfuric acid and separating the remained mixed gas using pressure swing adsorption device, where the pressure swing adaptation device comprises at least two absorption tower units, the absorbent in the absorbing tower is at least one of the two absorbents such as active carbon or silicon, the active carbon's volume ratio is 0-50%, after absorbing, pressure, washing and desorption, the chlorine has a purity of more than 99.2%, the oxygen has a purity of more than 98.5% and the recovery rate of oxygen and chlorine is 98.5%.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for recovering oxygen and chlorine using pressure swing adsorption device.    Hydrochloric acid circulating pump (P1)    Vacuum pump (P2)    Absorption column (T1)    Drying column (T2)    Pressure tank. (VL)
NOVELTY - The system has a gasification furnace (1) whose combustible gas outlet is connected with gas inlet of cyclone dust removing separator (2). The gas outlet of cyclone dust removing separator is connected with gas inlet of fan (3) whose gas outlet is connected with gas inlet of gas storage tank (4). The oil groove (6) is connected with oil storage tank (7) and inlet of circulating pump (8). The outlet of circulating pump is connected with inlet of floating pipe coil heat exchanger (9) whose outlet is connected with a spray pipe inlet of cooling device (5).    USE - System for preparing liquid fuel from biomass such as straw, firewood, wooden meal, bamboo and agricultural wastes.    ADVANTAGE - The biomass liquid fuel preparation system can be used conveniently.    DETAILED DESCRIPTION - A pipeline is provided with a valve. Each joint is provided with a high temperature resistant sealing pad. The second gas outlet of gas storage tank is connected with gas inlet of cooling device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass liquid fuel preparation system.    Gasification furnace (1)    Cyclone dust removing separator (2)    Fan (3)    Gas storage tank (4)    Cooling device (5)    Oil groove (6)    Oil storage tank (7)    Circulating pump (8)    Heat exchanger (9)
NOVELTY - The device has a strengthening separating device provided with a shell. A cavity of the shell is provided with a rotary drum. An inner part of the drum is provided with a cylindrical rotary filler. A center part of an inner cavity of the shell is provided with a liquid distributor. The distributor is arranged at an inner ring of the drum. A lower part of the drum is provided with a rotating shaft. The shaft is connected with a lower end of the drum. A top part of the shell is provided with a liquid inlet, a gas outlet and a pressure meter. A water storage tank is connected with a gas inlet.    USE - Automatic back flushing filtering device for separating and removing solid dust and liquid fog drop in coke oven gas such as nitrogen gas, oxygen, hydrogen, methane, carbon monoxide, carbon dioxide and organic hydrocarbon (all claimed).    ADVANTAGE - The device has high separation precision. The device is easy to operate and safe and stable to use. The device improves solid dust and liquid fog removing efficiency in coke oven gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an automatic back flushing filtering device.
NOVELTY - A solar water electrolysis system comprises solar energy to electric energy. The electric energy decomposes water to generate hydrogen and oxygen, collecting, compressing, and storing.    USE - A solar electrolytic water system.    ADVANTAGE - The solar water electrolysis system is safe, has low consumption and no pollution, and circulates to generate hydrogen fuel and oxygen.
NOVELTY - Method of processing a cassava crop involves: separating the cassava into root, leaf and stem components; and processing the components to provide commercial products.    USE - In processing cassava crop for forming modified starch and starch derivatives; for forming feed for livestock, for extraction of vegetable protein, for forming biomass pellets; and in production of algal products such as biodiesel, omega 3 fatty oils, high protein stockfeed and biomass (claimed).    ADVANTAGE - The method provides recycled material and energy that can be re-used throughout the plant in order to reduce the environmental impact of the processing installation. The recycling process includes a waste water treatment plant, in which effluent from the processing of root components is treated to provide treated water, biogas and treatment sludge. The treated water may be then reused in any of the processing steps, e.g. processing of the root components, or utilized to irrigate a cassava crop which is to undergo processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an installation of processing a cassava crop involving: installation comprising mechanisms for separation of the cassava into root, leaf and stem components and devices for separate or combined processing of each of the components to provide commercial products.
NOVELTY - Compost waste, contaminated toxic waste of class I or II and organic waste or chemicals of biological class I and II inertization involves blending a mixture of animal waste and plant inoculants with microorganisms mixed compost (strains of fungi, bacteria and actinomycetes), pH adjusters and seeds of higher plants (legumes, grasses and crucifers). Chains of carbonic cellulose, hemicellulose, lignin and other organic chains of active ingredients are cleaved and transformed into non-contaminated compost or bio-fertilizer materials.    USE - Method for inertization of compost waste, contaminated toxic waste of class I or II and organic waste or chemicals of biological class I and II used as bio-fertilizer in agriculture field (claimed).
NOVELTY - A fatty acid alkyl esters preparing method involves adding a mixture of lower alcohol or lower alkyl alcohol and water in a liquefaction reactor by utilizing algae as a raw material according to a specific proportion. The mixture is reacted for 5-60 minutes at specific temperature, filtered, separated, and distilled after recycling solvent to obtain slurry with rich fatty acid ester liquid product. Fine fractionating of collected fatty acid carbon atom number is performed to different fatty acid ester composition.    USE - Method for preparing fatty acid alkyl esters by liquefying algae biomass.    ADVANTAGE - The method enables simplifying preparation process, recycling the solvent with low cost, and realizing industrial production.    DETAILED DESCRIPTION - A fatty acid alkyl esters preparing method involves adding a mixture of lower alcohol or lower alkyl alcohol and water in a liquefaction reactor by utilizing algae as a raw material according to a specific proportion, where the algae raw material, and the lower alcohol or low alkyl alcohol and the water are mixed at a mass ratio of 1:20 to 1:5, mixing ratio of the lower alkyl alcohol to water is 1: 0 to 1: 2, and liquid reaction temperature is 150-350 degrees C. The mixture is reacted for 5-60 minutes at specific temperature, filtered, separated, and distilled after recycling solvent to obtain slurry with rich fatty acid ester liquid product. Fine fractionating of collected fatty acid carbon atom number is performed to different fatty acid ester composition.
NOVELTY - Hydrogen is generated by hydrolyzing granular material obtained by press-molding hydrogenated magnesium.    USE - A generation method of hydrogen for fuel cell system (claimed).    ADVANTAGE - Hydrogen production rate is improved, and production of magnesium hydroxide membrane on the surface of magnesium hydride powder is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the principal part of the fuel cell system. (Drawing includes non-English language text).    Fuel cell system (1)    Hydrogen-producing apparatus (2)    Oxygen supply source (3)    Fuel cell (4)    Membrane electrode assembly (5)
NOVELTY - A complete-treatment process of wastewater and its apparatus involves introducing wastewater, activating microorganisms or chloroplast, decomposing or processing hardly decomposable chemical oxygen demand (COD), nitrogen bond material and phosphorus bond material, supplying dissolved oxygen using dissolved oxygen supply unit, making contact fixed bed contact the microorganisms, forming endless track electrode, and providing rotation suspension support rack stand which carries out rotation hanging suspension of endless track electrode.    USE - Complete-treatment process of wastewater and its apparatus for farming use.    ADVANTAGE - Wastewater is recycled. Fertilizer, biogas and manure are collected using surplus sludge or other introduction surplus sludge.    DETAILED DESCRIPTION - A complete-treatment process of wastewater and its apparatus involves introducing wastewater, activating microorganisms or chloroplast, decomposing or processing hardly decomposable chemical oxygen demand (COD), nitrogen bond material and phosphorus bond material, supplying dissolved oxygen using dissolved oxygen supply unit, making contact fixed bed contact the microorganisms, forming endless track electrode, providing rotation suspension support rack stand which carries out rotation hanging suspension of endless track electrode, providing rotation suspension support shaft which hangs suspension rotation, drive, electricity supply and insulation support of endless track electrode, carrying out rotation hanging suspension, cutting off iron reaction material membrane which carries out production adhesion in electricity supply surface, and connecting electricity supply unit to rotation suspension support shaft. An INDEPENDENT CLAIM is included for an amount reduction and processing and apparatus of surplus sludge.
NOVELTY - The method involves preparing a multilayer film that is laminated with a reinforcement film and a conveyance film, and an electrolytic membrane that is provided with a catalyst electrode layer (S110). An incision is provided in a boundary of an inner area set to the reinforcement film of the multilayer film, and an outer side area formed in an outer peripheral part of the inner area (S120). The multilayer film and the electrolytic membrane are bonded by thermo-compression (S130). The inner area of the two films is peeled from the laminated body of the electrolytic membrane (S140).    USE - Method for joining a reinforcement film on an electrolytic membrane during manufacturing of a fuel cell.    ADVANTAGE - The inner area of the reinforcement film and the conveyance film is peeled from the laminated body of the electrolytic membrane, so that the reinforcement film can easily affixed on the electrolytic membrane.    DETAILED DESCRIPTION - The reinforcement film is made of polyethylene naphthalate, and the polyethylene naphthalate is made of polyethylene terephthalate. An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of an electrolytic membrane and a reinforcement film joining method.'(Drawing includes non-English language text)'    Step for preparing multilayer film that is laminated with reinforcement film and conveyance film, and electrolytic membrane (S110)    Step for providing incision in boundary of inner area set to reinforcement film of multilayer film, and an outer side area formed in outer peripheral part of inner area (S120)    Step for bonding multilayer film and electrolytic membrane by thermo-compression (S130)    Step for peeling inner area of two films from the laminated body of electrolytic membrane (S140)
NOVELTY - The method involves preparing a diffused layer base material (S100), and coating a water-repellent paste to one side of the base material to form a porous layer while generating water-repelling gas (S200), when one side of the diffused layer base material is heated. The side of diffused layer base material is covered with a shielding film for shielding the water-repelling gas (S300). The diffused layer base material is heated with which paste coated in an assigned surface is covered with shielding film above gravitational direction (S400).    USE - Method for manufacturing a fuel cell i.e. polymer electrolyte fuel cell.    ADVANTAGE - The method enables heating the base material, thus effectively providing water-repellent property with respect to the diffused layer base material, and suppressing water retained in surroundings of the diffused layer base material.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing a fuel cell.'(Drawing includes non-English language text)'    Step for preparing diffused layer base material (S100)    Step for coating water-repellent paste to one side of base material to form porous layer (S200)    Step for covering side of diffused layer base material (S300)    Step for heating diffused layer base material with which paste is coated in assigned surface (S400)
NOVELTY - The device has a fluidized bed gasification furnace whose lower part is connected with an air inlet pipe. An upper part outlet of the fluidized bed gasification furnace is connected with a cyclone separator. The cyclone separator is connected with a dust remover through a pipeline. A spraying purifier is connected with an air storage tank that is connected to a boiler.    USE - Biomass gasification industrial boiler fuel gas combustion device for use by farmers.    ADVANTAGE - The device is reasonable in structure. The device reduces sulfur dioxide and oxynitride discharge gas boiler efficiency for purifying gasification solid emission. The device has low production cost, and avoids generation of pollution and enables replacing fossil fuel energy to the boiler.
NOVELTY - Producing (P1) biofuel from biomass that includes free monosaccharides, comprises: mixing (14) the biomass with a recycled hydrolyzate for a sufficient time to elute a portion of the free monosaccharides from the biomass, to form a sugar enriched hydrolyzate; separating (18) sugar enriched hydrolyzate from the biomass; and fermenting (24) monosaccharides in the separated sugar enriched hydrolyzate.    USE - The processes are useful for producing biofuel from biomass, where the biomass is sugarcane bagasse which is a byproduct from a sugar mill (all claimed) and the fuel is used for operating the plant.    ADVANTAGE - The processes: reduce the concentration of slag forming constituents in the biomass residue; and convert the biomass residue into a high value product.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing (P2) biofuel from biomass that includes free sugars, comprising mixing the biomass with a liquid solution until a substantial percentage of free sugars in the biomass are eluted into the liquid solution, where the biomass is mixed with the liquid solution prior to pretreating the biomass, separating liquid solution including free sugars from the biomass and fermenting free sugars in the separated liquid solution; and    (2) producing (P3) biofuel from biomass that includes free sugars, comprising mixing the biomass with a hydrolyzate prior to pretreating the biomass, allowing free sugars contained within the biomass to be eluted by the hydrolyzate, separating hydrolyzate including the eluted free sugars from the biomass and fermenting free sugars contained in the separated hydrolyzate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of process of producing biofuel from biomass.    Mixing (14)    Hydrolysis (16)    Separating (18)    Conditioning (22)    Fermenting (24)
NOVELTY - The composite membrane comprises a fibrous non-woven substrate comprising consolidated synthetic thermoplastic fibers. The composite membrane is coextensively disposed on a surface of the fibrous non-woven substrate. A continuous polysulfide rubber film is adhered to the substrate. The synthetic thermoplastic fibers comprise melt-blown fibers and electrospun fibers.    USE - The composite membrane is useful for separating a gas component including hydrogen sulfide and carbon dioxide from a mixed gas stream including hydrocarbon gas such as methane and combustion exhaust gas (all claimed).    ADVANTAGE - The composite membrane is capable of effectively separating the gas component from the mixed gas stream with excellent permeability, and has high surface area and mechanical strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for separating a gas component from a mixed gas stream.
NOVELTY - The furnace has a sealing furnace cover placed on a furnace end. A mixed fuel gas conveying pipe is connected with two ends of a low temperature mixed fuel gas chamber and a filter. A mixing gas filter reinforced plate is installed on the low temperature mixed fuel gas chamber. A lower part of a furnace waist is sleeved on an upper end of a furnace head. An upper part of the furnace waist is fixed with a fire-resistant layer to form a raw fuel gas mixing cavity. A lower end of an oxidization chamber is equipped with an air nozzle. The filter is connected with a lower end of a drain pipe.    USE - Circulation-type biomass fuel gas generating furnace.    ADVANTAGE - The furnace can remove tar content, and provides clean biomass fuel gas to a user, and has prolonged service life.
NOVELTY - An ionic-dissociation-substance-permeable film is a membranous substance having ion conductivity and electroconductivity, comprising an ion-exchange resin and an electron conductor. The film comprises a low-temperature dissociation catalyst of ionic dissociation substance in one surface, and a low-temperature recombination catalyst of ionic dissociation substance in the other surface.    USE - Film is used in apparatus used for purifying ionic dissociation substance (all claimed) e.g. purification of hydrogen in hydrogen fuel battery motor vehicles, refinery processing installations in hydrogen production, refinery processing installation of highly purified oxygen, and refinery processing installation which removes trace amount of oxygen from inert gas.    ADVANTAGE - The film exhibits excellent permeation function even at low temperature, and selectively permeates gas, such as oxygen and hydrogen. Since the film can be operated at a temperature lower than oxygen-gas-permeable film using ceramic material, the cost is reduced as energy for heat source is not required. The film has excellent deformation tolerance and chemical stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) purification of ionic dissociation substance; and    (2) purification apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the ionic-dissociation-substance-permeable film.    Membranous substance (1)    Ion-exchange resin (2)    Electron conductor (3)
NOVELTY - Method for removing biological phosphorus by activated sludge process, involves carrying out phosphorus discharge process in anaerobic tank and phosphorus uptake process in aerobic tank, supplying organic matter to the anaerobic tank when phosphorus releasing capability in the tank deteriorates, contacting electrode with water to be treated in anaerobic tank, and controlling electric potential to value lower than oxidation-reduction potential inside anaerobic tank and recovering the phosphorus discharge capability.    USE - The method is useful for removing biological phosphorus contained in water e.g. sewage.    ADVANTAGE - The method is reliable and cost-effective as compared to existing methodologies, and enables to recover and stabilize the phosphorus releasing ability in anaerobic tank as organic substance is suitably supplied to the tank.    DETAILED DESCRIPTION - Method for removing biological phosphorus by activated sludge process, involves carrying out phosphorus discharge process in anaerobic tank and phosphorus uptake process in aerobic tank, supplying organic matter of suitable quantity to the anaerobic tank when the phosphorus releasing capability in the anaerobic tank deteriorates, contacting electrode with water to be treated in the anaerobic tank, and controlling the electric potential to a value lower than the oxidation-reduction potential inside the anaerobic tank and recovering the phosphorus discharge capability in the anaerobic tank.
NOVELTY - The device has a gas generator connected with an atomizing processor. A circulating pump is connected with a circulating water inlet pipe, where a middle part of the circulating pump is provided with a gas inlet. An atomizing processor is arranged at a top part of an air outlet and a water opening. A side face of the atomizing processor is provided with a circulating spraying pipe and a spraying opening. A gas pipe is provided with a smoke exhaust valve. Another gas pipeline is arranged with the smoke adjusting valve. Circulating water is supplied to a water tank by utilizing the atomizing processor.    USE - Agriculture and forestry waste raw material gasification treatment device for use in a home.    ADVANTAGE - The device has wide practicability.
NOVELTY - The vessel case has an inner wall which is divided into two chambers. The inner wall is provided with an aperture for fluidly connecting the chambers. A lid with an inner wall is provided on the case. The outer walls of the lid chamber and lid inner partition wall are congruent with the outer walls of the vessel chamber and vessel inner partition wall and are fastened together to form chamber. A seal or gasket is provided between the connecting walls of the vessel lid and case, so as to form gaseous chamber which is fluidly connected to other chamber.    USE - Vessel case of hydrogen electrolyzer.    ADVANTAGE - Since the vessel is provided with fluidly connected chambers, the hydrogen electrolyzer are structurally and fluidly integrated with each other as single integral unit. Hence the space to install the device can be reduced and easier to utilize with various applications.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen electrolyzer.    External auto refill vessel (1)    Auto refill fluid pump (2)    Fluid flowing to pneumatic valve for auto refill (3)    LED strip (4)    Pneumatic valve (5)
NOVELTY - An ethanol production apparatus has reactor which processes organic waste pulp in subcritical water, discharge pipe which discharges to-be-processed object from the reactor, cooling device provided in the middle of the discharge pipe, and injects cooling water directly in the discharge pipe, and saccharification reaction apparatus which saccharifies to-be-processed object mixed with cooling water and enzyme.    USE - An ethanol production apparatus for producing ethanol using organic waste pulp (claimed).    ADVANTAGE - To-be-processed object processed within the reactor can be cooled in a short time after the reaction, processing without excessively decomposing cellulose is possible, reaction rate and glucose yield are significantly increased, purification of furfurals which inhibit fermentation reaction after saccharification is completely suppressed by suppressing excessive decomposition of cellulose, and only preservative is decomposed without excessively decomposing cellulose.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of organic waste pulp which involves processing organic waste pulp with subcritical water, and performing saccharification reaction of to-be-processed object using enzyme.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the subcritical water pre-processing which shows the glucose production from paper sludge, and influence of pH buffer solution concentration. (Drawing includes non-English language text).
NOVELTY - Circulating-type biopesticide production facility comprises unit which produces antimicrobial terpenes and antimicrobial lipopeptide as biopesticide, and woody biomass which is used for producing raw material for the unit.    USE - As circulating-type biopesticide production facility.    ADVANTAGE - The biopesticide production facility does not require microbial culture for producing biopesticide, hence reduces biopesticide production cost, and produces no environmental pollution. The chemical substance production facility reduces amount of industrial waste discharged from the biopesticide production facility.    DESCRIPTION OF DRAWING(S) - The drawing shows flow diagram illustrating the process of producing antimicrobial terpene in the circulating-type biopesticide production facility.
NOVELTY - The device has spaced rotary shafts on the bottom of chute, which are connected with a collecting plate whose one end is provided with a counter weight block. The rotary shaft and collecting plate are provided as ladder type in accordance with the order of lower to upper. The area of next lower collecting plate is larger than the area of upper closed collecting plate. The weight of counter weight block of next lower collecting plate is larger than the weight of upper counter weight block. The feeding port of chute is connected with drying chamber with horizontally arranged rotary chain.    USE - Energy-saving material driving device.    ADVANTAGE - The device can make full use of waste heat, so that large amount of energy can be saved turning the waste to treasure as well as protecting the environment. The device can produce fuel and take it as energy, and can perform recycling effectively.
NOVELTY - The device has a sludge conveying device which is connected with the feeding end of the stirrer. The stirrer is connected with a material conveying device. The conveying device is connected with forming device. The forming device is connected with a finished product conveying device. A feeding end of mixer is connected with stabilizing agent quantitative adding device. The sludge conveying device and the mixer are provided with sludge meter.    USE - Device for preparing combustion coal.    ADVANTAGE - The combustion coal preparing device has simple structure reasonable design, convenient operation and convenient to use. The combustion performance of the combustion coal preparing device can be improved. The usage amount of the coal powder can be minimized, thus the coal-saving effect can be enhanced. The resource utilization rate can be promoted. The time and cost required for preparing the combustion coal can be reduced.
NOVELTY - The method involves measuring temperature of a compost material. The ventilation amount with respect to the compost material of the unit quantity is determined based on the measured temperature of the compost material. The temperature of compost material is set in specific range. The center end temperature of compost material is measured. The moisture content of compost material is set in specific range. The air is uniformly supplied to the compost material.    USE - Manufacturing method of compost for livestock such as cow, noodles sheep and goat.    ADVANTAGE - The discharge amount of methane and nitrous oxide from compost material can be reduced, since ventilation amount with respect to compost material of the unit quantity is determined based on measured temperature of compost material. The electric power consumption of air blower can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost manufacturing apparatus has a determination unit that determines air volume of a ventilator based on the measured temperature of compost material. A control unit controls air volume of a ventilation flowing unit. The determination and control units are inverter control apparatus. The inverter control apparatus controls operation of ventilation flowing unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating the temperature change of composite material. (Drawing includes non-English language text)
NOVELTY - Preparing nutrient solution for plant cultivation, involves adding organic substance (0.05-1 g) to water (1 l), and constructing microbial ecosystem containing nitrifying bacteria by culturing the nitrifying bacteria under aerobic condition. The organic substance is chosen from corn steep liquor, manure, green manure, organic fermented fertilizer, fallen leaves, fish meal, oil cake, bean curd lees, organic refuse, rice bran, livestock excrement, and rice straw.    USE - The method is useful for preparing nutrient solution for cultivating plant by hydroponics method. The nutrient solution is useful for preparing liquid manure (all claimed). The plant includes ornamental plant, solanaceous plants e.g. tomato plant and eggplant, and lettuce.    DETAILED DESCRIPTION - Method for preparing nutrient solution for plant cultivation, involves adding organic substance (0.05-1 g) to water (1 l), and constructing microbial ecosystem containing nitrifying bacteria by culturing the nitrifying bacteria under aerobic condition. The organic substance is added to water, once in every seven days. The organic substance is chosen from corn steep liquor, manure, green manure, organic fermented fertilizer, fallen leaves, fish meal, oil cake, bean curd lees, organic refuse, rice bran, livestock excrement, and rice straw. The microbial ecosystem suppresses generation of ammonia which is an intermediate decomposition product. When corn steep liquor (66.67 mg) is added to water (1 l), the corn steep liquor decomposes into nitrate and nitrogen to produce nitric acid. An INDEPENDENT CLAIM is included for hydroponics method of a plant, which involves adding organic substance (1-5 g) directly to nutrient solution (1 l) for plant cultivation which is prepared by the above-mentioned method, where the nutrient solution comprises microbial ecosystem, and cultivating plant under aeration condition, where the organic substance is added nutrient solution, once in every 14 days.
NOVELTY - The invention relates to a plant and a process for recovering the slag resulting from coal burning process within an electric power plant. According to the invention, the claimed plant comprises a conveyer belt (1) with scrapers, a funnel (5) provided with a grate (7), a conveyer belt (8) with inclined scrapers, a temporary silage (4) having a capacity ranging between 10...15 m3, located at a height of 4...7 m, a batching-mixing device (3), a crusher (2) with an opening technological channel (6), a manual vane valve (9), a platform (10) for discharging the slag recovered from the boiler and for draining the water contained therein, and a facility (11) for storing fuels of caloric power higher than the slag, such as biomass as wood dust, coke powder or hard coal. The process claimed by the invention consists in taking over the slag before it is discharged into the technological channel (6) and passing it through a funnel (5) provided with a grate (7) for size screening, spreading it on an inclined conveyer belt (8) with scrapers to convey it up to a temporary silage (4), while the refuse from the grate (7) is manually charged into a mobile container and conveyed to a crusher (2), from the silage (4) the slag being charged into a motor vehicle trailer and transported to a concrete-lined platform (10) where the excess water is removed, and in the last stage the slag reaches a batching-mixing device (3) where it is mixed with fuels of higher caloric power.
NOVELTY - The dryer has a drying room (21) in which waste is injected through an inlet port. An exhaust duct (28) is installed in end of a drum (20) to discharge dry exhaust gas from the drying room. A hot air guide portion (60) is provided with a hot air fluid path in which a hot air distributor plate (45) with distribution holes (46) and a hot air supplying duct (40) are arranged. A lateral film (95) is arranged adjacent to the exhaust duct according to the columnar direction of the drum. Hot air is discharged through hot air distributor plate in spray direction.    USE - Dryer for drying domestic waste, household waste and industrial waste obtained from downtown area, house, industry and domestic waste center to produce solid fuel.    ADVANTAGE - The flying of waste from the drying room can be prevented. The domestic waste and household waste can be dried efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the dryer.    Drum (20)    Drying room (21)    Exhaust duct (28)    Hot air supplying duct (40)    Hot air distributor plate (45)    Distribution holes (46)    Hot air guide portion (60)    Lateral film (95)
NOVELTY - Producing 8-15C hydrocarbon involves: a) providing a ketone starting material; b) providing an aldol starting material comprising hydroxymethylfurfural; and c) mixing the ketone starting material and the aldol starting material in a reaction in the presence of a proline-containing catalyst and a solvent, where the solvent comprises water that is free of organic solvents, to produce 8-15C hydrocarbon.    USE - For producing 8-15C hydrocarbon (claimed) useful as trasportation fuels and surfactants.    ADVANTAGE - The method increases carbon chain length via the aldol reaction that utilizes reagents derived from biomass sources, is highly selective, can be performed at room temperature and does not require the use of an organic co-solvent, thus making the method more suitable for large-scale production with specificity; and utilizes additional catalyst that allow the aldol reaction to proceed under conditions suitable for large-scale use. The method increases carbon chain length by utilizing the aldol reaction that can be performed with catalysts, and which can be performed at room temperature using only water as the solvent, where the reaction utilizes dihydroxyacetone (DHA) (and other ketones or aldehydes) as ketone reagent and 5-(hydroxymethyl)furan-2-carbaldehyde (HMF) as the aldehyde reagent, which can be obtained from biomass cellulosics, and the reaction has high specificity and results in formation of 8-15C hydrocarbon, with a yield of 60%.
NOVELTY - The invention relates to a process for processing wood wastes and biomass and to an installation for applying the process. The claimed process consists in heating the starting material at a temperature of 400...500 degrees C thereby resulting a calcined material which is granulometrically classified, the coarse charcoal fraction being used as fuel and the fine fraction is treated and conditioned in order to be used as natural and neutralizing fertilizer for acidic soils. The claimed installation comprises inclined or vertical calcining columns (3), provided with fire-boxes (4), fixed on a shaft (5), the fuel necessary to heat and calcine is burned in a heating chamber (7), the resulting charcoal is removed by means of a conveyor (11), the exhaust gases, with a temperature of about 300 degrees C, being treated for recovering the heat energy.
NOVELTY - The pre-processing system has a landfill gas inlet which is connected with coarse filter. Condenser and blower are respectively connected together. A stage roots blower is connected with desulfurizing tower. Desulfurizing tower and regeneration tank are connected together by pipeline. A barren solution groove is formed on upper end of barren solution pump connected with desulfurizing tower. The top portions of desulfurization tower and multiple paths of pipeline are connected with landfill gas inlet and condenser. A buffer tank is connected with electric generating set.    USE - Pre-processing system for desulphurizing landfill gas.    ADVANTAGE - The desulphurization efficiency of landfill gas can be improved. The system can be operated safely and reliably and can be maintained conveniently. The operational cost of the system can be reeduced.
NOVELTY - A fermentation jar producing mixed alcohol by using straws includes a cylindrical main body and a supporting column. Lower end of the main body is provided with a discharging port and a sterile air inlet. The main tank body is internally provided with a spiral snakeshaped steel pipe, upper end of which is fixedly connected with water outlet, and lower end of which is let out and is fixedly connected with water inlet. The main tank body is provided with a cylindrical rotary cylinder sieve, the bottom of which is provided with a driving motor.    USE - Fermentation jar producing mixed alcohol by using straws.    ADVANTAGE - The device is capable of uniformly stirring, has high control precision of anaerobic fermentation temperature, and can realize continuous high-efficiency production.
NOVELTY - Marsh gas generating device capable of self-flowing and sand discharging comprises a marsh gas tank, an overflow weir, a marsh gas pipe, a window and a discharging pipe. The marsh gas tank main body is cylindrical. The bottom is a plane. Two feeding tubes are parallel to the center line. Two sand discharging pipes are set at the bottom of the marsh gas tank.    USE - A marsh gas generating device capable of self-flowing and sand discharging.    ADVANTAGE - Mud and sand in the methane tank can automatically flow and discharge under the self-flowing effect. The device has convenient and simple operation, no need of special sand discharging device and no need of power consumption, and is especially suitable for medium and small sized biogas engineering.
NOVELTY - Organic waste aerobic fermentation device comprises roller, rolling ring supporting device, driving device, transmission component, feeding device, tail gas recycling pipeline, condenser, fan, heater and gas distribution pipe through hole. The roller is provided on the rolling ring supporting device, which can be used as revolving motion of handle on the rolling ring supporting device. A front sealing cover is provided with a feeding device, where one end of the tail gas recycling pipe is connected with the sealing cover.    USE - Device for organic waste aerobic fermentation.    ADVANTAGE - The device is capable of recycling the tail gas to the roller to reduce the odor emission in the environment in the material fermentation cylinder and shortening the fermentation period. It can realize the harmless and recycling treatment of sludge, kitchen garbage and organic waste.
NOVELTY - The reactor has an automatic on-off valve (1) connected with a gasometer valve (2), a filter condensate separator (3), a compressor unit (4), a compressor check valve (5), an energy recovery heat exchanger (6) and a chilled water outlet (8). A pipeline check valve (10) is connected with a pressure reducing valve (11), a relief valve (12) and a manometer (14). A thermometer (15) is connected with a digital temperature indicator (17) for measuring temperature of the chilled water outlet. A gas analyzer is connected with a flow relief switch and a position transmitter.    USE - Anaerobic reactor for treating wastewater in a treatment plant.    ADVANTAGE - The reactor can analyze concentrations of methane, hydrogen sulfide and carbon dioxide gases in the wastewater so as to extract the biogas from the treatment plant in a safe manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of an anaerobic reactor.    Automatic on-off valve (1)    Gasometer valve (2)    Filter condensate separator (3)    Compressor unit (4)    Compressor check valve (5)    Energy recovery heat exchanger (6)    Chilled water outlet (8)    Pipeline check valve (10)    Pressure reducing valve (11)    Relief valve (12)    Manometer (14)    Thermometer (15)    Digital temperature indicator (17)
NOVELTY - High concentration wastewater treatment device comprises apparatus for production of microalgae, optical source for irradiating light, effluent feeding portion for supplying the effluent to growing bed, and growing bed in which the culture space is formed such that the microalgae is cultured in the growing bed.    USE - The device is used for wastewater treatment (claimed), producing microalgae used in biofuel production, and obtaining nitrous oxide generated during the treatment.    ADVANTAGE - The device enables high concentration wastewater treatment, and is suitable for mass production, and environmentally-friendly. The wastewater treatment can be performed indoor. The carbon dioxide generated during wastewater treatment is absorbed by the microalgae for photosynthesis, thus the device can reduce exhaustion of the greenhouse gas and prevent global warming.
NOVELTY - Organic fertilizer comprises potassium sulfate, monopotassium phosphate, urea, superphosphate, magnesium sulfate heptahydrate, zinc sulfate heptahydrate, sodium borate and elements comprising 22-24 wt.% of nitrogen, 11-12 wt.% of phosphorus, 11-12 wt.% of potassium, 0.6-1.2 wt.% of calcium, 0.7-1.4 wt.% of magnesium, 1.8-2.8 wt.% of sulfur, 0.8-0.1 wt.% of zinc and 0.18-0.2 wt.% of boron, where the organic fertilizer is based on organic fertilizer leaching solution.    USE - The organic fertilizer is useful for promoting growth of the grape.    ADVANTAGE - The organic fertilizer improves the yield and quality of the grape.
NOVELTY - Processing organic waste by adding organic waste through inlet port into storage tank provided with continuous stirred tank reactor, filling storage tank with water, subjecting the organic waste to microbial fermentation, adding microorganisms capable of performing hydrolysis, acid and methane fermentation, agitating organic waste, transferring organic waste from stirred tank reactor to anaerobic digester and raising water level of exhaust gas inlet when gas pressure reaches threshold, and dissociating generated scum and precipitating minerals in fermentation broth.    USE - The method is useful for processing organic waste.    DETAILED DESCRIPTION - Method for processing organic waste, involves (a) adding the organic waste through inlet port into storage tank provided with continuous stirred tank reactor, (b) filling the storage tank with water, subjecting the organic waste to microbial fermentation in the continuous stirred tank reactor and adding microorganisms capable of performing hydrolysis, acid fermentation and methane fermentation, (c) agitating upper surface of the organic waste, (d) transferring the organic waste from the stirred tank reactor to anaerobic digester and raising water level of exhaust gas inlet when pressure of gas inside the reactor reaches threshold, (e) dissociating generated scum in fermentation broth inside the anaerobic digester, and (f) precipitating minerals present in the fermentation broth, where when gas pressure does not reaches threshold value then the control unit present in the treatment apparatus compresses gas through gas-injection nozzle equipped with the reactor.
NOVELTY - Cigarette organic fertilizer comprises straw (1000 parts by weight (pbw)) containing water (55-65 pbw), oil cake (5.25-45 pbw) and fungicide (0.035-1.35 pbw).    USE - Used as cigarette organic fertilizer.    ADVANTAGE - The organic fertilizer is cost effective, and has superior tobacco proportion and medium smoke proportion (0.2 Yuan/kg, 1.5% and 4%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cigarette organic fertilizer comprising: crushing the straw into the length for 3-5 centimeter; soaking the straw with the water or drenching with the water, making the relative water content of the straw for 55-65%: fully and uniformly mixing the fungicide and oil cake according to the corresponding proportion, producing viable organism powder, regulating the viable organism powder moisture, paying a layer straw and scattering a layer water viable organism powder in the selected manure area to stack forming using recursive device, covering the plastic cloth outside the pile article of stacking forming, where the thickness of each straw layer is 40-50 cm and the thickness of viable organism powder is 0.4-0.6 cm; piling up for 7-10 days and digging up and turning one time, repeating 3 times till the fermentation finishes, manufacturing the organic fertilizer, where the standard of the manufactured organic fertilizer is the fermented organic fertilizer, which is tawny or taupe, not stink and has light ammonia taste.
NOVELTY - Sludge compost comprises (pts.wt.) sludge (2-6), plant ash (0.5-1.5), straw powder (0.1-0.3), mushroom slag (0.5-1.5), chicken manure (0.5-1.5), and leavening agent (0.5-1.5).    USE - Sludge compost used as organic fertilizer.    ADVANTAGE - The sludge compost has low cost and less pollution to environment. It has reduced sludge dehydration treatment cost and has accelerated sludge fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sludge compost by dehydrating and mixing sludge with plant ash; stacking for 15 days, in which plant ash breaks cell wall and removes water contained in sludge; mixing treated sludge, straw powder, mushroom slag and chicken manure; fermenting under high temperature; turning over pile; and inletting oxygen everyday for 20 days to finish fermentation.
NOVELTY - The device has an alcohol feed distributor that enters into kettle main portion from the lower end of the kettle main portion. A stirring component is provided with a water wing type axial flow stirring paddle. A heat exchanger is connected with the lower end of the alcohol feed distributor.    USE - Bio-diesel esterification reaction device.    ADVANTAGE - The contact area of the reaction material and the alcohol feed distributor is increased, thus the homogeneous phase esterification reaction is performed by the bio-diesel esterification reaction device efficiently and rapidly. The reaction energy consumption is reduced by the bio-diesel esterification reaction device. The reactant is completely utilized in the reaction device. Since the alcohol is recovered during non-reaction state of the reaction device, the consumption of the alcohol is reduced. The reaction material is stirred by the reaction device uniformly, thus the partial over-heat caused by the esterification reaction in the carbon atmosphere is avoided. The temperature of the reaction device is controlled conveniently.
NOVELTY - The system has a dryer (200) that receives the material which is crushed through a crusher (100). The percentage of water content of the crushed material is measured and the cell is loaded. The building has fixed percentage of water content which is dried through the dryer and molded to the rolling press. A portion of the pellet type solid fuel is recycled to the cooling through the molder (300) and the energy source which is dried heats up the dryer.    USE - Bio solid fuel manufacturing system.    ADVANTAGE - The combustion efficiency can be improved. The manufacturing cost of the bio solid fuel can be reduced. The process efficiency is improved. The bio solid fuel manufacturing system is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the bio solid fuel manufacturing system. (Drawing includes non-English language text)    Crusher (100)    Dryer (200)    Molder (300)
NOVELTY - A rolling wheel is connected with a chain wheel. A speed reducing motor is connected with a driving chain wheel. A fermenting and drying assembly is placed in a rotating multi-functional shaft. A waste exhaust outlet is connected with a high frequency impulse dust-removing deodorizing device. A vent-pipe is connected with fermenting and drying assembly. An infrared temperature probe is arranged in the fermentation drying assembly of the housing. A certain space is formed on side portion of a heat preservation plate.    USE - Multifunctional solar biochemical treatment system used for treating organic kitchen wastes.    ADVANTAGE - The energy consumption of the multifunctional solar biochemical treatment system can be reduced. The efficiency and environment-friendly effect of the multifunctional solar biochemical treatment system can be improved.    DETAILED DESCRIPTION - The driving chain wheel is connected with a loudspeaker opening-shaped sealing opening end unit. A connecting flange is arranged in the rotary connecting unit. A fermentation drying chamber is arranged on the inner wall of vertical hollow stirring plate. A fluid inlet and outlet is extended out of the ferment drying chamber.
NOVELTY - A transition metal carbide catalyst (I) is used in hydrodeoxygenation of biomass oil by loading the catalyst (I) into a reaction pipe under hydrogen gas atmosphere; and introducing the biomass oil continuously into the reaction pipe via a high pressure liquid pump based on a hydrogen-to-oil ratio of 800-1600 and a liquid hourly space velocity (LHSV) of 1-4/hour to carry out biomass oil hydrogenation refining process at 1-10 MPa and 200-500 degrees C, cooling the product via a cold trap, and then collecting the product via a liquid collector.    USE - Transition metal carbide catalyst (I) used in hydrodeoxygenation of biomass oil (claimed).    ADVANTAGE - The transition metal carbide (I) has low cost, high catalytic activity and good stability, and is suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of transition metal carbide catalyst (I), comprising (A) impregnating a carrier in an aqueous solution containing an active metal component, drying to a constant weight at 100-125 degrees C, roasting at 500-650 degrees C for 5-6 hours to obtain a load type catalyst; and (B) placing the load type catalyst in a stainless steel reaction tube, introducing methane gas (CH4) and hydrogen gas (H2) at a volume ratio of (1-3):(9-7) into the reaction tube, and carrying out a temperature-programmed carbidization process to obtain active transition metal carbide catalyst (I).
NOVELTY - Biolipid production of solid fuel comprises heating raw materials at more than 100 degrees C; precipitating; taking out oil; putting prepared oil into reaction tank; heating at more than 50 degrees C; adding 3-5% methanol and reacting for 1 hour; adding 2-3% acid; continuously reacting for 3 hours; adjusting pH at 7.5-8; adding grease into deposition cone tank; reducing temperature at 30 degrees C; discharging impurity; adding straw processing grain or 200-500 mm straws into grease at ratio of 90-95% straw and 5-10% grease; pressurizing at 15-25 MPa; heating; and shaping.    USE - Biolipid production of solid fuel.    DETAILED DESCRIPTION - Biolipid production of solid fuel comprises heating raw materials at more than 100 degrees C; precipitating; taking out oil; putting prepared oil into reaction tank with stirrer; heating at more than 50 degrees C; adding 3-5% methanol and reacting for 1 hour; adding 2-3% acid; continuously reacting for 3 hours; adjusting pH at 7.5-8; adding grease into deposition cone tank; reducing temperature at 30 degrees C; discharging impurity; taking straw processing grain or 200-500 mm straws; adding into grease at ratio of 90-95% straw and 5-10% grease; putting them into pressure vessel at 15-25 MPa; heating using heat that can be selected according to spray oil or pressure; and shaping.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for biolipid production of solid fuel (Drawing includes non-English language text).
NOVELTY - Preparing biodiesel by catalytic grease combining phospholipase with lipase, where it combines the phospholipase with lipase as catalyst to catalyze the reaction of grease containing phospholipid and short chain alcohol to prepare biodiesel.    USE - The method is used for preparing biodiesel (claimed).    ADVANTAGE - The method above not only eliminates the side effect of phospholipid to phospholipase, but also improves the quality of the biodiesel. The method is simple, convenient to perform, and environment-friendly. The phospholipid is fully reacted, the yield rate of the biodiesel is high, and the separating effect is good. The method is especially suitable for grease containing high content of phospholipid, and provides possible development and usage of cheap greases in the biodiesel field.
NOVELTY - The palladium carbon catalyst comprises 0.7-1 mass% of active component i.e. metal palladium, 0.1-0.8 mass% of metal assistant agent i.e. metal barium, and carrier i.e. active carbon.    USE - The palladium carbon catalyst is useful for producing chloroacetic acid, which is useful as an organic synthetic raw material in preparation of pesticides, pharmaceuticals, dyes, carboxymethyl cellulose (CMC), spices and other organic reaction intermediates.    ADVANTAGE - The catalyst has good repeatability, high dispersion of carrier on the nano metal particle, high activity and selectivity and prolonged service life, and is capable selectively hydrogenating and dechlorinating to prepare high-purity chloroacetic acid in a cost-effective and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the palladium carbon catalyst.
NOVELTY - Preparation of 6-chlorohexanal comprises mixing 6-chlorohexanol, trichloroisocyanuric acid (TCCA), (2,2,6,6-tetramethylpiperidin-1-yl)oxyl (TEMPO), and sodium bicarbonate.    USE - Method for the preparation of 6-chlorohexanal (claimed) for preparing cystatin intermediates used as a renal dehydropeptidase inhibitor.    ADVANTAGE - The method has high yield and simple operation, and is environment-friendly.
NOVELTY - Cleaning agent comprises oil-degrading microbial inoculum.    USE - The agent is useful for bioremediation of sewage (claimed).    ADVANTAGE - The agent reduces energy consumption, has excellent stability and high efficiency, and does not cause secondary pollution.
NOVELTY - The cleaner has an underwater plasma processing apparatus generating internal air in an inner side of a pall ring (40). A suction fan (20) is provided with an air supply flow route (12) for inhaling external air and guiding flow direction of the external air in the pall ring. An air discharge path (14) guides the external air exhausted to an outer side. A lower water tank (33) is positioned at a lower side of the pall ring by a lift pump (37). A pressure controlling device maintains pressure of internal air of the underwater plasma processing apparatus.    USE - Wet-type air cleaner.    ADVANTAGE - The cleaner prevents flying of water particle and exhaustion of moisture and minimizes gas leak of a by-product material i.e. ozone, generated by plasma.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a wet-type air cleaner.    Air supply flow route (12)    Air discharge path (14)    Suction fan (20)    Lower water tank (33)    Lift pump (37)    Pall ring (40)
NOVELTY - The method of manufacturing organic fertilizer using organic sludge, comprises preparing 25-50 wt.% of organic fermentation material and 50-80 wt.% of sludge filter cake with water (30-40 wt.%), mixing the resulting slurry with organic fermentation microbial inoculum and auxiliary material and then conveying to a belt (2) to ferment auxiliary material mixture, mixing and fermenting the auxiliary material mixture and sludge filter cake and then mixing to a fermentation tank (6) under a normal temperature for 6-10 days, where the thickness of the organic fermentation material is 15 mm.    USE - The method is useful for manufacturing organic fertilizer. No biological data given.    ADVANTAGE - The method is capable of economically and energy efficiently manufacturing the organic fertilizer in an environmental friendly manner.    DETAILED DESCRIPTION - The method of manufacturing organic fertilizer using organic sludge, comprises preparing 25-50 wt.% of organic fermentation material and 50-80 wt.% of sludge filter cake with water (30-40 wt.%), mixing the resulting slurry with organic fermentation microbial inoculum and auxiliary material and then conveying to a belt (2) to ferment auxiliary material mixture, mixing and fermenting the auxiliary material mixture and sludge filter cake and then mixing to a fermentation tank (6) under a normal temperature for 6-10 days, where the thickness of the organic fermentation material is 15 mm. The organic fermentation material includes slag, mushroom, or Flammulina residue. The microbial inoculum comprises photosynthetic bacteria, nitrogen fixation spore bacteria, phosphorus bacteria,Lactobacillus and microzyme. An INDEPENDENT CLAIM is included for a device for manufacturing organic fertilizer using organic sludge.
NOVELTY - Synthesizing methanol, involves adjusting content of carbon dioxide in raw gas for synthesizing methanol to control the exothermal intensity of a reaction for synthesizing methanol, performing catalytic reaction of raw gas carbon monoxide, carbon dioxide and hydrogen, and subjecting the un-reacted carbon monoxide, carbon dioxide and hydrogen to gas-liquid separation process.    USE - The method is useful for synthesizing methanol.    ADVANTAGE - The method is cost-effective, achieves full circulation of carbon monoxide, carbon dioxide and hydrogen, reduces loss of heat and non-renewable resources, and optimizes methanol production.    DETAILED DESCRIPTION - Method for synthesizing methanol by full circulation of carbon monoxide, carbon dioxide and hydrogen, involves adjusting content of carbon dioxide in raw gas for synthesizing methanol to control the exothermal intensity of a reaction for synthesizing methanol, where the heat released by the synthesis reaction is matched with heat transfer of a methanol synthesis tower, and the molar percentage concentration of carbon dioxide in synthesis gas is 10.0-20.5%, performing catalytic reaction of raw gas carbon monoxide, carbon dioxide and hydrogen, and subjecting the un-reacted carbon monoxide, carbon dioxide and hydrogen to gas-liquid separation process, where the proportion of carbon monoxide, carbon dioxide and hydrogen in fresh gas is adjusted, hence synthesis gas entering the synthesis tower has the ratio of (hydrogen to carbon) 2-2.80.
NOVELTY - A waste gas generated in wastewater is recycled by dusting waste gas; performing gas-liquid separation for the gas as filtration regeneration fuel material and boiler fuel; and performing separation of oil-water for tar- water.    USE - Method for the recycle of waste gas generated in wastewater (claimed).    ADVANTAGE - The method not only avoids air pollution caused by harmful gas, but also save energy.
NOVELTY - A fuel electrode side diffusion barrier layer producing method involves preparing a metal substrate in which one side of the metal substrate is formed with an anode diffusion prevention layer. An anode layer is formed on top of the anode diffusion prevention layer. A solid electrolyte layer is formed on the top of the anode layer. Optionally, top of the solid electrolyte layer is provided with interfacial reaction prevention layer to form a cathode. A cathode layer is formed on top of the solid electrolyte layer or the interfacial reaction prevention layer.    USE - Method for producing fuel electrode side diffusion barrier layer for solid oxide fuel cell.    ADVANTAGE - The method enables producing fuel electrode side diffusion barrier layer with better intensity and flexibility and improved mechanical reliability, in a simple, easy and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an aerosol injection device for producing fuel electrode side diffusion barrier layer of a solid oxide fuel cell.
NOVELTY - Preparation of ethylene cracking material comprises utilizing heat insulation reactor, filling noble metal hydrogenation refined catalyst with reactor, and mixing fresh liquefied petroleum gas with particularly circulated hydrogenated product to enter reactor, with weight ratio of particularly circulated hydrogenated product and fresh liquefied petroleum gas of 1:1-5:1, and inlet temperature of reactor at 70-140 degrees C.    USE - Method of preparation of ethylene cracking material (claimed).    ADVANTAGE - The method hydrogenates industrial C4 fraction to ethylene cracking material having high mass; and overcomes industrial C4 fraction hydrogenation having large heat release amount and easy coked catalyst.
NOVELTY - Invention relates to the wood processing industry and can be used for production of charcoal out of lump wood and its wastes. Through the metering loader 15 the woody biomass is loaded into the drying zone 2 of the vertical retort 1, where it is dried and heated. Furnace gases in the form of steam gas mixture are removed from the drying zone 2 to the capacitor 16. The woody biomass passes from the drying zone 2 through the drum feeder 25 to the pyrolysis zone 3. In the pyrolysis zone 3 pyrogas is released, and coal is formed. Formed pyrogas is discharged from the pyrolysis zone 3 to the separation unit 12. The residual pyrogas are guided from the separation unit 12 to the furnace 9, where it is burnt. The coal formed in the pyrolysis zone 3 comes through the drum feeder 26 to the cooling zone 4.    USE - Woodworking industry.    ADVANTAGE - Invention enables to improve the efficiency of the pyrolysis process. 2 dwg
NOVELTY - The furnace has a cone-shaped cracking chamber arranged in a furnace body. The furnace body and the combustion chamber are provided with an interlayer. An air inlet opening is arranged on an outer wall of the furnace body. A feeding opening is formed on an upper end of the furnace body. An ash cleaning door is arranged at a lower part of the furnace body. An upper end of the cracking chamber is provided with an emergency discharging device. The outer wall of the furnace body is provided with a vent hole.    USE - Biomass fuel combustion furnace.    ADVANTAGE - The furnace has large contact area, and reduces heat energy consumption and tar so as to improve burn-off rate.
NOVELTY - The furnace has a fuel bin provided with a smoke outlet opening. An upper part of an outer cylinder is provided with an annular sealing groove. The annular sealing groove is provided with a sealing medium. An upper part cover is provided with a sealing ring. The sealing ring is inserted into the annular sealing groove. The smoke outlet opening is connected with a tar collecting chamber. The tar collecting chamber is provided with a radiating fin, a fuel gas pipe and an oil return opening that is connected with the fuel bin.    USE - Environment-friendly combustible household rubbish and biomass fuel using tar processing gasification furnace.    ADVANTAGE - The furnace is energy-saving and environment-friendly, and has wide application range. The furnace does not generate harmful gas and ensures complete tar processing.
NOVELTY - The device has an aquatic plant unit that is provided with conductive material for fixing the aquatic plants. An artificial medium unit is provided with carbon artificial medium for enriching a large amount of microorganisms for forming an efficient biomembrane purifying area. The conductive material is led out to the device by a guide wire for forming an air cathode of the microbial fuel cell. The nano-active carbon particles are evenly sprayed onto the surface of the nano-active carbon artificial medium for synthesizing an anode of the microbial fuel cell.    USE - Combined ecological floating bed device for purifying lake water.    ADVANTAGE - The quality of the water can be improved. The purification process can be ensured.
NOVELTY - Electric heating furnace comprises thermocouple, electric heating element, roller, loading plate, furnace body, furnace door, sealing bricks, loading plate auxiliary bricks, exhaust gas pipeline and tail gas collecting device. The inside of furnace door is sealed and composed by sealing bricks. The furnace bottom inside the furnace body is horizontally placed with rollers. The furnace door is provided with an observation hole, the central part of the furnace tail is provided with small hole for placing the thermocouple.    USE - Electric heating furnace for pyrolysis biomass material.    ADVANTAGE - The pyrolysis of biomass can be realized through controlling the delivery of roller bottom by program, and the bottom is designed into a roller capable of moving back and forth, making the temperature of pyrolysis more uniform. The mode structure of the design is simpler than achieving biomass pyrolysis by gradual boost of motor. The pyrolysis is also more uniform and controllable, and because the tightness is better, the furnace is more energy saving. The furnace has simple structure, good association of activity and inertia, and low production cost.
NOVELTY - Biomass gasification device comprises a feed mechanism, a gasification furnace and a gasification medium supply mechanism. The discharge port of the feed mechanism is connected with the raw material inlet of gasification furnace. The gas outlet of the gasification medium supply mechanism is connected with the gasification medium entrance of the gasification furnace. The gasification medium supply mechanism comprises a water vapor generator and an air compressor.    USE - Biomass gasification device.    ADVANTAGE - The device uses air and water vapor as gasification medium, can combine plasma torch and high temperature heat source, and can control the temperature field of each reaction area in the gasification furnace through the proportion of reasonable allocation with air and water vapor, and build the best oxidation, deoxidation, pyrolysis and drying environment, and ensures that the gasification process is rapid and efficient.
NOVELTY - The method involves subjecting an optionally pretreated biomass to torrefaction to produce a torrefied material and torrefaction gases. The torrefied material is cooled. The portion of cooled torrefied material is mixed with the torrefaction gases such that torrefaction gas components are condensed on the torrefied material.    USE - Method for cooling torrefied material.    ADVANTAGE - The energy yield of torrefied material can be improved. The hydrophobic of the torrefied product can be improved. The clogging of cooling device can be decreased.    DETAILED DESCRIPTION - The torrefied material is transferred through a cooled drum. The temperature of torrefied material is set less than 100 degrees C. The compacted material is separated by a sieve. The biomass is dried and heated. A torrefaction reactor (2) is provided for converting pretreated biomass to torrefied material and torrefaction gases. An inlet (21) is connected to outlet (25) of torrefaction reactor. A mixing zone is provided between inlet and outlet of torrefaction reactor. The compacted torrefied material is separated from non-compacted torrefied material. An INDEPENDENT CLAIM is included for system for cooling torrefied material.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional views of the torrefaction reactor.    Torrefaction reactor (2)    Inlet (21)    Outlet (25)    Torrefaction zones (29,32)    Torrefaction zone cooling media outlet (34)
NOVELTY - Preheated biomass is subjected to torrefaction to produce torrefied gases and a torrefied material at more than 220 degrees C. Water is added to the torrefied material to reduce temperature not below 120 degrees C, preferably not below 190 degrees C. The torrefied material and portion of torrefaction gases are cooled in a common cooling device to condense the components of torrefaction gases.    USE - Torrefaction of biomass e.g. lignocellulosic biomass, such as wood chips (claimed).    ADVANTAGE - The torrification method efficiently provides torrefied product having high hydrophobicity and energy yield, with reduced clogging of cooling device. The energy density of biomass fuel is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for torrefied material-cooling system.    DESCRIPTION OF DRAWING(S) - The drawings show a schematic view of torrefaction arrangement.    Biomass inlet (21)    Feeding screw (22)    Drying zone (23)    Heating zone (26)    Primary torrefaction zone (29)
NOVELTY - Torrefaction of biomass and combustion of generated gases, comprises: (a) drying biomass having an average moisture content of at least 20%, such as at least 25% (w/w) to obtain a dried biomass having an average moisture content of 3-15% (w/w) and a first gas product; (b) further drying the biomass from step (a) to obtain a dry biomass and a second gas product; (c) heating and torrefying the biomass from step (b) to obtain torrefied material and a third gas product; and (d) collectively combusting of the second and the third gas product without the first gas product.    USE - The method or system is useful for torrefaction of biomass and combustion of generated gases (claimed).    ADVANTAGE - The invention provides an improvement of the energy efficiency in a torrefaction process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a system for torrefaction of biomass and combustion of generated gases, comprising a first zone for drying biomass, said first zone having a biomass inlet, a gas outlet and a dried biomass outlet; at least one additional zone for further drying, heating and torrefying the dried biomass from the first zone, said at least one additional zone having an inlet connected to the dried biomass outlet of the first drying zone and at least one gas outlet; and a gas combustion chamber being connected to receive gases from the at least one gas outlet of the at least one additional zone but not from the gas outlet of the first zone.
NOVELTY - Method for processing organic waste, involves fermenting organic matter to obtain compost, incinerating the compost, absorbing alkaline fermentation gas emitted from the composting step in water to obtain fermentation gas dissolved solution, causing acid combustion gas resulting from the combustion step to react with fermentation gas dissolved solution to obtain combustion gas dissolved solution, and causing the combustion gas dissolved solution to react with the fermentation gas.    USE - The method and apparatus are useful for processing organic waste (all claimed) which is used for process of sewage sludge, foodstuff waste material, domestic-use organic refuse, livestock farming waste material, agricultural waste and fishery waste material.    ADVANTAGE - The method and system in which fermentation gas results from composting and combustion gas that results from burning compost can be processed together at one time and countermeasures for dealing with odors and desulfurization can be achieved effectively and efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing system of organic waste, which comprises composting apparatus which ferments organic waste to obtain compost, combustion furnace which burns the compost, fermentation gas treatment column which makes water absorb the alkaline fermentation gas emitted with composting apparatus and obtain fermentation gas dissolved liquid, combustion gas treatment column which makes acidic combustion gas emitted with the combustion furnace react with the fermentation gas dissolved liquid, and obtains combustion gas dissolved liquid, fermentation gas dissolved liquid supply part which supplies the fermentation gas dissolved liquid to combustion gas treatment column, and combustion gas dissolved liquid supply part which supplies the combustion gas dissolved liquid to fermentation gas treatment column.
NOVELTY - Treating a lignocellulosic feedstock comprising e.g. lignin to produce a sugar rich process stream, comprises (a) subjecting the feedstock to a first enzymatic hydrolysis to preferentially solubilize xylose and obtaining an effluent stream, (b) subjecting the effluent stream to a second enzymatic hydrolysis to preferentially solubilize cellulose and obtaining a sugar rich process stream, (c) treating the effluent stream and sugar rich process stream to recover enzymes, and (d) fermenting the sugar rich process stream.    USE - The sugar rich process stream is useful: for producing sugar derived products and producing alcohol through fermentation; as a fuel source for several products or other polymeric materials.    ADVANTAGE - The process ensures recovering and recycling of the enzymes used in each stage of the enzymatic process thus rapidly increasing the yield of alcohol in an economical manner.    DETAILED DESCRIPTION - Treating a lignocellulosic feedstock comprising cellulose, hemicellulose and lignin to produce a sugar rich process stream, comprises (a) subjecting the feedstock to a first enzymatic hydrolysis to preferentially solubilize xylose and obtaining an effluent stream, (b) subjecting the effluent stream to a second enzymatic hydrolysis to preferentially solubilize cellulose and obtaining a sugar rich process stream, (c) treating at least one of the effluent stream and the sugar rich process stream to recover enzymes utilized in at least one of (i) the first enzymatic hydrolysis and obtaining a first recovered enzyme stream, and (ii) the second enzymatic hydrolysis and obtaining a second recovered enzyme stream, where at least some of the first recovered enzyme stream is recycled to the second enzymatic hydrolysis or at least some of the second recovered enzyme stream is recycled to the first enzymatic hydrolysis, and (d) fermenting the sugar rich process stream.
NOVELTY - The gasifier has a vertical chamber (1) and a horizontal chamber (3) arranged in shape of L, where the vertical chamber receives products to be treated through an upper part via an air lock (2). Drying and pyrolysis operations are performed in the vertical chamber. Combustion operations of a portion of load and gasification operations are performed in the horizontal chamber. The horizontal chamber is equipped with a push rod (4) assuring progression of the load on a bottom (5) to solid residue discharge wells (6).    USE - Reversible fixed bed-type gasifier for producing combustible synthesis gas from solid residues e.g. biomass, wood and product for supplying the gas to burners of oven or boiler, engines and gas turbine so as to produce heat or electricity. Can also be used for a fluidized bed gasifier and circulating bed gasifier.    ADVANTAGE - The gasifier can be operated continuously either with parallel flow or with counter-flow based on quantities and characteristics of the products to be treated by enabling planned use of synthesis gas generated by the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a front schematic sectional view of a reversible fixed bed type gasifier.    Vertical chamber (1)    Air lock (2)    Horizontal chamber (3)    Push rod (4)    Bottom (5)    Solid residue discharge wells (6)
NOVELTY - The apparatus (12) has a gasification process part (4) in which a volatile component (6) is obtained by thermally decomposing a mixed raw material of biomass, where the apparatus calculates composition of reaction product gas of a gasification reaction to supply a gasifying agent in a gaseous-phase state. Value of production amount for chemical species is computed by a measured value regarding supply amount of each raw material. An elementary process type group includes an herbal elementary process type group corresponding to an herbal biomass e.g. bagasse, chaff and rice straw.    USE - Reaction simulation apparatus for a gasifier (claimed).    ADVANTAGE - The apparatus automatically sets supply amount of appropriate gasifying agent, performs exact gasification reaction, attains driving of a highly efficient gasifier and easily determines appropriate supply amount of the gasifying agent corresponding to the mixed raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gasifier.'(Drawing includes non-English language text)'    Gasifier (1)    Pyrolytic process part (2)    Communication part (3)    Gasification process part (4)    Volatile component (6)    Reaction simulation apparatus (12)
NOVELTY - The biogas purifier (2) has digestive liquid storage tank (3) which stores digestive liquid after methane fermentation process from methane fermentation tank (1). A digestive liquid discharge port (42) is provided at upper or lower portions of main structure. The biogas purification tank (4) has air-bubble-forming unit (43a) which performs gas bubble formation of biogas introduced from biogas inlet (43). The liquid is circulated between liquid storage tank and purification tanks, to purify biogas. The diameter of bubble generated by gas-bubble-formation unit is 300 mu m-3 mm.    USE - Biogas purifier for use in system for production of biogas using organic refuse, livestock excrement, sewage-treatment sludge, purification-tank sludge, etc.    ADVANTAGE - The stability over time of the methane concentration in purification biogas is improved, so that energy saving effect of the biogas purifier is achieved.    DETAILED DESCRIPTION - The range of concentration of digestive liquid inside biogas purification tank is set about 5000-40000 mg/L. An oxygen supply inside the biogas purification tank is cut off. Both the digestive liquid inflow port and digestive liquid discharge port are positioned in biogas purification tank. The digestive liquid discharge port and digestive liquid inflow port are positioned above the main structure. A digestive liquid discharge port is positioned downward to main structure. The digestive liquid is circulated between digestive liquid storage tank and biogas purification tanks according to digestive liquid circulation force.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production system. (Drawing includes non-English language text)    Methane fermentation tank (1)    Biogas purifier (2)    Digestive liquid storage tank (3)    Biogas purification tank (4)    Digestive liquid inflow port (41)    Digestive liquid discharge port (42)    Biogas inlet (43)    Gas-bubble-formation unit (43a)
NOVELTY - A composite material (31) comprises ceramic-coated particles whose surface of core made of metal which catalyzes ionization of oxygen is covered with porous ceramic. The ceramic-coated particles contain perovskite-type oxide (I).    USE - Composite material is used for forming cathode of solid oxide fuel cell for manufacture of solid oxide fuel cell system (all claimed).    ADVANTAGE - The cathode formed using the composite material does not deteriorate easily even at high temperature.    DETAILED DESCRIPTION - A composite material comprises ceramic-coated particles whose surface of core made of metal which catalyzes ionization of oxygen is covered with porous ceramic. The ceramic-coated particles contain perovskite-type oxide of formula: (Ln1-xAex)(M11-yM2y)O3-d (I).    Ln=lanthanoid;    Ae=Sr, Ba or Ca;    M1=Co or Mn;    M2=Fe, Ti, Ni, Al, Zr, Ga, Mg, Cu, In, Sn, V, Cr, Zn, Ge, Sc or Y;    x.y=0 to less than 1;and    d=neutral electric charge value.    INDEPENDENT CLAIMS are included for the following:    (1) solid-oxide fuel cell, which comprises an anode (10), a solid electrolyte (20), and a cathode (30) formed using composite material; and    (2) manufacture of solid oxide fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of solid oxide fuel cell system. (Drawing includes non-English language text)    Anode (10)    Solid electrolyte (20)    Composite material (31)    Junction portion (40)    Bonding (41)
NOVELTY - The biomass gasification system has an up-draft gasifier (4) with an outlet (15) at the top end (12) to discharge gasifier product gas. A pipe (5) is declined from the up-draft gasifier to a combustion unit to transport fractions of tar in the gasifier product gas towards the combustion unit and preferred into the combustion unit. The combustion unit heats a transfer medium. The pipe transports the gasifier product gas from the outlet of the up-draft gasifier to the inlet of the combustion unit.    USE - Biomass gasification system used for Stirling plant (claimed) to generate gasifier product gas to be burned in combustion unit.    ADVANTAGE - Avoids damage to internal combustion engine. Ensures effective way to cope with dust and tar residues from gasifier product gas before burning. Reduces amount of dust at outlet of up-draft gasifier. Offers cost-effective, highly efficient and environment-friendly biomass gasification system. Flushes tar residues away from gasifier towards combustion unit.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of the gasifier of a biomass gasification system.    Up-draft gasifier (4)    Pipe (5)    Top end (12)    Outlet (15)    Manifold system (16)
NOVELTY - The apparatus (S1) has a biological reactor (1) into which activated sludge for processing wastewater is thrown. An analyzer (6) measures the quantity of dissolved oxygen in wastewater. A blower (3) and an air volume controlling valve (5) control air volume of aeration unit (4) which aerates wastewater. A control unit (7) controls blower and valve based on measured value of analyzer so that measured value turns into target value of dissolved oxygen. The control unit changes target value of dissolved oxygen according to particle size of sludge estimated by estimation unit (8).    USE - Water treatment apparatus for processing organic substance and nitrogen in lifestyle wastewater e.g. sewage.    ADVANTAGE - The control of amount of aeration for parallel advancing nitrification reaction and denitrifying reaction by the aerobic tank can be performed appropriately by considering the active sludge particle size such as floc particle size and changing the target value of dissolved oxygen. Hence, the organic substance and the nitrogen in the wastewater can be removed efficiently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) water-treatment method; and    (2) program for treating wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water treatment apparatus. (Drawing includes non-English language text)    Biological reactor (1)    Blower (3)    Aeration unit (4)    Air volume controlling valve (5)    Dissolved oxygen analyzer (6)    Control unit (7)    Particle size estimation unit (8)    Water treatment apparatus (S1)
NOVELTY - The apparatus has an acquisition unit (21) that acquires correlation value of quantity of nitrous oxide in a reactor (13). A storage unit (23) stores the corrected amount of aeration to nitrous oxide production amount in related table which concerns on the appropriate amount of the nitrous oxide production. A control unit (25) controls the amount of aeration by setting the corrected amount of aeration using the appropriate corrected amount concerned on the aeration unit (15) corresponding to the correlation value of the quantity of nitrous oxide.The reactor has activated sludge stored with the to-be processed water.    USE - Apparatus for treating biological water e.g. to-be-processed water such as sewage water from home and factory, used for water-treatment system.    ADVANTAGE - The quality of the to-be-processed water can be improved. The suppression of the production amount of the nitrous oxide in the to-be-processed water can be attained. The amount of carbon dioxide discharged from water treatment plants at the time of sewage work can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the functional block diagram of the biological water treatment apparatus. (Drawing includes non-English language text)    Biological reactor (13)    Aeration unit (15)    Nitrous oxide amount correlation value acquisition unit (21)    Aeration amount corrected storage unit (23)    Aeration amount control unit (25)
NOVELTY - The carbonization-process system acquires dry biomass by drying the moisture biomass by an aerobic fermentation. A low temperature carbonization furnace (10) dry-distills dry biomass. The carbide is collected from the carbonization furnace. The combustion furnace (20) is set to burn the volatile component produced from carbonization furnace e.g. indirect heating type rotary kiln furnace. The hot air occurred with the combustion furnace is utilized as an indirect heating source of carbonization furnace.    USE - Carbonization-process system such as energy independent carbonization process system for processing moisture biomass. Uses include but are not limited to moisture biomass such as agricultural type waste material such as wooden waste material of forestry, rice straw, maize, and chaff, construction waste material, foodstuff waste material, food-processing residue such as high tea dreg and coffee dreg, livestock excrement, fishery residue and sewage sludge.    ADVANTAGE - Since the hot air occurred with the combustion furnace is utilized as an indirect heating source of carbonization furnace, the biomass can be dried efficiently by carrying out the aerobic fermentation of the moisture biomass and the external energy consumption can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbonization treatment method of moisture biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbonization-process system. (Drawing includes non-English language text)    Carbonization furnace (10)    Rotary kiln (11)    Outer periphery heating chamber (12)    Heating pipe (13)    Combustion furnace (20)
NOVELTY - Effective usage of woody biomass involves chipping woody biomass such that mean diameter is 40 mm or less, heating the wood chip to 250-450 degrees C, crushing, mixing the crushed wood chip and bamboo, molding the mixture and transporting the molded product.    USE - Effective usage of woody biomass as energy source for manufacture of steel in iron mill (claimed) and thermal power station.    ADVANTAGE - The woody biomass is efficiently used as energy source in manufacture of steel, by simple method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of effective usage of woody biomass. (Drawing includes non-English language text)
NOVELTY - The furnace has a gasification chamber connected with a gas pipe. The gas pipe is connected with a tar collecting processor in a series manner. A reflux pipe passes through the gasification chamber. An oil outlet opening of the reflux pipe is connected with a combustion section of the gasification chamber.    USE - Tar recovering device integrated biomass gasification furnace.    ADVANTAGE - The tar collecting processor is connected with the gas pipe in the gasification chamber so as to collect tar component and prevent the gasification chamber from being cracked. The furnace has wide range of applications, and reduces tar block damage degree of the gas pipe, avoids waste tar environment pollution and improves energy utilization rate.
NOVELTY - Invention relates to the fish industry and methods of producing biofuel from hydrobiont wastes. The method of obtaining biofuel from fat-containing hydrobiont wastes involves obtaining fish oil with acid number of 2.1-4.6 mg KOH/g. The fish oil is neutralised by adding alkali until attaining acid number of 0.7 mg KOH/g. The neutralised fat, which contains soap and alkali residues, is washed once with 10% salt solution and twice with water at temperature 90-95 degrees C for 90 minutes. The fish oil undergoes reesterification while adding 25% ethanol and 0.75% dry NaOH based on the weight of the fat used.    USE - Chemistry.    ADVANTAGE - Improved method and high output of biofuel. 1 cl, 1 ex
NOVELTY - Invention relates to obtaining a masout additive which contains organic active components dissolved in diesel, where the organic active components are a magnesium salt of tall oil acids of hardwood and terpene alcohols with the following ratio of components, %: magnesium salt of tall oil acids of hardwood 18-22, terpene alcohols 65-68 and diesel - the balance.    USE - Chemistry.    ADVANTAGE - Improved additive properties. 3 tbl
NOVELTY - The device has a gas furnace provided with a stirring chamber. A gas collecting chamber is connected with a tubular pipe layer. A furnace tube is provided with an upper and lower baffle plates. A gas-making furnace tube shell is provided with a high temperature smoke gas outlet. The high temperature smoke gas outlet is provided with a dust hopper. The stirring chamber is located in the gas-making furnace tubular pipe layer. A carbon coke cracking furnace tube shell is connected with the furnace tube shell. The furnace tube shell is connected with a high temperature flue gas pipeline.    USE - Biomass air flow state high temperature heat exchange gasification device.    ADVANTAGE - The device performs cracking-gasification process with high temperature gas that is obtained by burning the biomass micrometer fuel, where biomass micrometer fuel is a reproducible clean energy. The device has wide application range and high thermal efficiency and thermal value, and is inexpensive.
NOVELTY - A biomass briquette coal comprises (pts.wt.) coal slime (35-45), anthracite (25-35), flue-cured tobacco straw (20-25), chlorine-fixing agent (0.5-1.5), sulfur-fixing agent (0.5-1.5), and clay (7-9).    USE - A biomass briquette coal for use as fuel.    ADVANTAGE - The biomass briquette coal produces less pollution, and has improved ignition characteristic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the biomass briquette coal comprising:    (A) drying flue-cured tobacco straw, and crushing into strips having a length of 3-5 mm;    (B) crushing anthracite, drying and crushing clay, and screening clay using 300-500 mesh sieve; and    (C) mixing prepared materials, subjecting mixture to cold pressing high-pressure forming using a polygon forming machine, and drying.
NOVELTY - A composition comprises a polynuclear manganese cluster compound having oxygen-containing groups. The oxygen-containing group is carboxylate group, alcohol group, alkoxide group and/or ether group.    USE - Composition is used for generating hydrogen and oxygen from water (claimed) e.g. saline and sea water.    ADVANTAGE - The composition is economically prepared. The composition is active in natural water including sea water, even with low concentration of composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of generating hydrogen and oxygen from water.
NOVELTY - Mixed fuel includes lignin and hydrogen in the weight ratio of lignin to hydrogen of 9:1 to 1:9, mainly of 2:1 to 1:3.    USE - Power industry.    ADVANTAGE - More complete combustion of lignin; reduction of ash content of fuel. 1 cl
NOVELTY - Manufacture of biomass fuel involves mixing sludge (1) and activated carbon which has stinking-adsorption capacity.    USE - Manufacture of biomass fuel.    ADVANTAGE - The method efficiently and economically provides biomass fuel having deodorizing effect by preventing global warming.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) information-management method of biomass fuel; and    (2) information-management system of biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure explaining the manufacture of biomass fuel.    Sludge (1)    Spin-drying process (2)    Dehydrated sludge (3)    Drying (4)    Dried sludge (5)
NOVELTY - The method involves heating up the temperature of the metal type catalyst and the gasifying gas by supplying the mixed gas of an oxidizing agent and combustible gas in reaction container (10a) by which the metal type catalyst is arranged. The combustible gas in the mixed gas is a combination of one or more kinds selected from town gas, liquefied petroleum gas, biogas and the gasifying gas by which the tar decomposition process is carried out. The mixture amount of the combustible gas in the said mixed gas is one or less of a theoretical oxygen ratio.    USE - Method for decomposing tar contained in gasifying gas for gasification of waste material such as biomass fuel, coal, corks, waste oil, wood chip, sewage sludge and other organic compounds in gasification facility.    ADVANTAGE - The stable and favorable combustion can be enabled by supplying the mixed gas of the oxidizing agent and combustible gas in gasifying gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for tar decomposition installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tar decomposition installation. (Drawing includes non-English language text)    Tar decomposition installation (10)    Reaction container (10a)    Mixed gas supply unit (11)    Catalyst layer (12)    Catalyst temperature measurement unit (14)
NOVELTY - The structure has a filling unit covered with an original rubbish layer. The original rubbish layer is provided with a horizontal landfill gas collecting groove system outer layer and a horizontal landfill gas collecting groove system inner layer. A liquid collecting and discharging system is fixed with a marsh gas collecting system. The marsh gas collecting system is provided with a crushed stone layer.    USE - High efficient producing moor-type domestic rubbish landfill structure for use in an initial filling marsh gas field.    ADVANTAGE - The structure has high stability. The structure effectively prevents a domestic rubbish landfill stack body from being damaged, maintains level of water content at a rate of 30-60 percent and ensures better biogas production process.
NOVELTY - The system has a stacking tank (1) that integrates a required quantity of compost raw material (9) containing microorganisms and moisture content. A microwave waveguide (15) which has a microwave output hole (15a) that outputs a microwave to the compost raw material. The outputted microwave is propagated inside the microwave waveguide to the stacked compost raw material. The compost raw material of stacking tank is heated by absorbing the moisture content contained in the output microwave, and for performing heat energy conversion.    USE - System for manufacturing compost raw material e.g. livestock excrement such as cattle feces, pig feces, hen droppings and organic refuse.    ADVANTAGE - The power consumption of the compost manufacturing system can be reduced. The compost raw material can be heated and manufactured efficiently by absorbing moisture content in the compost raw material, and hence the activity environment of microorganism can be attained favorably. Since the manufacturing time of compost raw material is reduced, the productivity of the compost manufacturing system can be improved.    DETAILED DESCRIPTION - An air delivery valve (11) of the compost raw material stacking tank is connected to a ventilation unit (13) arranged at the floor surface, for supplying air with respect to the stacked compost raw material. The supplied air is provided within the microwave oscillation unit (19) to the air delivery tube. The microwave oscillation unit outputs a microwave to a microwave waveguide. An INDEPENDENT CLAIM is included for method for manufacturing compost.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the system for manufacturing compost raw material.    Compost raw material stacking tank (1)    Compost raw material (9)    Air delivery valve (11)    Ventilation unit (13)    Microwave waveguide (15)    Microwave output hole (15a)    Microwave oscillation unit (19)
NOVELTY - Composite methanol diesel oil producing device, comprises at least four groups of conveying portions, mixing portion and emulsifying portion. The output end of each conveying part is connected with the input end of the mixing component, and the output end of the mixing portion is connected with the input end of the emulsifying component.    USE - The device is used for producing composite methanol diesel oil used as fuel for car.    ADVANTAGE - The composite methanol diesel oil producing device is convenient for production of the composite methanol diesel oil, reduces the manual operation, and reduces the production cost.
NOVELTY - The furnace has a burning nozzle arranged on a fuel inlet of a lower part of a vertically arranged furnace body. Bottom of the furnace body is provided with a fuel preprocessing system. The fuel preprocessing system includes a fuel crushing device and a screening device. Bottom of the furnace body is connected with a burner. A gasification furnace synthesis gas opening is arranged with a synthetic gas monitoring unit. Microwave plasma generators are arranged in a gasification reaction zone of the furnace body. Each microwave plasma generator is formed with 2-4 working gas access openings.    USE - Microwave plasma biomass entrained flow bed gasification furnace.    ADVANTAGE - The furnace mainly uses microwave and is combined with the plasma technology and efficient air flow bed technology, which makes the furnace having high reaction activity based on the characteristics of the biomass fuel.
NOVELTY - The device has a water-cooling flue, a cooling medium conveying pipe, a water-cooling flue inlet water-cooling flue, a watercooling flue elbow, a straight watercooling flue, a lower bending head water-cooling flue and an outlet watercooling flue provided in an orderly sealing connecting form. A circumferential direction adjacent to the cooling medium conveying pipe forms an annular water cooling wall. An annular water cooling wall cavity is provided with a section of a smoke channel passing through a flat steel seamless connection.    USE - Biomass gasification cooling system water cooling smoke channel device.    ADVANTAGE - The annular water cooling wall cavity is provided with the section of the smoke channel passing through the flat steel seamless connection, so as to connect the effect of the smoke and the smoke gas, such that the gas duct wall inner wall temperature is low, and the tar is not suitable for solidification, thus effectively preventing the tar solidified of the coke ash fouling and ensuring the device long term operation stability. The device has small thickness of the smoke channel inner part refractory castable, and avoids the cracking and collapsing of the refractory casting material of the cylinder body, so as to cause burning through smoke leakage and to ensure the device long term operation.
NOVELTY - The exchanger has a heating pipe section inserted into a boiler, and a heat absorption section of a heating pipe arranged in a heat preservation wall. A heat preservation wall is welded with an inlet interface and an outlet interface. A heat insulating wall is welded with a lower end of an ash falling.    USE - Heat tube type heat exchanger for a biomass fuel gasification synthesis gas cooling system.    ADVANTAGE - The exchanger can meet the gasification system, while absorbing synthesis gas.
NOVELTY - The boiler has a down-sucking type biomass gasification heating device connected with a cooler through an air pipe, where the cooler is connected to a water heater through the air pipe.    USE - Biomass gasification boiler.    ADVANTAGE - The boiler is installed with a cleaning door and a stuffing box for the dust in the mixed gas at a specific time, so that the mixed gas is sent to the clean dust in the combustion heater in the down-sucking type biomass gasification heating device and cooling device to form a upwards from flame path taper pipe downwards, to discharge upward combustion from the chimney, thus burning the mixed gas burn fully, and reducing the dust in the flue gas. The boiler is environmental-friendly.
NOVELTY - The system is provided with a centralized gas supply gasification furnace automatic blanking fuel gas generator, a gas cooling device, a water circulation filter, a biomass gas concentrated storage device and a user terminal gasification furnace.    USE - Automatic centralized gas supply gasification furnace system for a straw resource.    ADVANTAGE - The system has simple structure, stable gas system and high storing amount, and reduces the usage cost and labor intensity of a worker and improves the production efficiency. The system is convenient to use.
NOVELTY - Block biomass raw material comprising crushing wood block, corn core, agricultural straw pressing block and pressing block biomass waste, is prepared. Gas is introduced into biomass raw material, and thermalization reaction is performed to generate mixed gas. Dust and ash of mixed gas are removed and subjected to gas-liquid separation process. The resultant mixed gas after gas-liquid separation is subjected to liquid collecting tank by high-pressure high-temperature resistant fan, and processed to obtain dry biomass fuel gas.    USE - Manufacture of dry biomass fuel gas.    ADVANTAGE - The method efficiently provides dry biomass fuel gas with reduced generation of sewage without producing equipment and pipeline blockage.    DETAILED DESCRIPTION - Block biomass raw material comprising crushing wood block, corn core, agricultural straw pressing block and pressing block biomass waste, is prepared. Gas is introduced into biomass raw material, and thermalization reaction is performed to generate mixed gas. Dust and ash of mixed gas (50-80%) are removed by introducing into mixed gas inlet of cyclone dust collector, and then to dust cleaning tower. Heat of mixed gas is exchanged after removing the dust by mixing gas temperature of heat exchanger. The liquid medium after condensed in the heat exchanger, the mixed gas is subjected to gas-liquid separating tower. Gas-liquid of the liquid medium is separated from the bottom of the separation tank. The resultant mixed gas after gas-liquid separation is subjected to liquid collecting tank by high-pressure high-temperature resistant fan, and processed to obtain dry biomass fuel gas. An INDEPENDENT CLAIM is included for device for manufacturing dry biomass fuel gas.
NOVELTY - The anchoring mechanism comprises gaskets for connecting inlet and outlet of a reactor rotary cylinder. A power system is provided that continues breakdown of biomass in the reactor revolving cylinder. A device tab and collector are equipped in a reactor. A moat is also provided that is fixed by a flexible rotary spring.    USE - Anchoring mechanism for rotary drum reactor thermal expansion compensator.    ADVANTAGE - The anchoring mechanism comprises gaskets for connecting inlet and outlet of the reactor rotary cylinder, where a power system is provided that continues breakdown of biomass in a reactor revolving cylinder, and thus ensures improved performance of the anchoring mechanism.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reactor revolving cylinder.
NOVELTY - Binder comprises (in wt.%): lignosulfonate (1-50), water (1-40), alcohol (1-20), cane molasses (1-20) and babassu oil (10).    USE - Binder for manufacturing briquettes of plant and mineral origin or of biomass furnace.    ADVANTAGE - The binder is easy to burn with low smoke and odor.
NOVELTY - The cracker has a heating cavity (2) provided with a combustion plate (11), an ash discharge cavity under plate (13) and an ash discharging opening (14). The heating cavity is connected with a fan (8) through an inlet (9) and a cyclone dust collector air inlet pipe (12). A hopper (6) is arranged at an upper part of a hopper switch (7). A speed reducer is connected with a spiral feeding device (17), a motor (18) and a material chamber (15).    USE - Cracker for pyrolysis of biomass solid fuel to produce biomass gas.    ADVANTAGE - The cracker reduces presence of tar content, thus ensuring thermal stability of gas fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cracker for pyrolysis of biomass solid fuel to produce biomass gas.    Heating cavity (2)    Hopper (6)    Hopper switch (7)    Fan (8)    Inlet (9)    Combustion plate (11)    Cyclone dust collector air inlet pipe (12)    Ash discharge cavity under plate (13)    Ash discharging opening (14)    Material chamber (15)    Spiral feeding device (17)    Motor (18)
NOVELTY - The system has a hot-blast stove and a sludge drying machine (2) which is connected with a high temperature smoke channel (11). The sludge drying machine is set on the upper portion of a cyclone device (3). A slag recycling channel (12) is positioned at the bottom portion of the sludge drying machine and the cyclone device. A slag recovery channel is connected to a fuel inlet of the hot blast stove.    USE - Sludge purifying treatment system.    ADVANTAGE - Sludge purification can be performed simply. The treatment system can be installed easily. The portability of the treatment system can be performed conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sludge purifying treatment system. (Drawing includes non-English language text)    Sludge drying machine (2)    Cyclone device (3)    High temperature smoke channel (11)    Slag recycling channel (12)    Circulating pipe (13)
NOVELTY - Double-layered semi-automatic photothermal anaerobic reaction cabinet comprises a solar heat collecting device and a biogas generator. The main body of the biogas generator is a double-layer glass fiber reinforced plastic structure with vacuum interlayer. The bottom of the main body of the biogas gas generator is set with multiple spiral deslagging device. The spiral deslagging device through a spiral drive motor drives the screw to rotate to discharge the biogas residue and sand.    USE - Used as a double-layered semi-automatic photothermal anaerobic reaction cabinet.    ADVANTAGE - The reaction cabinet: ensures simple installation without the requirement of an auxiliary pool, long service life and continuous and highly-efficient production; automatically discharges slag and sand; and can achieve semi-automatic centralized control, and is economical.
NOVELTY - The fluidized bed reactor has sparge pipes (40,42) which are installed at fluidized bed reaction furnace (60). The pipes are used for supplying auxiliary fuel or steam to the fluidized bed reaction furnace. Several spray holes are formed in the pipes. The fluidized bed material is flowed inside the reactor main portion. The sparge pipes are supported by the support stand. The reactor main portion is provided with combustor, heat exchanger, dryer, gasifier, pyrolyzer and mixer.    USE - Fluidized bed reactor for producing town gas from wood chip, sawdust, rice hulls, biomasses, coal and other waste products.    ADVANTAGE - The fluid supplied to the furnace can be heated easily and rapidly. The reverse flow of fluidized bed material from the furnace to the solid fuel feed port can be prevented effectively. The composition of the gas can be controlled easily and effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) operation method of fluidized bed gasifier; and    (2) method for supplying solid fuel to fluidized bed reaction furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fluidized bed reactor. (Drawing includes non-English language text)    Hopper (10)    Solid fuel transfer apparatus (20)    Solid fuel feed port (30)    Sparge pipes (40,42)    Fluidized bed reaction furnace (60)
NOVELTY - The system (10) has a fuel feeder (20) which produces the fuel gas. A fuel cell stack (900) is provided to produce fuel gas generated from the fuel feeders (20,30). The fuel gas is supplied to the fuel cell stack which is more than the amount of air.    USE - Fuel cell system for liquefied natural gas (LNG) ship.    ADVANTAGE - The load which is provided in the fuel cell system can be reduced. The subordinate can be controlled while the power consumption of the system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for liquefied natural gas (LNG) ship.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (10)    Fuel feeders (20,30)    Fuel cell stack (900)
NOVELTY - Pulverized food waste treatment agent comprises dried tree branches or leaves obtained from pine trees, big cone pine trees, white oak trees, mulberry trees, and persimmon trees, dried rice straws, dried flesh or outer skin of Lagenaria leucantha, dried vegetable chosen radish, cabbage, Arctium edule, and Nelumbo nucifera, dried flowers, leaves, and stems of sunflower, dried corn husk, and dried medical herbs including Astragalus membranaceus, angelicae radix, Cnidium, mugwort, and arrowroots.    USE - The pulverized food waste treatment agent is useful as alternative feed for cattle, or compost for providing antibacterial effect.    ADVANTAGE - The agent removes moisture and bad odor of food waste using natural materials.    DETAILED DESCRIPTION - Pulverized food waste treatment agent comprises dried tree branches or leaves obtained from pine trees, big cone pine trees, white oak trees, mulberry trees, and persimmon trees, dried rice straws, dried flesh or outer skin of Lagenaria leucantha, dried vegetable chosen radish, cabbage, Arctium edule, and Nelumbo nucifera, dried flowers, leaves, and stems of sunflower, dried corn husk, and dried medical herbs chosen from Astragalus membranaceus, angelicae radix, Cnidium, mugwort, wild Chrysanthemum, and arrowroots, where the dried products are pulverized to 100-300 meshes sieve.
NOVELTY - An apparatus for treating leachate has an anaerobic digestion unit for carrying out anaerobic digestion of leachate and producing hydrogen and methane gas, a sludge treatment portion for heat-decomposing sludge discharged from anaerobic digestion portion and producing hydrogen and methane gas, a filtrate processing unit for sterilizing anaerobic filtrate from anaerobic digestion portion, and a gas storage unit for storing hydrogen gas and methane gas generated in the sludge treatment portion.    USE - Apparatus for treating leachate (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for leachate treatment method.
NOVELTY - Method for producing biodiesel, involves separating fat and oils from organic waste, inoculating Rhodococcus into the separated fat and oils, culturing the strain, separating lipid from the cultured product, and producing the biodiesel by reacting the lipid chemically.    USE - The method is useful for producing biodiesel.    ADVANTAGE - The method produces high-value added biodiesel by utilizing waste resources and hence is economical and environmentally-friendly.
NOVELTY - A fuel oil preparation method involves putting biomass and waste plastic in a cracking reactor and heating to raise temperature for pyrolysis reaction to get product gas, followed by sending the product gas into refining tower for upgrading to obtain liquid product and sending liquid product into rectifying tower for rectifying and separating to obtain different fractions of fuel oil, where the gas product and solid residue from the rectifying tower is recycled to cracking reactor.    USE - Method for preparing fuel oil.    ADVANTAGE - The method enables preparing fuel oil with improved oil quality and oil producing rate in an economic and eco-friendly manner, and effectively saving petrochemical resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for preparing fuel oil.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has a reservoir (10) that accommodates sludge. A heat exchanger (50) is installed between high pressure pump (30) and pre-heater so that the warmed fluid is ejected in the pre-heater. An effluent cooling device is installed in depressurization valve (80) of a steam boiler (60) so as to decompress the fluid passing through the steam boiler. A three-way solenoid valve (90) is installed at rear end of depressurization valve. A methane gas engine generator (110) is connected to a methane gas discharge pipe of an anaerobic fermentation tub (100).    USE - Apparatus for treating sludge.    ADVANTAGE - The methane gas is used as the heating source so that the amount of electricity required for the sludge heating is reduced and the sludge treatment management cost is saved.    DETAILED DESCRIPTION - The apparatus has a filter (150) that is installed at the rear end of a flash chamber (140) for separately filtering the inorganic material from the fluid passing through the flash chamber. An INDEPENDENT CLAIM is included for sludge treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sludge treatment apparatus.    Reservoir (10)    High pressure pump (30)    Heat exchanger (50)    Steam boiler (60)    Depressurization valve (80)    Three-way solenoid valve (90)    Anaerobic fermentation tub (100)    Methane gas engine generator (110)    Flash chamber (140)    Filter (150)
NOVELTY - The system has multifunctional heat exchange device (3) that is connected to pyrolysis apparatus, and is provided with gas channel and condensed water passage. A guiding device (11) is connected to air supply device. A condensed mixed liquid outlet (10) is connected with static knockout device (13). A residual heat supply device is provided with buffer tank, condensed water outlet channel, boiler (15) and heat-conducting pipe (16) which are connected in series to form a water circulation passage. A pneumatic conveying apparatus (29) is connected with carbon powder collecting device (30).    USE - Biomass waste resource transformation system.    ADVANTAGE - The biomass waste resource transforming rate can be improved, by preventing the occurrence of pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass waste resource transformation system. (Drawing includes non-English language text)    Multifunctional heat exchange device (3)    Condensed mixed liquid outlet (10)    Guiding device (11)    Static knockout device (13)    Boiler (15)    Heat-conducting pipe (16)    Pneumatic conveying apparatus (29)    Carbon powder collecting device (30)
NOVELTY - A methanol gasoline comprises (pts.wt.) methanol (30-60), benzene (25-50), dimethyl ether (2-8), dimethylbenzene (1-5) and petroleum ether (1-8).    USE - Methanol gasoline.    ADVANTAGE - The gasoline has less pollution, and low cost; and does not affect the performance of the vehicle. The preparation is simple, does not discharge harmful substance, is environment-friendly, can replace petroleum fuel, can improve performance and quality of product and reduce carbon dioxide, oxynitride and main pollution discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of methanol gasoline comprising weighing each raw material under room temperature and normal pressure, mixing raw materials, and stirring to transparent product.
NOVELTY - Method for producing biogas by hot alkaline combined circulating refluxed sludge treatment and enhanced anaerobic digestion, involves mixing concentrated sludge with dehydrated sludge to obtain mixed sludge, taking the mixed sludge as the fed materials for performing anaerobic digestion, discharging the sludge in same volume, performing hot alkaline combined circulating refluxed sludge treatment, circularly performing anaerobic digestion, and collecting the biogas.    USE - The method is useful for producing biogas.    ADVANTAGE - The method enhances the mixing effect of the fermentation system, strengthens the dissolution of solid organic materials, and implements efficient and stable operation of the reactor.
NOVELTY - Biological oil removing agent comprises 20-40 wt.% of Bacillus subtilis, 20-35 wt.% of Bacillus polymyxa, 10-25 wt.% of Aspergillus niger, and 10-25 wt.% of Nocardia .    USE - The biological oil removing agent is useful for removing organic oil blockage in pipeline of a kitchen and a restaurant.    ADVANTAGE - The biological oil removing agent is non-toxic and eco-friendly.
NOVELTY - For purifying livestock farming biogas slurry, an Aucuba japonica variegate is used. The pink Reineckea herb is planted in the pollution environment of livestock farming biogas slurry; or planted in an automatic oxygen constructed wetland system.    USE - For purifying livestock farming biogas slurry (claimed).    ADVANTAGE - The pink Reineckea herb can be planted in the pollution environment of livestock farming biogas slurry, which fully absorbs ammonia nitrogen, total nitrogen (TN), total phosphorus (TP), chemical oxygen demand and other pollutants in the livestock farming biogas slurry, as well as pink Reineckea herb tenacious vitality, can be planted directly, without special management and perennial characteristics, which permanently solves the biogas slurry pollution problems of the purifying livestock farming. The Aucuba japonica variegate allows less investment, low running costs, shows good effect, and the operation is simple, to ensure winter purifying effect of artificial wetland system. The harvest pink Reineckea herb can cure tuberculosis, cough haemoptysis, chronic bronchitis, asthma, rheumatoid arthritis, and other symptoms. The pink Reineckea herb allows environmental protection, combined with the landscape construction and the economic construction, which reflects the sustainable development idea of both of the sewage treatment, the ecological restoration, as well as the landscape construction and the economic benefit, and also has far reaching significance.
NOVELTY - Preparing fuel from municipal domestic wastes by using device comprises taking municipal solid waste separated from plastic, metal and glass bottle as recycled material, removing stone, brick and cement as non recycled waste material, and remaining waste as raw material, preparing raw materials by screening, gravity separation, sieving, crushing, drying, removing water, and performing extrusion molding.    USE - The method is useful for preparing fuel from municipal domestic wastes by using device.    ADVANTAGE - The method replaces the solid combustible mineral coal and coke to form large fuel electric plant or replacement energy product of domestic fuel; and is economical.
NOVELTY - The method comprises taking 0-95% of ethanol water solution as a solvent and then extracting Scutellaria plant to obtain a crude extract and then separating and purifying via polyamide or macroporous resin to obtain refined products. The Scutellaria plant comprises Scutellaria baicalensis. The active extract is extracted from the underground part or overground part of the Scutellaria plant. The parts extract and separate from stem and/or leaves. A particle size of the polyamide or the macroporous resin is 10-100 meshes.    USE - The method is useful for preparing an active extract containing isoscutellarein 7-O- beta -d-glucuronide, which is useful for treating cardiovascular disease and cerebrovascular disease (claimed). No biological data given.    ADVANTAGE - The method is capable of simply and economically preparing the active extract in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises taking 0-95% of ethanol water solution as a solvent and then extracting Scutellaria plant to obtain a crude extract and then separating and purifying via polyamide or macroporous resin to obtain refined products. The Scutellaria plant comprises Scutellaria baicalensis. The active extract is extracted from the underground part or overground part of the Scutellaria plant. The parts extract and separate from stem and/or leaves. A particle size of the polyamide or the macroporous resin is 10-100 meshes. A weight ratio of the crude extract and the polyamide or macroporous resin is 1:5-40. A ratio of a diameter and a height of chromatographic column is 1:5-20. An INDEPENDENT CLAIM is included for a composition.
NOVELTY - Preparing dutasteride comprises reacting acidity of DT4 carboxyl with ammonia directly for generating DT4-ammonium salt, where the ammonium salt is dewatered into DT4-amide, and conducting the amide and the 2,5-bis(trifluoromethyl)phenylamine (BTFMA) with an amino exchange reaction.    USE - The process is useful for preparing dutasteride (claimed) which is useful for treating benign prostatic hyperplasia (BPH), and reducing acute uroschesis. No biological data given.    ADVANTAGE - The process is capable of rapidly, economically and easily preparing dutasteride with high yield and purity, and reduced waste water in a large scale, simple and an environmental friendly manner. The dutasteride avoids adverse events.
NOVELTY - Method of launching biological treatment plants involves feeding waste water into an aeration tank and biocenosis culturing in aeration conditions. Biocenosis culturing is carried out with continuous aeration for 36-48 hours with 0.5-1.0 m3/h of air per 1 m3 of the aeration tank of the portion of clarified household wastes with addition of biologically active nitrogen and phosphorus compounds BOD5:N:P=100:1:0.5. Adaptogen is simultaneously added with gradual growing, in 36-48 hours, in the wastes being treated of a given concentration of the reference component contained in adaptogen from 0 to 5asterisk104 maximum allowable concentration (MAC).    USE - Chemistry.    ADVANTAGE - Invention provides faster launching of biological treatment plants, cuts the time for growing biocenosis; treatment of clarified household wastes begins after 5 days. 3 cl, 1 tbl, 1 ex
NOVELTY - The system has a connecting pipe whose smoke exhaust cyclone dust collector is connected with a tubular dust-removing and cooling device and a flue gas pipe. An air outlet of a biomass gasification furnace is connected with the cyclone dust collector. A smoke exhaust pipe of the tubular dust-removing and cooling device is connected with a smoke inlet pipe of another tubular dust-removing and cooling device. A smoke exhaust pipe of the latter tubular dust-removing and cooling device is connected with a smoke inlet connecting pipe of a foam dust-removing cooling tower.    USE - Dust removing system for a biomass gasification furnace.    ADVANTAGE - The system has simple structure, better dust removing effect and low operation cost.
NOVELTY - Producing a synthetic coal from a fermentation residue having a low lignocellulosic content, comprises subjecting the fermentation residue to hydrothermal carbonization in an aqueous suspending medium at 170-225 degrees C, at a pressure of 0.8-2.41 MPa, for less than 4 hours, and separating the resulting synthetic coal from a liquid component.    USE - The method is useful for producing a synthetic coal from a fermentation residue having a low lignocellulosic content (less than 20 wt.%) (all claimed). The coal is used as a soil additive to improve moisture retention and provide nutrients for plant growth, and for the production of industrial chemicals e.g. methanol, acetic acid and ethylene glycol, and hydrocarbon fuels. The coal is useful as a carbonaceous starting material for the production of coke used for the manufacture of steel.    ADVANTAGE - The method does not require drying of the fermentation residue which provides for a more energy efficient method of processing. The synthetic coal has combustion heat of greater than 10000 British thermal units per pound.
NOVELTY - Production equipment comprises a microcomputer control processor, a gasoline transport component, an additive transport component, a methanol transport component and a reconciled pipeline. The gasoline transport component, additive transport component and methanol transport component are respectively connected with the microcomputer control processor through the circuit. The output ends of the gasoline transport component, additive transport component and methanol transport component are connected and passed into the reconciled pipeline.    USE - The equipment is useful for alcohol fuel real-time deployment.    ADVANTAGE - The equipment: makes alcohol fuel deployment flexible and easy, and reduces the inventory of raw material, thus the alcohol fuel is really turned into a car commercial fuel, and is suitable for real-time production in accordance with the storage conditions of alcohol fuel.
NOVELTY - On-site analysis (M1) of at least one quality parameter of material in or from a torrefaction process, comprises: (a) diverting material from the torrefaction process; (b) disintegrating the material from step (a) to expose cross-sections of the material; (c) obtaining a hyperspectral image in at least part of the region of 400-25000 nm of the disintegrated material from step (b) using an on-site camera; and (d) correlating the hyperspectral image from step (c) to the at least one quality parameter of the material.    USE - The methods are useful for: on-site analysis of at least one quality parameter of material in or from a torrefaction process, where the quality parameter is dry matter content, hydrophobicity, brittleness, heating value or grade of torrefaction; and controlling a torrefaction process having an operation temperature and a residence time (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for controlling (M2) a torrefaction process having an operation temperature and a residence time, comprising (a1) obtaining of a hyperspectral image in at least part of the region of 400-25000 nm of optionally disintegrated at least partly torrefied biomass from the torrefaction process, (b1) analyzing the hyperspectral image using multivariate analysis to obtain a data set, (c1) comparing the data set from step (b1) with a reference data set, (d1) based on the comparison of step (c1), determining an optimal operation temperature and an optimal residence time, and (e1) controlling the torrefaction process based on the optimal operation temperature and the optimal residence time.
NOVELTY - The method comprises determining a surface temperature of a biomass in a torrefaction arrangement using an infrared-thermometer, and supplying a stream of inert non infrared active gas in the space between a lens of the infrared-thermometer and the biomass. The temperature of the inert non infrared active gas at a purge gas outlet is above 150 degrees C, above 200?C, above 250?C, above 300?C, above 350?C, above 400 degrees C and above 450 degrees C. The inert non infrared active gas is nitrogen gas. The surface temperature of the biomass at the moment of temperature measurement is 270-350 degrees C.    USE - The method is useful for monitoring a process of torrefaction of a biomass such as lignocellulosic biomass including wood chips (claimed).    ADVANTAGE - The method is capable of precisely and reliably monitoring the process of torrefaction of the biomass with high sensitivity, and prevents condensation of condensable substances in the torrefaction gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of controlling a process of torrefaction of a biomass; and    (2) a torrefaction arrangement.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of infrared-thermometer and a purge gas outlet arranged in a common open-ended pipe for measurement of surface temperature in a torrefaction arrangement.    Infrared thermometer (21)    Lens (22)    Open-ended pipe (23)    Purge gas heater (24)    Heating media inlet (25)    Heating media outlet. (26)
NOVELTY - Extruding and homogenizing machine comprises a main body having a supply opening, an extruder screw, an outlet, a compression cone arranged on the end of the extruder screw, and means for opening and closing the outlet.    USE - The extruding and homogenizing machine is useful for producing recovered solid fuel, where the fuel is useful for domestic consumption and/or energy recovery, preferably using a heat treatment process selected from incineration, incineration, pyrolysis, gasification and gasification plants combined plasma (all claimed).    ADVANTAGE - The machine or method can recover waste energy in a non-harmful and non-polluting manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing recovered solid fuel comprising processing a starting material in extruding and homogenizing machine, at a temperature between 200 and 500 degrees C, and with the outlet opening closed by the opening and closing means; and    (2) a recovered solid fuel obtainable by the method.
NOVELTY - Extract of organic material from a species of Nicotianeae comprises a mixture of 26-33C alkanes at a purity of at least 90 vol.% of total extract.    USE - Used as organic material extract.    ADVANTAGE - The extract of organic material is produced from N. glauca that: grows well in warm arid and semi-arid climates on marginal infertile lands, and grows well on land that is not arable, thus growing in areas where food crops would not thrive without irrigation; and is a potential biofuel crop as it boasts (hardiness, high sprouting capacity, large production of ground biomass and high content of non-structural carbohydrates). At least 95 vol.% of the extract of organic material is produced from species of Nicotianeae .    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of a species of the Nicotianeae in the production of organic material extract.
NOVELTY - The controlling method involves checking and adjusting the dilution gradient of reagents along an overall electrode active surface to achieve variation of reagent dilutions among different parts of the electrode active surface. A local current density produced in a fuel cell per unit of electrode active surface is checked and/or adjusted.    USE - Controlling method for fuel cell (claimed).    ADVANTAGE - Enables controlling the electric efficiency of fuel cell in an easy and rapid manner, before operating the fuel cell itself. Enables controlling the electric power output of fuel cell to dynamically optimize balance between output power and current efficiency according to requirements, thus increasing energy conversion efficiency close to 100% with respect to Gibbs free energy associated with reactions taking place in the fuel cell. Enables maximization of the electric efficiency and power output of fuel cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method of evaluating the electric efficiency of a fuel cell; and    (2) a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic illustration of a fuel cell.    Fuel cell (1)    Intermediate space (2)    Cathodic space (3)    Anodic space (4)    Positive electrode (5)
NOVELTY - Treating lignocellulosic feedstock (10) having cellulose, hemicellulose and lignin to produce sugar rich process stream, comprises: (a) subjecting feedstock to first enzymatic hydrolysis process (20) to solubilize xylose and obtaining effluent stream (22); (b) subjecting stream to second enzymatic hydrolysis process to preferentially solubilize cellulose and obtaining sugar rich process stream; (c) treating sugar rich process stream to reduce level of lignin and obtaining lignin stream and lignin reduced sugar rich process stream; and (d) fermenting lignin reduced sugar rich process stream.    USE - The method is useful for treating a lignocellulosic feedstock comprising cellulose, hemicellulose and lignin to produce sugar rich process stream.    ADVANTAGE - The method reduces the concentration of a product stream from a corn based ethanol plant; reduces or removes lignin from the sugar rich process stream which increases the conversion of the sugar rich process stream to alcohol by the fermentation organisms; increases the yield of fermentable sugars in the process stream at a faster reaction rate; provides lignin with increased yield of alcohol and has a high degree of polymerization; and provides a synergistic effect which reduces the duration of the fermentation process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow chart of treating a lignocellulosic feedstock.    Lignocellulosic feedstock (10)    Optional steam explosion (12)    Activated feedstock (14)    First enzymatic hydrolysis process (20)    Effluent stream (22)
NOVELTY - A hydrogen generating apparatus (100) comprises modifier which produces hydrogen-containing-gas by reforming from raw material and controller which stops operation at 2nd state higher than a state with 1st oxygen concentration in raw material.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Oxygen concentration in raw material can reduce malfunction of a modifier.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel cell system (20); and    (2) operating method of hydrogen generating apparatus (100).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a hydrogen generating apparatus. (Drawing includes non-English language text).    Modifier (1)    Combustor (2)    Temperature detector (3)    Controller (5)    Hydrogen generating apparatus (100)
NOVELTY - The method involves detecting parameter data of an individual electrochemical cell to be analyzed (S1) to check quality of the electrochemical cell. The detected parameter data is transmitted (S2) to a control unit. The detected parameter data is assigned (S3) to the electrochemical cell or stored to the electrochemical cell. A determination is made to check whether a predetermined relationship exists between the parameter data and a predetermined parameter value i.e. quality value (S4), by the control unit for the electrochemical cell that is assigned with the parameter data.    USE - Method for selecting electrochemical cells e.g. galvanic cells and fuel cells, during manufacturing of a battery e.g. plug-in hybrid battery, hybrid cell battery, electric car battery, apparatus battery and stationary application battery (all claimed).    ADVANTAGE - The method enables determining whether the predetermined relationship exists between the parameter data and predetermined parameter value by the control unit for the electrochemical cell that is assigned with the parameter data, thus selecting the electrochemical cells with required quality in an inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a battery comprising multiple electrochemical cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for selecting electrochemical cells during manufacturing a battery.'(Drawing includes non-English language text)'    Step for detecting parameter data of individual electrochemical cell (S1)    Step for transmitting detected parameter data to control unit (S2)    Step for assigning detected parameter data to electrochemical cell (S3)    Step for determining existence of predetermined relationship between parameter data and predetermined parameter value (S4)
NOVELTY - The boiler has a water jacket furnace body whose upper part is provided with a water jacket partition wall. A lower part of a gasification chamber is provided with three combustion chambers. Two dust chambers are provided with a separating plate. A gasification chamber is arranged on an upper part of a sealed inlet. One of two dust chambers is provided with a blower. An inner side part of one of the three combustion chambers is provided with multiple water jacket heat absorption pipes. An upper part of the combustion chamber is provided with a smoke outlet.    USE - Firewood and coal gasification boiler.    ADVANTAGE - The boiler has rational structure, stable gasification and high thermal efficiency, and supplies oxygen according to user requirements and realizes long burning distance and large heating surface.
NOVELTY - The furnace has a furnace cover arranged on an upper end of a furnace body and provided with a feeding device. A cold water pre-heating device is connected with an air inlet pipeline. A lower part of the furnace body is provided with an ignition device and a discharging device. A side wall of a material stewing tank is provided with a discharging port. An inner wall of the furnace body is provided with a hollow furnace cavity. A water outlet pipe of the cold water pre-heating device is arranged in the furnace cavity and connected with the heat collecting water tank.    USE - Straw gasification carbon hot water furnace.    ADVANTAGE - The furnace is environment friendly and energy-saving, and ensures high burning rate.
NOVELTY - A hydrogen gas manufacturing apparatus comprises hydrogen gas storage tank (2) which stores emitted hydrogen gas, float tank connected to hydrogen gas generation container (1) where salt solution and aluminum foil are placed, and flexible pipe. Hardened aluminum foil with wrinkle and oxide layer on the surface is immersed in salt solution.    USE - A hydrogen gas manufacturing apparatus (claimed).    ADVANTAGE - The hydrogen gas manufacturing apparatus has cheap raw materials, simple installation, and safe hydrogen gas generation control.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen gas manufacturing apparatus. (Drawing includes non-English language text).    Hydrogen gas generation container (1)    Hydrogen gas storage tank (2)    Reaction liquid storage tank (3)    Inlet ports (4)    Waste liquid opening (5)
NOVELTY - The present invention relates to a reflow/addition method for kitchen waste compost, which is a manufacturing flow of adopting the immature kitchen waste compost fermenting for about 14 days to reflow and be added into new kitchen waste compost and then being sufficiently mixed in a temperature-adjustable agitating tank. Compared with conventional methods, this invention can increase quantity of the fermentation bacteria and shorter the fermentation/maturation time.
NOVELTY - Plant (1) comprises digester (4), bag-like casing (5) of flexible material and fluid-tight, where the bag-like casing is adapted for containing sewage (14), and defines in internal zone, digestion chamber (40) for digesting the sewage, and the plant further comprises heater (45,68) for heating the sewage.    USE - The plant and co-generation installation are useful for producing biogas (claimed) using sewage, preferably liquid wastewater originating from zootechnic farm.    ADVANTAGE - The plant is simple, and cost-effectively processes large amount of sewage, and increases yield of biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for co-generation installation.    DESCRIPTION OF DRAWING(S) - The drawing shows side view of plant.    Plant (1)    Digester (4)    Bag-like casing (5)    Sewage (14)    Digestion chamber (40)    Heater (45,68)
NOVELTY - Preparing natural d- alpha -tocotrienol from naturally occurring plant source extracts comprising tocotrienols, comprises: (a) heating mixture of secondary amine attached to solid-phase-support and a mixture of tocotrienols and optional alpha -tocopherol from plant extract in the presence of paraformaldehyde, until the non- alpha tocotrienols disappear from the supernatant to give solid-support-adducts; (b) filtering the solid-support-adduct mixture and washing the solid support to remove the unreacted materials; and (c) reducing the solid-support-adduct mixture with reducing agent.    USE - The process is useful for preparing of natural d- alpha -tocotrienol from naturally occurring plant source extracts.    ADVANTAGE - The process involves recovering the solid-phase-bound secondary amine for future use&provides d- alpha -tocotrienol with high purity in economical manner.    DETAILED DESCRIPTION - Preparation of natural d- alpha -tocotrienol from naturally occurring plant source extracts comprising tocotrienols and optionally including alpha -tocopherol or organic impurities comprises: (a) heating mixture of secondary amine attached to solid-phase-support and a mixture of tocotrienols and optional alpha -tocopherol from plant extract in the presence of paraformaldehyde, until the non- alpha tocotrienols disappear from the supernatant to form solid-support-adducts of beta -, gamma -, and delta -tocotrienols and amine; (b) filtering the solid-support-adduct mixture and washing the solid support to remove the unreacted materials that may be present; and (c) reducing the solid-support-adduct mixture with reducing agent to cleave the solid-support-amine and give d- alpha -tocotrienol.
NOVELTY - Marking a petroleum hydrocarbon or liquid biologically derived fuel, comprises adding at least one biphenyl compound (I) to the petroleum hydrocarbon or biologically derived fuel.    USE - The method is useful for marking a petroleum hydrocarbon or liquid biologically derived fuel (claimed), where the petroleum hydrocarbon includes crude oil and products derived from petroleum refining process such as lubricating oil, hydraulic fluid, brake fluid, gasoline, diesel fuel, kerosene, jet fuel and heating oil, and the liquid biologically derived fuel includes biodiesel fuel, ethanol, butanol and/or tert-butyl ether.    DETAILED DESCRIPTION - Marking a petroleum hydrocarbon or liquid biologically derived fuel, comprises adding at least one biphenyl compound of formula (I) to the petroleum hydrocarbon or biologically derived fuel.    G1 = 4-40C organic functional group.
NOVELTY - Disclosed is method of bio-diesel production from dairy waste. Fossil fuels demand to meet energy requirement is increasing every day and oil reserves are reducing dramatically. Sustainable energy production represents one of the most alarming problems of the 21st century. The basic sources of this energy are petroleum, natural gas, coal, hydro and nuclear power. Petroleum based diesel consumption pattern in India 6 is around 36 multiply 10 tons. The major disadvantage of using these fuels is atmospheric pollution. Petroleum fuels combustion is a major source of greenhouse gas (GHG). Apart from these emissions, petroleum fuels are also major source of other air contaminants including NOx, SOx, CO, particulate matter and volatile organic compounds. Recently, because of increase in crude oil prices, limited resources of fossil oil and environmental concerns, there has been a renewed focus on vegetable oils and animal fats to make bio-diesel. As a kind of alternative renewable biofuels, development of biodiesel is helpful to realize sustainable development of human being. India milk production is 109 million tons for 2009-2010 as per US government report. Every year billions kg of waste produced annually by dairy industries in India. Present reviews accentuate the potential advantages of using dairy waste as a source of bio-diesel production. Image 0/0
NOVELTY - Producing a mixture of methyl ester from an oil source involves reacting the oil source with an alcohol in the presence of a heterogeneous catalytic system derived from mixed metal oxide of calcium and a second metal.    USE - For producing a mixture of methyl ester from an oil source (claimed), and for producing biodiesel.    ADVANTAGE - The method is cost and time effective method which acquires biodiesel from a non-edible oil source which is commercially available at low price compared to its edible counterparts; and provides high yield (i.e. 80%) of biodiesel.
NOVELTY - The system has carbon-dioxide absorption column (37) which makes absorption liquid absorb the carbon dioxide in the fuel gas which flowed down the shift reaction device (5,7,11). The evaporator (6,9,13) heat-exchanges with the fuel gas heated up with the shift reaction heat arose in the shift reaction device, and generates a vapor. The absorption liquid heater heats the absorption liquid supplied to the absorption liquid reproducing apparatus from the carbon-dioxide absorption tower by the vapor generated with the evaporator as a heat source.    USE - Gasification-power-generation system for generating gasified fuel gas emitted from coal and biomass used as fuel for gas turbine.    ADVANTAGE - The shift reaction heat which produces the carbon monoxide contained in fuel gas in the case of the shift reaction converted into the carbon dioxide can be collected effectively. The electric power generation efficiency of the gasification-power-generation system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon-dioxide separation-and-recovery apparatus equipped with the gasification-power-generation system.    Inlet port gas pipe path (1)    Shift reaction device by-pass line (2)    Shift reaction device (5,7,11)    Evaporator (6,9,13)    Carbon-dioxide absorption column (37)
NOVELTY - The generator has an ash cleaning port fixed on an upper part of a furnace ash chamber. A lower material opening is fixed above a middle part of the furnace ash chamber. An air pipe is sleeved on an air inlet flange. A fire grate is fixed on a fire grate supporting plate. An electric heating rod is arranged on a sleeve. An outlet of the air pipe is fixed on a lower part of the furnace ash chamber. A safety valve is fixed on an upper part of the furnace ash chamber.    USE - Biomass fuel gas generator.    ADVANTAGE - The generator is simple in structure, simple to operate, convenient to use and environment-friendly. The generator has high thermal efficiency, stable furnace temperature and high furnace gas tar content.
NOVELTY - The apparatus has a rotational axis (42) provided in an inner wall of a frame (14) along an upper direction of a notch part i.e. clearance gap (20), in parallel with a carrier (16) while connecting an L-shaped flat plate i.e. plane board (40), with the rotational axis. Gravity of the flat plate is smaller than gravity of coating liquid (18). A liquid level sensor e.g. electrostatic capacitive type liquid level sensor, detects liquid level height (44) of the coating liquid along the upper direction of the notch part. A wall controller controls movement of a movable wall.    USE - Apparatus for coating a liquid composition coating film on a carrier during manufacture of a sheet-like device e.g. fuel cell, primary/secondary battery and green sheet.    ADVANTAGE - The rotational axis is provided in the inner wall of the frame along the upper direction of the notch part in parallel with the carrier while connecting the flat plate with the rotational axis, so that utilization efficiency of coating liquid with respect to the amount of injection materials can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a coating apparatus.'(Drawing includes non-English language text)'    Frame (14)    Carrier (16)    Coating liquid (18)    Clearance gap (20)    Plane board (40)    Rotational axis (42)    Liquid level height (44)
NOVELTY - Method for saccharifying biomass involves (a) adding enzyme to lignocellulosic biomass and saccharifying biomass, and (b) (i) adding alkali to saccharification reaction slurry, subjecting the mixture to solid-liquid separation, and removing enzyme adsorbed to saccharification reaction residue and obtaining enzyme recovered liquid or (ii) adding alkali to saccharification reaction residue obtained by solid-liquid separation of saccharification reaction slurry and removing enzyme, where the addition of alkali increases pH of enzyme.    USE - The method is useful for saccharifying biomass, preferably lignocellulosic biomass.    ADVANTAGE - The method saccharifies biomass containing high lignin content and enables high recovery of enzymes. The method is cost-effective as recovered enzyme is recycled.
NOVELTY - A pot-type hydrogenated generator (100) comprises pot part (1) for generated water which stores natural water, base part (2) which supplies electricity to pot part and has ring-shaped electrode connector (21) and punctate electrode connector (24), water tank room, reaction chamber, communicating port formed between water tank room and reaction chamber, electrode plate which is made of polymer film and contains porous metal plate or metal net body, spring with electrical conductivity, and electrode board with electrode terminals.    USE - The device is for producing hydrogenated water for drinks (claimed).    ADVANTAGE - The water tank and the polymer film cannot be easily damaged, cleaning of anode and cathode electrodes can be simultaneously performed, hydrogen gas is efficiently dissolved, and hydrogen can be effectively produced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the pot part and base part of the pot-type hydrogenated water generator.    Pot part (1)    Base part (2)    Ring-shaped electrode connector (21)    Punctate electrode connector (24)    Pot-type generator (100)
NOVELTY - Activated sludge comprises gene fragment amplified by PCR using at least one primer set chosen from (a) primer set comprising 19 and 18 base pair sequences (SEQ ID NOs: 7 and 8) fully defined in the specification, (b) primer set comprising 21 and 21 base pair sequences (SEQ ID NOs: 9 and 10) fully defined in the specification, and (c) primer set comprising 19 and 19 base pair sequences (SEQ ID NOs: 11 and 12) fully defined in the specification.    USE - The activated sludge is useful for processing wastewater from paper plant (claimed).    ADVANTAGE - The activated sludge treats wastewater with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing wastewater from paper plant, which involves adding activated sludge to wastewater from paper plant and heating the product using oven, until the dry weight ratio reaches 5% or more.
NOVELTY - Producing an aqueous solution of fulvic acid and humic acid, comprises: providing an organic compost material (502); combining the organic compost material with a crop (504); heating the organic compost material (506); combining the organic compost material with water (508); and extracting an aqueous liquid (510), where the aqueous liquid comprises humic acid and fulvic acid.    USE - The method is useful for producing an aqueous solution of fulvic acid and humic acid.    ADVANTAGE - The method: avoids the harmful effects of the mining process on the environment; is operated in a cost effective manner; does not require the use or generation of new decomposition microbes or microorganisms; does not require the use of acids or bases to leach out the humic substances; and allows for commercial and large-scale production of fulvic acid and humic acid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of producing the aqueous liquid containing humic acid and fulvic acid.    Providing an organic compost material (502)    Combining the organic compost material with a crop (504)    Heating the organic compost material (506)    Combining the organic compost material with water (508)    Extracting an aqueous liquid (510)
NOVELTY - System comprises pipeline and constant volume pump assembly, where the pipeline is connected sequentially with constant volume pump assembly of hybrid component and harmonic components. The pump assembly comprises gasoline, methanol gasoline and additive constant volume pump. The harmonic component comprises harmonic tank and circulation pipeline. The two ends of circulation pipeline are connected with mixing tank input end and output end of controller.    USE - The system is useful in production of methanol gasoline.    ADVANTAGE - The system is simple, cost-effective, rapid and accurate, and improves production efficiency.
NOVELTY - A fluorous Dendron compound (I) is new.    USE - For nonstick frying pans, optics, electronics, displays, fuel and solar cells, rechargeable batteries, drugs, and medical application.    ADVANTAGE - The design of compound is environmentally friendly and efficient fluorous phase based on dendritic architectures.    DETAILED DESCRIPTION - A fluorous Dendron compound of formula (I) is new.    R1=1-6C alkyl;    R5=1-9C perfluoroalkyl group and optionally containing 1 or 2 ether oxygens;    R6-R8=H or group of formula -O-CH(F)2-CH(F)(OR5)-H.    Provided that: at least two of R6-R8 are -O-CH(F)2-CH(F)(OR5)-H. An INDEPENDENT CLAIM is included for producing the fluorous dendron (I).
NOVELTY - Fermentation tank comprises container for accommodating animal carcasses, where the container opening is provided with a sealing cover, an air pipe and a valve unit. The air pipe and the valve unit are connected with the sealing cover. The lower end of the container sidewall of inner cavity is provided with a concave baffle plate.    USE - The tank is useful for fermenting animal carcasses.    ADVANTAGE - The fermentation tank first discharges internal gas with odor to prevent people from symptoms, preferably vomiting and nausea.    DETAILED DESCRIPTION - Fermentation tank comprises container for accommodating animal carcasses, where the container opening is provided with a sealing cover, an air pipe and a valve unit. The air pipe and the valve unit are connected with the sealing cover. The lower end of the container sidewall of inner cavity is provided with a concave baffle plate. The concave baffle plate divides container inner cavity of the container into a first cavity and a second cavity. The baffle plate comprises holes. The second cavity at the bottom of the container and second lumen connected with a fan are arranged in the sidewall of the container.
NOVELTY - Production device for transesterification of distributed vegetable oil comprises a reaction kettle, a water washing pot, a catalyst recovering pot, a dryer, a warm water storing tank, a conduction oil heating tank, a reaction cycle pump, an air pump, a material pump and a conduction oil pump. The warm water storing tank and conduction oil heating tank are respectively provided with an electric heater. The top of the water washing pot is provided with a material inlet pipe and a warm water inlet pipe, and the bottom is provided with an air dispersing pipe and a material outlet pipe.    USE - Used as a production device for transesterification of distributed vegetable oil.    ADVANTAGE - The device is integrated to realize homogeneous catalysis and heterogeneous separation, and to improve the yield of the vegetable oil; is light weight and simple; and is convenient to process the dispersed raw material in a timely manner.
NOVELTY - Pre-treating non-grain biomass, comprises (a) removing the foreign matters from the biomass, washing, crushing into powder; (b) adding clean water, boiling to sterilize, artificially or natural freezing; (c) crushing the frozen biomass, adding cellulase, adjusting the pH value and the solid-to-liquid ratio; (d) continuously grinding; (e) preserving heat to continue enzymolysis until inactivate the cellulase; and (f) filtering, and using the filtrate for the alcoholic fermentation, the filter residue being original lignin.    USE - The method is used for pre-treating non-grain biomass. The biomass is straw, wood or weed (all claimed).    ADVANTAGE - The method above is capable of reducing the secondary combination between the lignin and the cellulose, thus improving the effect of the cellulose without generating poisonous matter to prevent the growth of the alcoholic fermentation microorganism.
NOVELTY - A microwave biomass pyrolysis continuous reaction device comprises a microwave generator (1), a reactor (7), and a product separation device. The reactor is set in a cavity (6) connecting microwave generator with a waveguide (2). The reactor comprises a feeding section having a feeding hole (8), a reaction section, and a discharging section having a discharging hole (9) to discharge the generated solid coke.    USE - A microwave biomass pyrolysis continuous reaction device.    ADVANTAGE - The device increases biomass pyrolysis efficiency and improves yield and quality of liquid biological oil. It has a simple structure and a rational design.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass pyrolysis continuous reaction, comprising:    (A) using microwave generator to generate microwave;    (B) feeding biomass in a reactor at 10-50 kg/hour with a dwelling time of 1-5 minutes, and heating biomass with microwave; and    (C) leading the reaction product enters to a product separation device.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the device.    Microwave generator (1)    Waveguide (2)    Cavity (6)    Reactor (7)    Feeding hole (8)    Discharging hole (9)
NOVELTY - A Penicillium oxalicum (CGMCC-4357), is new.    USE - The P.oxalicum is useful for preparing fermented product. The method (M1) is useful for producing cellulose degrading enzyme. The method (M1) is useful for saccharifying straw cellulose (all claimed).    ADVANTAGE - The P.oxalicum is simple, stable and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M1) for producing cellulose degrading enzyme, involves inoculating the P.oxalicum in liquid enzyme production culture medium to obtain endoglucanase, exoglucanase or betaglucosaccharase, where the liquid enzyme production culture medium comprises carbon source, nitrogen source, inorganic salt and water; # (2) method (M2) for saccharifying straw cellulose, involves hydrolyzing straw cellulose using the cellulose-degrading enzymes to saccharify the straw cellulose, where reaction solution comprises phosphoric acid buffer solution with pH of 6 and concentration of 0.05 mol/l; and # (3) fermented product prepared from the P.oxalicum.
NOVELTY - A flue gas purifying device comprises gas inlet pipe (1) and gas outlet pipe (2) installed in upper part of purifying chamber (3); top part of purifying chamber arranged with flue gas diffusing cavity (4) communicating with gas inlet pipe; side wall of purifying chamber arranged with filtering cylinder (5) vertical to level; opening of filtering cylinder facing downwards; and filter element (6) installed in filtering cylinder; and purifying chamber filled with stuffing (7), and bottom part arranged with water outlet (8).    USE - Flue gas purifying device.    ADVANTAGE - The device can provide gas flue fuel with little pollution and high calorific value; and the fuel full utilizes organic waste, e.g. leaf, sawdust, crop straw and seed hull, saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the flue gas purifying device.    Gas inlet pipe (1)    Gas outlet pipe (2)    Purifying chamber (3)    Flue gas diffusing cavity (4)    Filtering cylinder (5)    Filter element (6)    Stuffing (7)    Water outlet (8)
NOVELTY - Regenerating deacidification catalyst used in purifying biodiesel comprises contacting the deacidification catalyst to be regenerated with 1-4C low carbon alcohol, to remove colloidal material absorbed in the deacidification catalyst and replace the moisture absorbed in the deacidification catalyst, where the deacidification catalyst is solid acid.    USE - Method for regenerating deacidification catalyst used in purifying biodiesel (claimed).    ADVANTAGE - The method can prolong service life of the deacidification catalyst; ensures long-term running of the deacidification system; saves human power, material and cost; and reduces production cost of the biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for purifying biodiesel comprising contacting biodiesel with 1-4C low carbon alcohol in the presence of the deacidification catalyst to esterify the free fatty acid contained in the biodiesel. The method further comprises regenerating the inactivated deacidification catalyst.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of a method for regenerating deacidification catalyst (Drawing includes non-English language text).
NOVELTY - Using ethylic acid and methanol to prepare fuel ethanol comprises performing supercritical esterification for ethylic acid and methanol firstly to prepare methyl acetate; and performing hydrogenation reaction for methyl acetate and hydrogen to prepare fuel ethanol.    USE - Method for using ethylic acid and methanol alcohol to prepare fuel ethanol (claimed).    ADVANTAGE - The method uses supercritical esterification. The reaction time is short, where no catalyst is used. Conversion rate of the ethylic acid in esterification is high. Copper zinc aluminum-rare earth compound catalyst is used for performing hydrogenation reaction. Compared with the traditional copper zinc aluminum catalyst, the method is capable of increasing conversion of methyl acetate and yield of ethanol. The hydrogenation reaction efficiency is high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fuel ethanol prepared by above cited method.
NOVELTY - Method for promoting enzymatic complex to catalyze and degrade straw through active culture medium, involves (a) crushing the straw to obtain the straw powder and sieving the powder to obtain coarse powder, (b) culturing Phanerochaete chrysosporium in liquid medium to obtain enzymatic complex liquid, (c) adding the obtained liquid to the coarse powder and adding active culture medium to the solution, and (d) reacting the solution.    USE - The method is useful for promoting enzymatic complex to catalyze and degrade straw through active culture medium.    ADVANTAGE - The method improves enzymolysis rate of lignin in straw, and is simple, cost-effective and environmentally-friendly.
NOVELTY - Preparing microorganism oil by increasing oil-producing microbial fermentation involves negative ion surface active agent (0.5-4 g/l) and/or its analogue in culture medium during the process of fermenting to produce microbial cell, where the negative ion surface active agent is selected from oleate, oleate, n-caprylate, n-caprylic acid ester, 1-octyl sulfonate, lignosulfonate; the negative ion surface active agent analogue is fatty acid of long chain, polarity fat and/or aliphatic ester of long chain.    USE - For preparing microorganism oil (claimed), useful for preparing biodiesel.    ADVANTAGE - The method promotes growth of oil-producing microbial cell and the accumulation of the oil, thus the method enhances the economic feasibility of microorganism oil in biodiesel oil raw material.    DETAILED DESCRIPTION - Preparing microorganism oil by increasing oil-producing microbial fermentation involving negative ion surface active agent (0.5-4 g/l) and/or its analogue in culture medium during the process of fermenting to produce microbial cell, where the negative ion surface active agent is selected from oleate, oleate, n-caprylate, n-caprylic acid ester, 1-octyl sulfonate, lignosulfonate; the negative ion surface active agent analogue is fatty acid of long chain, polarity fat and/or aliphatic ester of long chain. The cultivating way of producing microbial cell is batch type fermentation, two phases batch type fermentation, flowing batch type fermentation or continuous fermentation.
NOVELTY - Fermentation device comprises a main unit of fermentation tank (1), forced ventilation device (3) which is connected at bottom of the fermentation tank, filter layer which is present at bottom of the ventilation device, percolate collecting tank (4) which is present at lower portion of the filter layer, and waste gas treatment system (2) which is connected with top of the main unit of fermentation tank through a pipe.    USE - The fermentation device is useful for composting sludge (claimed).    ADVANTAGE - The fermentation device is environmentally-friendly and suitable for small sewage treatment plant, and processes the sludge at a high rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for composting sludge, which involves (a) adding organic conditioner to the to-be-processed sludge to adjust the water content and carbon and nitrogen ratio, and mixing the sludge and the organic conditioner, (b) inoculating composite microorganism suspension and surfactant solution in the mixture, (c) adding the mixture obtained in step (b) into the fermentation device, and subjecting the mixture to primary fermentation by starting forced ventilation device in the fermentation device for 7-10 days, and (d) subjecting the obtained product to secondary fermentation by natural ventilation for 20-30 days.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of fermentation device.    Main unit of fermentation tank (1)    Waste gas treatment system (2)    Forced ventilation device (3)    Percolate collecting tank (4)    Gravel layer (12)
NOVELTY - Fermentation enhancing agent comprises (in parts weight): wheat bran (20-28), marsh gas fermenting additive (35-40), lime (5), ammonium hydrogen carbonate (1-3), zinc sulfate (1-2), and carbon powder or coal powder (5-10).    USE - The fermentation enhancing agent is useful for producing marsh gas (claimed).    ADVANTAGE - The fermentation enhancing agent is cost-effective and environmentally-friendly and rapidly produces high amounts of marsh gas with reduced fermentation time and waste, and has high fermentation conversion rate for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing marsh gas, which involves adding (in parts weight) fermentation enhancing agent (1-4) to the above raw material (100-400) in the marsh gas pool or marsh gas tank, and adding waste dry battery (4-20) into the tank containing raw material.
NOVELTY - The device has charging circuit board which is provided in shell (1). A battery box is provided with rechargeable battery. The shell is provided with charging plug which is connected with circuit board which is connected with battery. The amplifying circuit and the control chip are connected with the oxygen sensor. The shell is provided with a button (5), LCD screen (10) and air inlet hole (9). The button is connected with control chip, sensor, oxygen sensor, carbon monoxide sensor and hydrogen sulphide sensor through the air inlet hole.    USE - Device for monitoring coal mining environment.    ADVANTAGE - The mining environment can be monitored effectively, so that safety of the workers can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the device for monitoring coal mining environment. (Drawing includes non-English language text)    Shell (1)    Button (5)    Air inlet hole (9)    LCD screen (10)
NOVELTY - A resonance oxyhydrogen machine comprises electrolytic tank and group of voltage electrolytic circuits, each group being electrically connected with a battery power supply, and is provided with first infinite resonant cavity electrically connected with first transistor and second transistor electrically connected with second infinite resonant cavity. The first infinite resonant cavity, second transistor and second infinite resonant cavity are connected in parallel.    USE - A resonance oxyhydrogen machine.    ADVANTAGE - The machine can not only save electricity and produce gas quickly at low temperature, but also controls the size and number of the produced gas.    DETAILED DESCRIPTION - Resonance oxyhydrogen machine comprises electrolytic tank and group of voltage electrolytic circuits, each group being electrically connected with a battery power supply, and is provided with first infinite resonant cavity electrically connected with first transistor and second transistor electrically connected with second infinite resonant cavity. The first infinite resonant cavity, second transistor and second infinite resonant cavity are connected in parallel. Each group of voltage electrolytic circuit is also provided with a buffering loop as 2 input ends of the electrolytic tank which are electrically connected with each group of voltage electrolytic circuit and are the positive and negative electrode ends. The positive electrode end is zinc oxide bar which is inserted into an end of the electrolytic tank and is opposite to the oxygen outlet. The negative electrode end is a carbon rod which is inserted into the other end of the electrolytic tank and is opposite to the hydrogen outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a voltage electrolytic circuit diagram.
NOVELTY - Acid electrolytic method uses an acid aqueous solution as fuel with a solid polymer electrolyte membrane that produces hydrogen. It specifically comprises applying a voltage across the anode and cathode with the anode side of the electrolyzing electrode more than 2 M of the formic acid solution. The anode catalytic oxidation reaction uses the electrolytic current to produce hydrogen on the cathode at temperatures of 20-70 degrees C.    USE - Acid electrolytic method for producing hydrogen.    ADVANTAGE - The electrolytic voltage is low, thus reducing the energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the acid electrolysis hydrogen device.
NOVELTY - The apparatus (200) comprises a coolant supply part (210), a supply line (220), a heat exchanger (230), a reproducing unit (240) and a sensor (250), where the coolant supply part supplies a refrigerant for heat exchange purpose with the natural gas. The multiple heat exchangers are installed at the former branch line, where cold natural gas is supplied from the supply line with the refrigerant. A reproducing unit is selectively supplies regeneration fluid in order to remove carbon dioxide.    USE - Apparatus for producing liquefied natural gas.    ADVANTAGE - The apparatus comprises coolant supply part, supply line, heat exchanger, reproducing unit and sensor, and hence ensures low production cost of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus. (Drawing includes non-English language text).    Apparatus (200)    Coolant supply part (210)    Supply line (220)    Heat exchanger (230)    Reproducing unit (240)    Sensor (250)
NOVELTY - A semiconductor catalyst comprises cadmium selenide or salts, complexes of vulcanized cadmium quantum dot, and cobalt, nickel or iron as raw materials.    USE - Semiconductor catalyst for an optical catalytic hydrogen production system.    ADVANTAGE - The method enables preparing the catalyst in an efficient, stable and simple manner with low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing semiconductor catalyst, which involves adding water-soluble cadmium selenide or cadmium sulfide quantum dot in a transparent reactor, adding electron body in the reactor or organic solution to obtain the mixed solution A, adding salt or complex solution in the cobalt, nickel or iron in the mixed solution A to obtain mixed solution B, adding water or water in the mixed solution B, dissolving mixed solvent of water and organic solvent in water to obtain mixed solution C, adjusting pH value to be 4 so as to obtain mixed liquid D, introducing inert gases to the reactor filled with the mixed solution D, or the reactor with vacuum transparent mixed solution D, and centrifuging the precipitate for light catalytic hydrogen production system of catalyst    (2) an optical catalytic hydrogen production system containing semiconductor catalyst.
NOVELTY - Natural gas reforming catalyst comprising a metal core and rhodium deposited on the metal core, is new.    USE - The reforming catalyst is useful: in the natural gas reformer; and for producing hydrogen from hydrocarbon and water (all claimed).    ADVANTAGE - The reforming catalyst reduces a potential for ammonia formation during hydrogen reforming.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the natural gas reforming catalyst; and    (2) a natural gas reformer comprising a hydrocarbon inlet, the reforming catalyst for generating hydrogen from hydrocarbon and water, and a hydrogen outlet.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of a core-shell catalyst for natural gas reforming.    Core-shell reforming catalysts (10)    Metal core (12)    Rhodium shell. (14)
NOVELTY - The method involves pre-treating plant biomass by steam explosion (10) in a reactor at 160-260 degrees C and hydrolyzing (20) the treated material by hydrolytic bacteria with or without addition of cellulase enzymes, in conjunction or not with xylanase enzymes. The hydrolyzed material is anaerobic digested (30) for producing biogas, where all processes are carried out in separate reactors.    USE - Method for producing biogas from plant biomass in reactors operated in semi-continuous or continuous process.    ADVANTAGE - The method involves pre-treating plant biomass by steam explosion in a reactor at predetermined temperature, and thus provides biogas from plant biomass in a simple manner with or without addition of cellulase enzymes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for carrying out the process for producing biogas, which includes a reactor for pretreatment of plant biomass by steam explosion, another reactor for hydrolysis of the treated material by hydrolytic bacteria, with or without addition of cellulase enzymes, and a third reactor for anaerobic digestion of the hydrolyzed material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a system and process of producing biogas from biomass. (Drawing includes non-English language text).    Steam explosion (10)    Hydrolysis reactor (20)    Anaerobic digestion (30)
NOVELTY - The method involves treating plant biomass by steam explosion (10) at 160-260 degrees C, where the treated plant biomass is hydrolyzed and anaerobic digested (20) by using anaerobic bacteria. The plant biomass treatment and hydrolysis processes are carried out in separate reactors. The anaerobic digestion is accomplished in a single reactor for producing biogas and digested biomass. The hydrolysis and digestion are carried out in separate reactors.    USE - Method for producing biogas from lingo cellulosic materials.    ADVANTAGE - The method involves treating plant biomass by steam explosion, where the treated plant biomass is hydrolyzed and anaerobic digested by using anaerobic bacteria, and thus provides biogas in a simple manner without addition of catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing biogas, which comprises a reactor for treating plant biomass by steam explosion, and another reactor for hydrolysis and anaerobic digestion of the treated material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a system and process of producing biogas from biomass. (Drawing includes non-English language text).    Steam explosion (10)    Anaerobic digestion reactor (20)
NOVELTY - The method involves laminating hydrogen-ion-conductive macromolecule on a film. A catalyst layer is formed in two sides of the film by hot-pressing process at fixed temperature. A hydrophilic solvent is coated on the catalyst layer after formation of catalyst slurry. The catalyst slurry is stored in dispersion media. Drying process is performed on the film to dry. The film is made of sulfonic acid group, carboxyl group, phosphate group, imide group, sulfone-imide group, sulfonamide group, hydroxy group or a hydrocarbon polymer film.    USE - Method for manufacturing a polyelectrolyte membrane fuel cell-electrode assembly.    ADVANTAGE - The method enables controlling glass transition temperature of a hydrocarbon membrane by utilizing decal process of a hydrocarbon membrane electrode assembly in an effective manner. The method enables avoiding deterioration effect of the film while processing. The method ensures simple manufacturing process of a polyelectrolyte membrane fuel cell-electrode assembly. The method enables maintaining temperature level during manufacturing process. The method enables improving productivity and processing efficiency of the polyelectrolyte membrane fuel cell-electrode assembly.    DETAILED DESCRIPTION - The hydrophilic solvent is selected from alcohol, ketone, aldehyde, carbonate, carboxylate, carboxylic acid and amide.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing a polyelectrolyte membrane fuel cell-electrode assembly.'(Drawing includes non-English language text)'
NOVELTY - A process, comprises: forming, in a cathodic compartment, hydrogen gas, where the cathodic compartment contains a cathode; forming, in a catalyst compartment, oxygen gas by a one or more chemical reactions involving a catalyst; and forming, in an anodic compartment, an electric current, where the anodic compartment contains an anode electrically interconnected with the cathode, where the anodic and cathodic compartments are in fluid communication and the catalyst compartment is in fluid communication with one or both of the anodic and cathodic compartments.    USE - The process is useful for generating hydrogen, oxygen or both from water (claimed).    ADVANTAGE - The process efficiently generates one or both of hydrogen and oxygen from water that is substantially free of expensive sacrificial reagents, high temperatures and/or pressures, and/or large electrical overpotentials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an electrochemical device, comprising: an anodic compartment having an anode; a cathodic compartment having a cathode; and a catalyst compartment containing a catalyst, where the anodic and cathodic compartments are in fluid communication and the catalyst compartment is in fluid communication with at least one of the anodic and cathodic compartments, where the anode and cathode are electrically interconnected.
NOVELTY - A blanket comprises a material having the following properties: thermal insulation, such that the blanket is capable of withstanding temperatures of 100-1000 degrees C; gas impermeability; and flexibility, such that the blanket can be folded over on itself for storage; where the blanket is configured to conformally cover a combusting biomass to facilitate pyrolysis or drying of the biomass.    USE - The blanket and method are useful for producing biochar or dry biomass (claimed).    ADVANTAGE - The blanket can be efficiently used as a portable and reusable kiln for pyrolyzing biomass into biochar or drying biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method, comprising: (a) combusting a biomass at a temperature sufficient to initiate pyrolysis or drying of the biomass; (b) covering the biomass with the blanket, where the temperature of the biomass covered by the blanket can be controlled and is sufficient to pyrolize or dry the biomass, and where air from outside the blanket only reaches the biomass in a controlled manner; and (c) maintaining the temperature of the biomass covered by the blanket for a sufficient time to produce biochar or dry biomass.
NOVELTY - Producing mechanically stabilized polyazole, comprises: (a) treating at least one polyazole having at least one amino group in a repeating unit, with a solvent comprising (i) at least one strong acid and (ii) at least one stabilizing reagent (0.01-30 wt.%); and (b) carrying out stabilization reaction immediately and/or in a subsequent step, by heating to a temperature of greater than 25 degrees C, using a stabilizing reagent comprising at least one polyvinyl alcohol.    USE - The mechanically stabilized polyazole is useful for producing a membrane, which is useful for producing a membrane-electrode unit. The membrane-electrode unit is useful for producing a fuel cell (all claimed).    ADVANTAGE - The method produces the polyazole exhibiting high conductivity and excellent mechanical stability. The membrane exhibits long-term stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a membrane comprising at least one mechanically stabilized polyazole, which is obtainable by the above method; and    (2) a membrane-electrode unit comprising at least one above membrane.
NOVELTY - An article comprises gaseous fuel mixture (40) containing 30-95 vol.% of hydrogen and 5-70 vol.% of methane, based on the total volume of the mixture. The article consists of refillable gas cylinder (10) comprising non-corrosive container (20) and a valve (30) connected to the container. The cylinder can be used with hydrogen-containing gas. The gaseous fuel mixture is provided within the non-corrosive container.    USE - Article used as heating source (claimed).    ADVANTAGE - The article provides environmentally-friendly heating method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for providing environmentally-friendly heating source.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the refillable and non-corrosive gas cylinder containing gaseous fuel mixture.    Gas cylinder (10)    Non-corrosive container (20)    Valve (30)    Gaseous fuel mixture (40)
NOVELTY - A hydrocarbon refrigerant composition comprises (vol.%): propylene (preferably 50-65); propane (preferably 30-45); and isobutene (preferably 5-10).    USE - In refrigerant composition, and detergent composition (claimed). The composition is also used for cleaning semiconductor chips, and motherboards.    ADVANTAGE - The hydrocarbon composition is used as a refrigerant having a relatively high ignition temperature with minimal environmental impact.
NOVELTY - Producing a volatile biomass product, comprises grinding a biomass feedstock to produce ground biomass particles, dispensing the ground biomass particles into thin sheets, subjecting the ground biomass to sequential or concurrent ramps of temperature and pressure shocks, and selectively collecting at least one group of volatile compounds as it is released from the biomass.    USE - The method is useful for producing a volatile biomass product. The system is useful for converting biomass to biofuel (all claimed). The method is useful for generating chemical intermediates from biomass using a pyrolysis reactor.    ADVANTAGE - The method enables a high-yield release of useful volatile bio-intermediary compounds, and improves the thermal conductivity of carbon, which serves to efficiently transmit heat energy needed to break down the biomass to the next stage in its decomposition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for converting biomass to biofuel, comprising means for grinding biomass into particles, means for dispensing the ground biomass particles into thin sheets, means for applying pressure shocks to the ground biomass, means for applying temperature ramps to the ground biomass, and means for collecting at least one group of volatile components as it is released from the biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a system for biomass conversion.    Anvil (74)    Openings (75a)    Center opening (75c)    Feedthroughs. (80)
NOVELTY - The system has a hydrogen tank (140) that is provided with a hydrogen storage material. The vacuum degree adjusting devices (193,196) adjust the vacuum degree of the air layers (190,192), respectively. The amount of hydrogen released by the hydrogen storage material is adjusted, while adjusting the vacuum degree of air layers, and supplyamount and dissipation amount of heat from thermal-medium layers. A fuel cell of a fuel cell module (150) produces electric power using the released hydrogen.    USE - Fuel cell system used as fuel cell hot water supply cogeneration system installed in household and public bath facility.    ADVANTAGE - The heating and cooling of the hydrogen tank are performed simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hot-water supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the fuel cell hydrogen tank integrated unit.    Fuel cell hydrogen tank integrated unit (110)    Hydrogen tank (140)    Fuel cell module (150)    Air layers (190,192)    Vacuum degree adjusting devices (193,196)
NOVELTY - Use of calcium oxide-cement kiln dust at a concentration of 1.5-20 g/l, for anaerobic granulation of palm oil mill effluent, is claimed.    USE - The calcium oxide-cement kiln dust is useful for anaerobic granulation of palm oil mill effluent which is useful for producing biogas including methane (all claimed).    ADVANTAGE - The process utilizes upflow anaerobic sludge bed reactor which increases the production of the biogas with low operating costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biogas from palm oil mill effluent using the calcium oxide-cement kiln dust, comprising: inoculating palm oil mill effluent sludge in a reactor; conducting anaerobic digestion on the sludge; and conducting anaerobic granulation of palm oil mill effluent.
NOVELTY - The solid oxide fuel cell apparatus (1) has a fuel gas supply unit to supply fuel gas to a fuel electrode layer (90), while a oxidizing agent supply unit provides oxidizing agent to an air electrode layer (92). A controller (110) monitors and controls the driving state of the solid oxide fuel cell apparatus. The controller performs a refresh process that supplies fuel gas to the fuel electrode layer to obtain predetermined restoration acceleration conditions upon determining that a fuel cell (84) is in an oxide excessive state.    USE - Solid oxide fuel cell apparatus.    ADVANTAGE - Prevents the fall of the electric power generation performance of the in the operation of the solid oxide fuel cell apparatus, since the controller executes refresh process in which fuel gas is supplied to fuel electrode layer of fuel cell to obtain predetermined restoration conditions of the fuel cell exists in an oxide excessive state, thus ensuring high electric power generating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the solid oxide fuel cell apparatus. (Drawing includes non-English language text)    Solid oxide fuel cell apparatus (1)    Fuel cell module (2)    Auxiliary machine (4)    Generator room (10)    Control box (52)
NOVELTY - Producing ethanol, comprises: supplying feed stock into a first container, where the feed stock contains at least one type of sugar; measuring the sugar concentration of the feed stock; adjusting the sugar concentration of the feed stock to fall within a predetermined range; introducing the feed stock from the first container into a bio-reactor comprising a second container and at least one substrate disposed within the second container; and fermenting.    USE - The method is useful for producing ethanol (claimed), which is used as biofuel.    ADVANTAGE - The method utilizes the bioreactor that allows for the maintenance of a constant concentrated microbial population, and enhanced the ethanol production by stabilizing microbial populations, thus improving the overall efficiency, while reducing costs and space requirements, as compared with conventional ethanol production process.    DETAILED DESCRIPTION - Producing ethanol, comprises: supplying feed stock into a first container, where the feed stock contains at least one type of sugar; measuring the sugar concentration of the feed stock; adjusting the sugar concentration of the feed stock to fall within a predetermined range; introducing the feed stock from the first container into a bio-reactor comprising a second container and at least one substrate disposed within the second container, where the substrate is inoculated with at least one microbial population, preselected for fermentation capability, and the microbial population propagates on the surface of the substrate; and fermenting the feed stock within the bio-reactor to generate ethanol.
NOVELTY - The system has combustion chamber (84) with space in which several oxidizing agent gas pipe path (78) is accommodated. The end of oxidizing agent waste gas supply pipe (86) and end of fuel waste gas supply pipe (88) are positioned from side of oxidizing agent gas discharge chamber (76b). The pipe line length to which fuel waste gas exit side of fuel waste gas supply pipe protrudes in combustion chamber is made long length than pipe line length to which oxidizing agent waste gas exit side of oxidizing agent waste gas supply pipe protrudes in combustion chamber.    USE - Heat processing system for fuel cell system installed in vehicle.    ADVANTAGE - Since the end of oxidizing agent waste gas supply pipe and end of fuel waste gas supply pipe are positioned from side of oxidizing agent gas discharge chamber, the loss of the heat energy from combustor can be suppressed effectively. The size of the heat processing system can be reduced. The manufacturing cost of the heat processing system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the heat exchanger. (Drawing includes non-English language text)    Oxidizing agent gas discharge chamber (76b)    Oxidizing agent gas pipe path (78)    Combustion chamber (84)    Oxidizing agent waste gas supply pipe (86)    Fuel waste gas supply pipe (88)
NOVELTY - A carbon-dioxide-recycling apparatus consists of a hydrogen source supplier (101) for supplying a hydrogen source chosen from hydrogen and substance containing hydrogen, a fuel production unit (103) to produce fuel including carbon, and a fuel separator (104). Carbon dioxide emitted from a fuel-use apparatus (102) using chemical reaction of fuel including carbon, is chemically reacted with hydrogen of hydrogen source using a photocatalyst irradiated with light. The fuel separator separates fuel in the fuel production unit from chemical-reaction product.    USE - Apparatus is used for recycling carbon dioxide emitted from fuel-use apparatus e.g. fuel cell (claimed). Can also be used for recycling carbon dioxide emitted from thermal power stations.    ADVANTAGE - The apparatus efficiently reduces carbon dioxide emitted from a source, by economical recycle process. Since a photocatalyst is used, the use of electric power is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the carbon-dioxide recycling apparatus. (Drawing includes non-English language text)    Hydrogen source supplier (101)    Fuel-use apparatus (102)    Fuel production unit (103)    Fuel separator (104)
NOVELTY - The system (10) has an electrolysis apparatus (12) to electrolyze water and generate oxygen and high-pressure hydrogen. A piping (20) emits hydrogen from electrolysis apparatus. A gas-liquid separation apparatus (22) separates moisture content in hydrogen. A drain line (26) emits water from separation apparatus. A back pressure valve (94) and a solenoid valve (98) are positioned at drain line. A fault detection apparatus (102) detects pressure of drain line and detects failure of back pressure valve, after closing the opening of solenoid valve by depressurization.    USE - Water-electrolysis system used for manufacturing hydrogen used as fuel gas in fuel battery.    ADVANTAGE - Since fault detection apparatus detects the pressure of drain line after closing the opening of solenoid valve by depressurization and detects the failure of back pressure valve when the pressure of drain line is raised, the failure of the back pressure valve can be detected reliably at a simple economical structure and process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling water-electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water-electrolysis system. (Drawing includes non-English language text)    Water-electrolysis system (10)    Electrolysis apparatus (12)    Piping (20)    Gas-liquid separation apparatus (22)    Drain line (26)    Back pressure valve (94)    Solenoid valve (98)    Fault detection apparatus (102)
NOVELTY - The system (10) has an electrolysis apparatus (12) to electrolyze water and generate oxygen and high-pressure hydrogen. A piping (20) emits hydrogen from electrolysis apparatus. A gas-liquid separation apparatus (22) separates moisture content in hydrogen. A drain line (26) emits water from separation apparatus. A heating apparatus (92) raises the water temperature in gas-liquid separation apparatus before draining the water on drain line from the gas-liquid separation apparatus.    USE - Water-electrolysis system used for manufacturing hydrogen used as fuel gas in fuel battery.    ADVANTAGE - Since the heating apparatus raises the water temperature in gas-liquid separation apparatus before draining the water on drain line from the gas-liquid separation apparatus, the solubility of hydrogen into high-pressure water can be reduced, and the amount of dissolved hydrogen in drain line can be reduced effectively. Hence the quantity of the hydrogen vaporized due to the rapid pressure drop at drain line can be reduced, and the performance and durability of the device are improved. Hence the water-electrolysis process can be performed in an economical and efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling waste-water in water-electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water-electrolysis system. (Drawing includes non-English language text)    Water-electrolysis system (10)    Electrolysis apparatus (12)    Piping (20)    Gas-liquid separation apparatus (22)    Drain line (26)    Heating apparatus (92)
NOVELTY - The hydrogen gas generator (10) has an anode (18), a cathode, a housing (14) that has an internal cavity, and a perforated wall (30) provided within the cavity. The perforated wall is provided near a cavity end electrically connected to the anode or cathode, and separates an end portion of cavity from the main portion of the cavity. The water in the housing is allowed to extend continuously from the main portion of the cavity through the perforated wall and into the end portion of the cavity.    USE - Hydrogen gas generator for production of hydrogen gas.    ADVANTAGE - Provides a cylindrical hydrogen gas generator which produces hydrogen gas more efficiently than the stacked plate generators. Allows the current to flow through the brine salt solution producing chemical reaction when a voltage differential is placed between the anode and cathode plates. Allows production of hydrogen gas by applying the sufficient voltage differential between the anode and cathode. Allows the brine to flow from the cavity to end chamber and end chamber to cavity by implementing perforated wall which sufficiently separates the main housing cavity from end chambers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the use method of the hydrogen gas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows the exploded perspective view of the hydrogen gas generator.    Hydrogen gas generator (10)    Housing (14)    Anode (18)    Perforated wall (30)    Hydrogen gas outlet (80)    Purge valve (82)
NOVELTY - Apparatus comprises processing tank provided with crusher having liquid raw material supply port in the upper part of the tank, water supply port, air ejection member for aeration of heater, and outlet for removal of prepared liquid manure, where the crusher crushes solid raw material, liquid raw material supply port supplies liquid raw material into the processing tank, water supply port supplies water to the raw material to obtain liquid raw material and air ejection member to pass air into heater which heats the liquid raw material with microorganisms.    USE - The apparatus is useful for preparing liquid manure (claimed), which is used as fertilizer in cultivation of crops e.g. rice, cabbage and spinach.    ADVANTAGE - The apparatus prepares liquid manure simply, rapidly and cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing liquid manure, which involves adding raw material in crusher and crushing the raw material, adding water to the crusher to make the crushed raw material into liquid state, passing the liquid raw material to the processing tank, heating the liquid raw material, aerating and fermenting the raw material using microorganisms, and removing the processed liquid manure.
NOVELTY - Fermented liquor is obtained by mixing optimum proportions of sugar solution and fermented liquor in which microbes are living and carrying out additional fermentation.    USE - The fermented liquor including rice wine and fruit wine is useful for providing antioxidant effect (all claimed).    ADVANTAGE - The fermented liquor is nutritious and capable of long-term storage at room temperature without using refrigerator, has excellent taste and aroma, prevents oxidation e.g. spoiling, and suppress freshness reduction. The method is environmentally-friendly and reduces production and transportation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fermented liquor.
NOVELTY - Method for producing hydrogen and butanol, involves saccharifying cellulose substrate by mixed culture of Clostridium having cellulose assimilation ability and Clostridium having hydrogen and butanol producing ability, and producing hydrogen and butanol from the saccharified product.    USE - The method is useful for producing hydrogen and butanol.    ADVANTAGE - The method produces hydrogen and butanol at high yield.
NOVELTY - The electrolytic cell has transparent, pressure-stable plastic half cells (A,B) which are disconnected by stable partition walls (1) and are gastight-locked by locking elements (4,6a). The stable partition wall has ion exchange membrane (2). The inside pressure is increased only by influence of stream-pressure electrolysis with hydrogen and oxygen according to Nernst equation by redox potential change, so that monitoring of electrochemical reduction, oxidation and electrochemical process are performed with automatic increase in pressure by switch of electric current in electrolytic cell.    USE - Low pressure electrolytic cell.    ADVANTAGE - The mixing of gasses can be avoided. The increase of inside pressure can be controlled efficiently. The overvoltage can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the low pressure electrolytic cell.    Partition walls (1)    Ion exchange membrane (2)    Locking elements (4,6a)    Electrodes (8a,8b)    Half cells (A,B)
NOVELTY - Converting solid biomass into biogas, comprises introducing the biomass into a container, by means of two screw-form, non-contact crushing of running waves into each other and simultaneously mixing, and then discharging from the container and automatically filling a fermenter (2) with the biomass from the container and emptying.    USE - The method is useful for municipal waste.    ADVANTAGE - The method: is simple and robust, economical, and achieves a higher yield and the digestate can be utilized as fertilizer; utilizes the jacket-heating system that ensures faster and more homogeneous temperature distribution in the reactor, which leads to a shorter residence time; makes use of a device which utilizes the complete reactor space, and ensures low intrinsic energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for converting the solid biomass into the biogas, comprises a two-stage seed tank and a two-stage solid- fermenter that comprises a fermenter and a main secondary fermenter (3), and a jacket heating system and a conveyor belt for feeding substrate in the fermenter.    DESCRIPTION OF DRAWING(S) - The drawings 1 and 2 show a schematic representation of a media mixer and a system for a quasi wet process, respectively (Drawing includes non-English language text).    Preliminary tank (1)    Fermenter (2)    Secondary fermenter (3)    Shredder or blender (4)    Conveyor screw (5)
NOVELTY - The furnace has a furnace body whose upper part is provided with a combustion chamber. A lower part of the furnace body is provided with a gasification chamber. The combustion chamber and the gasification chamber are provided with a mixing combustion device. The gasification chamber is connected with a combustion nozzle. The mixing combustion device is provided with an air hole. The air hole is connected with an air inlet channel via an adjusting valve.    USE - Direct-fired biomass gasification furnace.    ADVANTAGE - The furnace adopts the gasification chamber that is connected with the combustion nozzle for mixing fuel at the combustion chamber. The furnace ensures high power and better heat utilization rate.
NOVELTY - The system has an electric tar precipitator divided into two branches that are respectively connected with two pipe fittings. A secondary tube-type indirect cooler is connected with an inlet. An outlet of a pipe is connected with a filter purifying device that is connected with the inlet and connected with a primary water-gas separator through the pipe. The primary water-gas separator is connected with an inlet of a secondary water-gas separator through a connecting pipe. An inlet of the secondary water-gas separator is connected with a gas storage pipeline system.    USE - System for generating biomass fuel gas that is utilized as firewood stove fuel gas, industrial fuel gas and power supply plant fuel gas.    ADVANTAGE - The system has simple and rational structure, and rationally utilizes biomass energy without causing secondary pollution to surrounding environment.
NOVELTY - The device has a lower cylinder body supported by a support mechanism. A lower end of the lower cylinder body is connected with a connection seat. A valve seat is connected with a conical seat. A supporting sealing frame is provided with a rotating shaft. A rod is installed on the rotating shaft. The rotating shaft is rotated in a synchronous manner. An end of the rod is arranged in a chain box. The chain box is connected with a hung bell type valve body through a hanging chain. An end of another rod is hinged with a pull rod.    USE - Feeding device for a biomass gasification furnace.    ADVANTAGE - The device is rational in structural design, aesthetic in appearance, environment-friendly and safe to operate, and has uniform feeding effect, and ensures stable furnace pressure and avoids the need to stop continuous feeding process.
NOVELTY - The mechanism has a shell body provided with a double-layer water jacket, a water inlet and a water outlet. A flange cover is arranged with a lower flange cover and a rotating shaft. The rotating shaft is connected with the shell body and a supporting flange and installed on a seal bearing assembly by a driving mechanism unit. A spiral ash conveying unit is arranged in the rotating shaft.    USE - Ash conveying mechanism for a biomass gasification furnace.    ADVANTAGE - The mechanism is simple in structure and convenient to pack, and realizes pressure return water cooling effect at low temperature, and can collect ash material in a convenient manner.
NOVELTY - The mechanism has a furnace gate placed with a base plate. The base plate is formed with a through-hole. A gas-distributing pipe is inserted into the through-hole. A peripheral wall of the gas-distributing pipe is formed with an air hole. A cap assembly is sleeved on the distributing pipe and a center plate. The central plate is fixed on a bottom plate.    USE - Biomass gasification furnace ash disk mechanism.    ADVANTAGE - The mechanism is simple in structure and reliable and stable to operate, and realizes ash combustion and transmission in an effective manner.
NOVELTY - The furnace has an inner cylinder body formed as a conical structure and provided with a flange. An outer cylinder body is filled with heat insulating material and provided with an ash outlet. An upper part of the inner cylinder body is provided with a flange pipe. The flange pipe is connected with an air inlet pipe.    USE - Ash outlet biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure, convenient to pack and operated at low temperature and humidity, and has better sealing effect, and avoids dust stratification phemenenon and prevents an ash pan mechanism from falling down, and can conveniently collect ash material.
NOVELTY - The structure has a water jacket whose inner wall surface is provided with a flame-resistant heat insulated wall body. A plate is fixed with an outer cylinder body, a dust ring and a water sealing ring. A dust-baffle ring is connected with the water sealing ring. A block plate is welded with the dust-baffle ring. A furnace body is set in a biomass fuel feeding opening part and formed with a gas outlet opening part.    USE - Biomass gasification furnace body structure.    ADVANTAGE - The structure is simple, and realizes self-steam generating function, and can uniformly combust and gasify materials with high stability, and increases air outlet temperature and combustion temperature and improves gas production rate.
NOVELTY - Zinc azide complex (III) are new.    USE - (III) is useful for: preparing (I) (claimed); and treating hypertension and congestive heart failure. No biological data given.    ADVANTAGE - The process is economical and environment-friendly and suitable for large-scale commercial production.    DETAILED DESCRIPTION - Zinc azide complex of formula (L1aZn(N3)bXc) (III) are new.    X = NO3, OH, Cl, Br or I;    L1 = amine ligand that can coordinate with Zn; and    a = 0-2;    b = 0-4; and    c = 0-2.    INDEPENDENT CLAIMS are included for:    (1) a process for preparing (III); and    (2) a process-1 for preparing a substituted tetrazole derivative of formula (I), comprising reacting (III), which is prepared by the complex formation reaction, with a nitrile compound of formula (R-CN) (II) after isolation or in situ.    R = organic residual group.
NOVELTY - A circulating fluid containing desulfurizing bacteria is sprayed to flow downwards through the spray header at the top of the desulfurizing tower, and biogas is blown from bottom of the desulfurizing tower. A filler is fully contacted with the circulating fluid, and the hydrogen sulfide of the biogas is oxidized and removed by desulfurizing bacteria in circulating fluid by bio-oxidation. The addition amount of biogas slurry is 2.0-2.5 L/m3 of circulating liquid.    USE - Biological desulfurization of biogas.    ADVANTAGE - The biological desulfurization of biogas is carried out efficiently by a simple process under controlled conditions.
NOVELTY - Corn stalk sterile organic fertilizer is prepared by (parts by weight): stalk (700-800), water (200-300), clear liquid dung (31-41), and oil cake (25-30).    USE - As corn stalk sterile organic fertilizer (claimed).    ADVANTAGE - The corn stalk sterile organic fertilizer has low cost; has easy material; has simple operation; has no pollution; recovers natural ecological balance; has proportion of high class tobacco and proportion of medium class tobacco increase for 0.2 Yuan/kg, 1.5% and 4%. The clear liquid dung improves fermentation speed of the corn stalk without carrying more bacteria when using. The oil cake provides nutrition; and increases the flavor of the tobacco leaves and oil content so as to improve proportion of medium-high class tobacco.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing corn stalk sterile organic fertilizer by the formulation involving processing the corn stalk to length of 45-50 mm; soaking the stalk with water or making the stalk drench through with water till the relative water content is 58-62%; pacing one layer of stalk on the selected manure collected zone and watering the clear liquid dung, then spreading one layer of oil cake, stacking and forming, sealing the stacked material with mud slurry; the thickness of each layer of straw is 30-40 cm, and the thickness of the oil cake is 0.4-0.6 cm; turning once after stacking for 25 days, stacking and sealing, repeating for three times till ending the fermentation, then obtaining the organic fertilizer.
NOVELTY - A biological organic fertilizer comprises livestock dung and straw at mass ratio of 15-19:10-6.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer can be prepared without using coal and with little power consumption and no wastewater discharge, waste gas and waste residue, and is energy-saving and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the biological organic fertilizer, comprising:    (A) culturing an enzymatic microorganism, dissolving brown sugar with warm water, and adding the enzymatic microorganism to ferment for 5-8 hours;    (B) crushing straw to obtain straw powder;    (C) pouring livestock dung and straw powder into a fermentation tank, adding fermented brown sugar aqueous solution into the fermentation tank, and uniformly stirring; and    (D) turning over the materials to increase oxygen during the fermentation process and obtaining the biological organic fertilizer.
NOVELTY - Preparing compost tea comprises (a) loading the compost tea into a mesh bag with a mesh hole diameter of 0.08-0.5, (b) adding water into a container, placing the breather pipe at the bottom of the container, where the aeration quantity (1 m3) of water is 0.2-0.8 l/hour and ventilating the mixture for 20-60 minutes, and removing the chlorine and adding molasses, alga powder and humic acid with a mass ratio of 1:1.5-5:1.5-4.5 and then placing the mesh bag loaded with compact in step (a) into the water.    USE - The method is useful for preparing compost tea, which is useful for improving soil hardening.    ADVANTAGE - The method is capable of easily, rapidly and economically preparing the compost tea for improving soil hardening in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing compost tea comprises (a) loading the compost tea into a mesh bag with a mesh hole diameter of 0.08-0.5, (b) adding water into a container and placing a breather pipe at the bottom of the container, where the aeration quantity (1 m3) of water is 0.2-0.8 l/hour, ventilating the mixture for 20-60 minutes, and removing the chlorine and adding molasses, alga powder and humic acid with a mass ratio of 1:1.5-5:1.5-4.5 and then placing the mesh bag loaded with compact in step (a) into the water, where the mass ratio of the compact and the water is 1:10-4, the total adding mass of the molasses, alga powder and humic acid is 1-5% of the mass of the compact.
NOVELTY - The system has bio gas system which produces bio gas by anaerobic digestion action of organic material. A landfill bio gas system discharges the methane gas produced from life waste landfill. A bio gasification system generates and discharges synthetic gas from biomass through gasification process. An oxyhydrogen (HHO) gas reactor generates HHO gas by processing HHO in waste water. A fuel-based generation system has gas generator which combusts the gases from the bio gas system, landfill bio gas system, bio gasification system and HHO gas reactor to generate electricity.    USE - Neo-genesis energy power generation system for fuel base electric power system.    ADVANTAGE - The electric energy production cost from the biogas is reduced and usage of neo-genesis energy is maximized.
NOVELTY - Device comprises fermentation warehouse, factory, multi-functional stack dumper, feeding device, sieving machine.    USE - The device is useful for producing fertilizer using aerobic fermentation of organic solid waste.    ADVANTAGE - The device is simple, and cost-effective, and has high degree of mechanization.    DETAILED DESCRIPTION - Device comprises fermentation warehouse, factory, multi-functional stack dumper, feeding device, sieving machine, where the factory is provided with multiple groups of fermentation chamber, each fermentation chamber comprises upper and lower corresponding to the position is provided with a primary fermentation chamber, and secondary fermentation chamber, the primary fermentation chamber is connected with bottom of the secondary fermentation chamber are equipped with transmission belt, rolling shaft and aeration pipe, the feeding device is located at discharge end of the primary fermentation chamber, the primary fermentation chamber is connected with the secondary fermentation chamber are provided with multi-functional stack dumper, the secondary fermentation chamber are provided with movable baffle plate the primary fermentation chamber is connected with the secondary fermentation chamber of the transmission belt is connected with the movable baffle plate corresponding to the primary fermentation chamber of the movable baffle plate is located in the secondary fermentation chamber of transmission belt, the secondary fermentation chamber of the movable baffle plate is located on the upper portion, the factory top portion is provided with several air inlet of the ozone concentration pipe, and the ozone concentration pipe is connected with the factory building is provided with a deodorization device. An INDEPENDENT CLAIM is included for method for producing fertilizer using aerobic fermentation of organic solid waste.
NOVELTY - A biomass comprehensive transformation device comprises pyrolyzing furnace, tri-state purification separation device, standing separating device, gas purifying device, air storage tank and pneumatic device. A pneumatic device is set on the tri-state purification separation device. The device also includes a pyrolysis furnace liner, an outer cylinder, a fire grate, a discharge hole, and an air outlet pipe.    USE - Biomass comprehensive transformation device.    ADVANTAGE - The device is capable of converting biomass to biomass fuel gas, biomass vinegar and biomass tar, or biomass carbon, biomass fuel gas, biomass vinegar and tar, completely collects and utilizes the biomass, and will not produce secondary pollution to the environment. The biomass conversion rate is 0.5-1.5 t/hour. The device has simple structure, easy operation and is suitable for countryside use.
NOVELTY - Temperature elevation of water scrubber comprises introducing washing water to water scrubber through exchanging heat or without exchanging heat, continuously sending washing water in water scrubber to heat exchanger, exchanging heat and returning water to water scrubber, finishing once heating circulation of washing water, and repeating heating circulation until temperature of the washing water at 80-90 degrees C.    USE - Method of temperature elevation of water scrubber (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a preparation of biodiesel comprising mixing grease with methanol to obtain crude biodiesel under ester exchange reaction conditions, distilling crude biodiesel to obtain methanol and distilled crude biodiesel product, and washing distilled crude biodiesel product; sending washed crude biodiesel product to flashing tower with heat exchanger in upper part, flashing, cooling, discharging biodiesel steam by heat exchanger in flashing tower, and extracting heavy component having boiling point higher than biodiesel oil from the bottom of flashing tower; and when heat exchanging efficiency of heat exchanger arranged in upper part of flashing tower is reduced to 50-70%, continuously introducing methanol to heat exchange medium tube pass of heat exchanger from one end of the heat exchange medium tube pass of heat exchanger, and continuously discharging contacted methanol from other end of heat exchange medium tube pass of heat exchanger, and descaling heat exchanger of flashing tower;and    (2) washing method of crude biodiesel product comprising heating washing water, contacting crude biodiesel product with heated washing water in water scrubber, with crude biodiesel product comprising biodiesel, glycerol and methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the temperature elevation of water scrubber.
NOVELTY - A biogas preparing refined industrial welding gas contains biogas as main fuel, and multifunctional catalyst added to biogas. The volume ratio of multifunctional catalyst and biogas is 15:100000. The multifunctional catalyst contains (in volume parts) solvent gasoline (20-25), cyclohexane (15-20), butyl acetate (10-15), ethylene glycol dimethyl ether (8-10), methyl ethyl ketone (6-12), n-butyl cyclohexane (5-18), butyl acetate (5-15), p-tert-butyl phenol (6-12) and organic boride (4-6).    USE - Biogas preparing refined industrial welding gas.    ADVANTAGE - The biogas preparing refined industrial welding gas has improved solubility and dispersion of fuel, gas and methane.    DETAILED DESCRIPTION - A biogas preparing refined industrial welding gas contains biogas as main fuel, and multifunctional catalyst added to biogas. The volume ratio of multifunctional catalyst and biogas is 15:100000. The multifunctional catalyst contains (in volume parts) 200# solvent gasoline (20-25), cyclohexane (15-20), butyl acetate (10-15), ethylene glycol dimethyl ether (8-10), methyl ethyl ketone (6-12), n-butyl cyclohexane (5-18), butyl acetate (5-15), p-tert-butyl phenol (6-12) and organic boride (4-6).
NOVELTY - Microbial organic fertilizer comprises mixture A and powder B. The mixture A comprises Klebsiella pneumoniae subsp pneumonaiae, Bacillus mucilaginosus, B.megaterium, B.subtilis, Sporotrichum thermophile Apinis a bacterial liquid and organic base material in a weight ratio of 1:1:1:1:1:500, where the organic base stock material comprises straw, and humic acid in a weight ratio of 3:3. The sterile powder B comprises fermented bacterial powder of Streptomyces microflavus.    USE - The microbial organic fertilizer is useful for planting grapes, cotton and potato (all claimed).    ADVANTAGE - The fertilizer enables planting in extreme dry condition, is enriched with potassium, nitrogen and potassium, and convenient to farmer, can be prepared simply, and has important application value.    DETAILED DESCRIPTION - Microbial organic fertilizer comprises mixture A and powder B. The mixture A comprises Klebsiella pneumoniae subsp pneumonaiae, Bacillus mucilaginosus, B.megaterium, B.subtilis, Sporotrichum thermophile Apinis a bacterial liquid and organic base material in a weight ratio of 1:1:1:1:1:500, where the organic base stock material comprises straw, and humic acid in a weight ratio of 3:3. The sterile powder B comprises fermented bacterial powder of Streptomyces microflavus, where the sterile powder of B is added to the mixture A (0.2%) to obtain microbial organic fertilizer. An INDEPENDENT CLAIM is included for method of preparing the microbial organic fertilizer, which involves (a) preparing mixture A, compacting the mixture A after stacking cover sealing by plastic film, naturally fermenting the mixture for 20 days, deposition the fermented product at 65 degrees C, (b) packing sterile powder B to the external bacteria bag, and (c) mixing prepared mixture A and sterile powder B.
NOVELTY - A catalytic cracking method involves refining a composite comprising (in wt.%) adsorption-depositing agent (10-80), assistant active component (5-10), cationic surfactant (0-5), non-ionic surfactant (0-10), auxiliary surfactant (0-5), and diesel oil (balancing amount).    USE - Catalytic cracking method for refining waste oil.    ADVANTAGE - The method enables catalytic cracking without acid and alkali refining, oxidative discoloration and diesel biomass, and the waste residue can be processed into agricultural fertilizer without any pollution to the environment, in a simple and convenient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for diesel-free acid and alkali refining.
NOVELTY - Environmental-friendly preparation of multi-vitamin multi-element oligosaccharide functional healthcare product, biogas and an organic fertilizer from straw, is claimed. The method utilizes a crushing device, a straw cleaning machine, a dissolving device , a biological decomposition device, a shrinking device, a purifying device, a drying granulating device, a biogas purifier, a biogas tank, and an organic fertilizer fermentation and dry granulation device .    USE - The method is useful for preparing multi-vitamin multi-element oligosaccharide functional healthcare product.    ADVANTAGE - The method: utilizes straw as raw material in comparison with chemical synthesis of agricultural products; realizes maximum utilization of waste; and is energy-saving.
NOVELTY - Preparing fenugreek saponin B, comprises (a) pouring an aqueous solution of fenugreek saponin extract into polyamide column, alkaline alumina column, neutral alumina column or silica gel column, eluting with water, collecting and combining the eluent, concentrating and drying the eluent to obtain the crude product (I) of fenugreek saponin B.    USE - The method is useful for preparing fenugreek saponin B.
NOVELTY - Producing ethylene cracking material through hydrogenation of liquefied petroleum gas, involves providing two reactors; filling non-noble metal hydrogenation refining catalyst in the two reactors; heating the effluent of a first reactor (3) and sending it to the second reactor (5); and partially circulating the liquefied petroleum gas after hydrogenation and obtained by effluent of second reactor, and mixing them with raw material (1) of fresh liquefied petroleum gas to enter first reactor.    USE - For producing ethylene cracking material through hydrogenation of liquefied petroleum gas (claimed).    ADVANTAGE - The method can process the industrial C4 fraction into ethylene cracking raw material through hydrogenation, synchronously solves the problems that the hydrogenation of the industrial C4 fraction has a large amount of heat release, and the catalyst can be easily subjected to coking.    DETAILED DESCRIPTION - Producing ethylene cracking material through hydrogenation of liquefied petroleum gas, involves providing two reactors; filling non-noble metal hydrogenation refining catalyst in the two reactors; heating the effluent of a first reactor (3) and sending it to the second reactor (5); and partially circulating the liquefied petroleum gas after hydrogenation and obtained by effluent of second reactor, and mixing them with raw material of fresh liquefied petroleum gas to enter first reactor, where weight ratio of circulated liquefied petroleum gas after hydrogenation to raw material of fresh liquefied petroleum gas is 8:1 to 1:1.    DESCRIPTION OF DRAWING(S) - The figure shows a view of a production line for producing ethylene cracking material.    Raw material (1)    First reactor (3)    Heater (4)    Second reactor (5)    Product cooler (6)    Reaction product outlet (7)
NOVELTY - Preparing mechanically stabilized polyazoles, comprises: treating at least one polyazole having at least one amino group in a repeat unit with a solution comprising at least one strong acid and at least one stabilizing reagent, where the total content of stabilizing reagents in the solution is 0.01-30 wt.%; and performing the stabilization reaction directly and/or in a subsequent processing step by heating to greater than 25 degrees C, where the stabilizing reagent used is at least one polyvinyl alcohol.    USE - The process is useful for preparing mechanically stabilized polyazoles, which are useful: in a membrane used in a membrane electrode assembly for producing a fuel cell (claimed); and as electrolyted for a display element, an electrochromic element or various sensors.    ADVANTAGE - The process provides mechanically stabilized polyazoles, which: provide membrane which has solubility of less than 0.5 wt.% of polyazole polymer in 99% phosphoric acid over 85-120 degrees C, in simple and inexpensive manner on industrial scale; exhibit improved mechanical stability compared to unbridged acid-containing polyazole membranes, good conductivity, improved compression stability and improved long-term stability; has improved modulus of elasticity and improved elongation at break; and provide solution, which is absolutely harmless from a health point of view.
NOVELTY - Stabilizing fast pyrolysis oil, comprises hydrogenating fast pyrolysis oil (14) with hydrogen (12) reactant in the presence of ruthenium metal catalyst (22) at at least 70 degrees C and at a pressure of at least 600 psig to form a hydrogenated fast pyrolysis oil exhibiting an increase in viscosity of less than 10% after accelerated stability testing at 80 degrees C for 24 hours.    USE - The process is useful for stabilizing fast pyrolysis oil, which is useful as a biofuel (claimed). The hydrogenated fast pyrolysis oil is useful to replace mineral fuel oil in heating.    ADVANTAGE - The process modifies fast pyrolysis oil with improved stability against viscosity increase without causing thermal degradation of the fast pyrolysis oil. The process reduces risk of handling problems when used in burner systems and hydrogen consumption in a cost-effective manner. The hydrogenated fast pyrolysis oil exhibits a carbonyl content reduction by at least 10% and a deoxygenation by at least 5% compared to the fast pyrolysis oil prior to hydrogenation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a process for hydrogenating pyrolysis oil.    Hydrogen (12)    Fast pyrolysis oil (14)    Compressor (16)    Pump (18)    Reactor (20)    Catalyst. (22)
NOVELTY - The gasifier has a system to release dry biomass from an upper drying chamber (101) into an intermediate gasification chamber (102). A gasified biomass release system releases gasified biomass from the gasification chamber into a combustion chamber. A product gas outlet is coupled to the gasification chamber to provide product gas for gasifying the biomass. An exhaust gas communication unit communicates exhaust gas e.g. flue gas, from the combustion chamber to the gasification chamber and the drying chamber. A product gas outlet is coupled to the gasification chamber.    USE - Self-sustaining biomass gasifier for use in a diesel engine and a stirling engine, for gasifying wet biomass to generate electricity or produce heat.    ADVANTAGE - The combustion chamber provides heat for gasifying process by burning solid products i.e. char, resulted from the gasification chamber in the presence of excess air introduced into a lower chamber, so that the excess air is preheated by using a heat exchanger in which the hot exhaust gases and the product gases are generated from an upper chamber, thus improving efficiency of combustion for improving efficiency of the gasifier by 80 percent, and hence reducing wastage of energy in the gasifier without the need for after-cooling of the product gases in an inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasifying biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasifier in which heat flux operation is performed.    Upper drying chamber (101)    Intermediate gasification chamber (102)
NOVELTY - Device for producing combustible pellets, preferably from horse manure comprises a sterilizing device (24) for sterilizing a pre-dried manure containing mixture by means of pressure and temperature, and a pelletizing device (50) for pressing the sterilized mixture into pellets (52) downstream of the sterilizing device.    USE - The device is useful for producing combustible pellets, preferably from horse.    ADVANTAGE - The device is suitable as a large-scale plant, and can used by multiple users at different places.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for producing combustible pellets from horse.    Horse manure containing mixture (10)    Drying device (14)    Sterilizing device (24)    Pelletizing device (50)    Pellet (52)
NOVELTY - The stove has a radiating pipe (5) provided with an independent box-type structure. A left steering chamber (6) is connected with a collector (9). A smoke pipe (10) is connected with an upper part of the left steering chamber. A jacket structure is connected with a gasification chamber (19). An end of the gasification chamber is connected with a combustion chamber (28). An outer wall of a furnace body is provided with a blower tube (14). The blower tube is connected with a blower (13). A side of a furnace wall (1) is provided with a hot air outlet pipe (31).    USE - Gasification and combustion hot-blast stove.    ADVANTAGE - The stove has high gasification efficiency and wide application range. The stove can utilize biomass fuel heat energy so as to avoid pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a gasification and combustion hot-blast stove.    Furnace wall (1)    Radiating pipe (5)    Left steering chamber (6)    Collector (9)    Smoke pipe (10)    Blower (13)    Blower tube (14)    Gasification chamber (19)    Combustion chamber (28)    Hot air outlet pipe (31)
NOVELTY - The system (100) has a fuel cell (1) that supplies electric power and heat. A circulation path (2) is provided to circulate thermal medium absorbing heat of the fuel cell. A regenerator (4) is provided to thermally store the heat of the thermal medium. A pump (71) is arranged at the circulation path to circulate the thermal medium. A controller (50) is provided to control the pump to change the operating quantity of the pump to two-stages of high operating quantity and low operating quantity larger than zero intermittently, when the fuel cell produces electric power.    USE - Fuel cell system e.g. hot-water storing type waste-heat-recovery system.    ADVANTAGE - The air entrainment of the circulation pump can be prevented. By increasing the quantity of the high temperature recycled water sent to storage tank, the heat release of heat recovery piping can be decreased and extension of the heat recovery piping can be attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Circulation path (2)    Regenerator (4)    Controller (50)    Pump (71)
NOVELTY - The method involves arranging electric power feeding portion at the side ends of an electrolytic membrane (48). The depressurization process of a cathode is started. The electrolytic current is applied to the cathode while performing the depressurization process of cathode. The specific electrolytic current is applied to cathode for performing depressurization process of cathode when pressure of cathode is lower than the predetermined threshold value.    USE - Shutdown method of water electrolysis system used during manufacture of fuel battery.    ADVANTAGE - The occurrence of blister in solid polymer film can be prevented effectively, since specific electrolytic current is applied to cathode for performing depressurization process when pressure of cathode is lower than the predetermined threshold value. The water electrolysis effect of water electrolysis system can be improved efficiently. The leakage of high-pressure hydrogen to anode electrode catalyst layer can be prevented. The occurrence of damage to anode and catalyst electrodes can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Electrolytic membrane (48)    Return line (80)    Pure-water supply piping (82)    Oxygen-pumping piping (84)
NOVELTY - Controlled method for producing biofuel and lipids from algae, comprises: providing upwelled water in a body of water by using an open-cycle ocean thermal energy conversion (OTEC) system; culturing algae in the upwelled water; feeding the algae to planktivorious organisms; extracting lipids from the planktivorious organisms; and polishing the lipids to make biofuel or other useful products.    USE - The method is useful for producing biofuel and lipids from algae, where the biofuel is used in a liquid fuel comprising diesel, biodiesel, kerosene, jet-fuel, gasoline, JP-1, JP-4, JP-5, JP-6, JP-7, JP-8, jet propellant thermally stable, a Fischer-Tropsch liquid, an alcohol-based fuel, or a cellulosic biomass-based transportation fuel (claimed).    ADVANTAGE - The method is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a controlled system for producing biofuel and lipids from algae, comprising means for generating or controlling upwelled water in a body of water, means for culturing algae in the upwelled water, means for feeding the algae to planktivorious organisms, means for extracting lipids from the planktivorious organisms, and means for polishing the lipids to form biofuel or other useful products.
NOVELTY - Therapeutic and prophylactic antimalarial drug comprises (in wt.%): antimalarial drug (0.8-13.5); excipients (70-90); and a probiotic biomass of strain Bacillus subtilis (10-12).    USE - Used as therapeutic and prophylactic antimalarial drug. No biological data given.
NOVELTY - Sorbent comprises porous carrier, and sorbing compound applied on the porous carrier, where the sorbent comprises sorbing compound (1-40 wt.%). The sorbing compound is chosen from alkanolamines, methyldiethanolamine, monoethanolamine, diglycolamine, and their mixtures.    USE - The sorbent is useful for purifying oil and natural hydrocarbon gas from hydrogen sulfide and mercapten (claimed).
NOVELTY - Electrode for cathodic evolution of hydrogen in electrolytic processes comprises a metal substrate coated with an external catalytic layer containing 4 to 40 g/m2 of crystalline ruthenium (Ru) oxide having a rutile-type structure with Ru-Ru and Ru-O bond length where a Debye-Waller factor is lower than 2x103/ Angstrom .    USE - The electrode is useful for cathodic evolution of hydrogen in electrolytic processes (claimed).    ADVANTAGE - The electrode may comprise an internal catalytic thin layer platinum-based, which gives an enhanced protection against accidental current reversal events. The invention provides, in comparison with the prior art, by an equal or higher catalytic activity, a lower overall raw material cost, a higher reproducibility in the preparation and an equal or higher lifetime and tolerance to accidental current reversals at the usual operative conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for manufacturing the electrode comprising preparation of a ruthenium solution by dissolution of a ruthenium nitrate in glacial acetic acid under stirring, with optional addition of nitric acid, followed by a dilution with an aqueous solution of acetic acid at a concentration comprised between 5 and 20% by weight; and application of the solution on a metal substrate in multiple coats, with thermal decomposition at 400-600 degrees C for a time not lower than 2 minutes after each coat.
NOVELTY - Biofilm removal agent comprises an enzyme for degrading polysaccharide containing uronic acid unit (5-100%) with respect to all saccharide units.    USE - The biofilm removal agent is useful for processing wastewater (claimed), and cleaning foodstuff preparing site e.g. kitchen medical device, and reverse osmosis membrane.    ADVANTAGE - The agent removes the biofilm adhered to the solid surface and biofilm discharged in water phase, and solves problems caused by biofilm including increase in frictional resistance of water pipe or fluid in ship bottom, reduction of heat transfer of heat exchanger, and corrosion material. Clogging of separation membrane can be prevented and organic wastewater by membrane separation activated sludge method can be stably processed for long period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for removing biofilm, involves processing biofilm using the biofilm removal agent;    (2) membrane separation method, involves filtering to-be-processed water using the installed membrane separation apparatus, processing the separation membrane using the biofilm removal agent, and suppressing raise of transmembrane pressure difference; and    (3) apparatus for processing organic wastewater by membrane separation activated sludge method comprising an activated sludge tank which accommodates the activated sludge containing microorganisms, membrane separation apparatus installed inside of the activated sludge tank, unit for separating treated water into solid and liquid, unit for measuring time dependent change of uronic acid unit concentration in water phase in the activated sludge tank, and an unit for adding the biofilm removal agent.
NOVELTY - The apparatus has deconstruction vessel (94) which communicates with pressurization vessel (24) for receiving pressurized biomass and catalyst and for converting biomass into feedstock and gaseous products. Valve (42) isolates pressurization vessel and permits pressurized fluid to create pressure differential between pressurization and deconstruction vessels in closed position, and permits fluid communication between pressurization and deconstruction vessels so as to deliver pressurized biomass to pressurization vessel and catalyst to deconstruction vessel in open position.    USE - Apparatus for producing feedstock for biofuel and biochemical manufacturing processes.    ADVANTAGE - As the valve permits fluid communication between pressurization and deconstruction vessels so as to deliver pressurized biomass to pressurization vessel and catalyst to deconstruction vessel in open position, the catalyst can be removed in more efficient manner from the feedstock.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for converting biomass to feedstock for biofuel and biochemical manufacturing processes; and    (2) method for converting biomass to feedstock for biofuel and biochemical manufacturing processes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for producing feedstock for biofuel and biochemical manufacturing processes.    Pressurization vessel (24)    Valve (42)    Deconstruction vessel (94)    Canister (210)    Metering pump (214)
NOVELTY - A cell that recombinantly expresses either at least one gene of the butanol biosynthetic pathway and a gene encoding a thiolase that condenses one acetyl-CoA with one propionyl-CoA to form a ketone; or a) a gene encoding a thiolase that condenses one acetyl-CoA with one propionyl-CoA to form a ketone, b) genes encoding a reductase, a hydratase, and a dehydrogenase that convert the ketone to valeryl-CoA, and c) a gene encoding a bi-functional aldehyde/alcohol dehydrogenase, is new.    USE - As cell selected from bacterial cell, fungal cell (including a yeast cell), plant cell, insect cell, or animal cell. The bacterial cell is an Escherichia coli cell. The cell is useful for producing pentanol (claimed). The pentanol is useful as biofuel.    ADVANTAGE - The pentanol can be produced through a biological process involving metabolic engineering by recombinant gene expression in cells.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cell culture medium or supernatant collected from culturing the cell;    (2) a method (M1) involving: culturing the cell in cell culture medium; and    (3) a method (M2) involving recombinantly expressing in a cell either the genes of the butanol biosynthetic pathway and the thiolase; or the genes selected from (a), (b) and (c).
NOVELTY - A modification system has desulfurizer with adsorption agent which adsorbs and removes sulfur compound contained in raw fuel gas, modifier which modifies raw fuel gas after desulfurizing to produce hydrogen rich gas, and adsorption performance evaluating unit which determines the adsorption performance of the adsorption agent based on the time-dependent detection result of a hydrogen gas sensor which detects the quantity of hydrogen gas contained in the raw fuel gas which flows in the desulfurizer.    USE - Modification system for fuel cell power generation system.    ADVANTAGE - Fall of adsorption performance is prevented before the performance degradation of modification catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of fuel cell power generation system. (Drawing includes non-English language text).    Desulfurizer (1)    Modifier (2)    Hydrogen gas sensor (5)    Fuel cell (8)    Adsorption performance evaluation unit (11)    Desulfurization control unit (12)
NOVELTY - Highly purified hydrogen purification method involves filling hydrogen recovery tower, filled with hydrogen storage alloy, with hydrogen-containing gas to occlude hydrogen, purging the impurity gas which remains in the hydrogen recovery tower, cleaning the impurity which remains in hydrogen recovery tower using a part of the highly purified hydrogen, recovering cleaning off gas emitted during cleaning process, releasing the hydrogen occluded during the hydrogen storage process out of the hydrogen recovery tower to obtain highly purified hydrogen, and cooling the hydrogen storage alloy.    USE - Highly purified hydrogen purification method for fuel cell manufacture.    ADVANTAGE - Product loss is reduced, and highly purified hydrogen gas recovery is highly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the structure of highly purified hydrogen purification systems. (Drawing includes non-English language text).    Hydrogen recovery tower (1a, 1b, 1c, 1d)    Medium distribution path (2a, 2b, 2c, 2d)    Pressure-control valve (3)    Valve (4, 5)    Vacuum pump (6)    Mass flow controller (7, 8)    Hydrogen-containing gas (A)    Off gas (B)    Highly purified hydrogen (C)
NOVELTY - The SOFC has an electricity generating element (A) whose fuel electrode (20) is embedded in a corresponding first recess (12) of a support substrate (10). The ratio of the depth (t1) of the first recess with respect to a distance (t2) between the wall surface of a fuel gas flow channel (11) and the bottom wall of the first recess ranges from 0.07 to 11.5.    USE - SOFC for generating electric power.    ADVANTAGE - Improves electronic conductivity in between the fuel electrode and interconnectors, thus increasing electric power generation output of SOFC. Improves the utilization factor of fuel gas. Reduces the usage-amount of nickel, thus reducing the manufacturing cost of SOFC.    DETAILED DESCRIPTION - Preferably, the support substrate is made of a material which comprises magnesium oxide, spinel, nickel oxide, nickel, yttrium oxide and/or calcium zirconate. Preferably, the fuel electrode is made of a material which comprises nickel oxide, nickel, yttrium oxide, calcium zirconate, and/or yttria stabilized zirconia.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of a SOFC.    Support substrate (10)    Fuel gas flow channel (11)    First recess (12)    Fuel electrode (20)    Electricity generating element (A)    Depth (t1)    Distance (t2)
NOVELTY - The method involves heating a deeply located fluidized bed region (7) of a fluidized bed reactor (2) at a gasification temperature, which is lower than a softening temperature of a starting material or ashes of the starting material. A reactor housing section (5), which lies higher than the fluidized bed region, is heated in another gasification temperature. The latter gasification temperature is higher than the former gasification temperature. The starting material is supplied into the fluidized bed region. Produced synthesis gas is discharged.    USE - Method for producing synthesis gas from carbonaceous starting material e.g. biomass and carbon.    ADVANTAGE - The method avoids occurrence of undesired adhesion even during application of softening critical starting materials with regular gasification efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing synthesis gas from carbonaceous starting materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a device for producing synthesis gas from carbonaceous starting material by gasification.    Device for producing synthesis gas from carbonaceous starting material (1)    Fluidized bed reactor (2)    Reactor housing (3)    Fluidized bed-housing section (4)    Reactor housing section (5)    Deeply located fluidized bed region (7)
NOVELTY - The system (100) has a methane separation apparatus (1) that separates methane from biogas. A buffer tank (3) stores off-gas discharged from separation apparatus. A pressure regulation device (5) adjusts pressure of off-gas discharged from buffer tank before combustion of off-gas. A combustion tower (6) burns off-gas when pressure of off-gas discharged from buffer tank is adjusted. A switching valve (4) switches supply of the off-gas to combustion tower. The switching valve adjusts pressure of the biogas supplied between buffer tank and pressure regulation device.    USE - Off-gas combustion system.    ADVANTAGE - The density and pressure variation of the off-gas can be prevented effectively, since combustion tower is provided to burn off-gas when pressure of off-gas discharged from the buffer tank is adjusted. The off-gas can be burned stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for off-gas combustion method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the off-gas combustion system. (Drawing includes non-English language text)    Methane separation apparatus (1)    Buffer tank (3)    Switching valve (4)    Pressure regulation device (5)    Combustion tower (6)    Off-gas combustion system (100)
NOVELTY - Determining an amount of biogenic gas generated by biodegradation of organic matter in a sedimentary series of a sedimentary basin, comprises considering bioreactive structural motif (I), taking a sample of rock of sedimentary series at a depth close to the surface, defining a reaction scheme, and determining the amount of biogenic gas produced by biodegradation of the bioreactive structural motif, by the reaction scheme and the quantities of each structural motif present in the sample.    USE - The process is useful for determining an amount of biogenic gas generated by biodegradation of organic matter in a sedimentary series of a sedimentary basin, where the biogenic gas is methane (claimed).    DETAILED DESCRIPTION - Determining an amount of biogenic gas generated by biodegradation of organic matter in a sedimentary series of a sedimentary basin, comprises considering bioreactive structural motif of formula (CxHyOvSzNw) (I), taking a sample of rock of sedimentary series at a depth close to the surface, such that the rock has undergone no biodegradation, and it determines the amount of each bioreactive structural motif present in the sample, defining a reaction scheme where the bioreactive structural motifs react parallel with electron acceptors, and each of the bioreactive structural motifs sequentially reacts with the electron acceptor according to reaction rates for each individual bioreactive structural motifs, where the speed is determined with experimental measurements, and determining the amount of biogenic gas produced by biodegradation of the bioreactive structural motif, by the reaction scheme and the quantities of each structural motif present in the sample.    x = greater than 6;    y = greater than x; and    v, z, w = less than 6.
NOVELTY - The method involves learning corrected amount with respect to the zero point of the pressure detection apparatus after the supply stoppage of the fuel gas. The pressure of the cathode is detected by the corrected amount calibrated by pressure detection apparatus. The oxidizing agent gas is supplied to the fuel battery from the oxidizing agent gas supply apparatus after implementing an electric power generation process at the time of generating the fuel battery.    USE - Shutdown method of fuel cell system.    ADVANTAGE - The flow volume of the low flow volume supplied from an oxidizing agent gas supply apparatus can be set accurately.    DESCRIPTION OF DRAWING(S) - The drawing shows a timing chart illustrating process of shutting down of fuel cell system. (Drawing includes non-English language text)    Air pump (50)    Back pressure valve (58)    In tank solenoid valve (63)    Cutoff valve (65)
NOVELTY - Biomass pyrolyzing furnace comprises furnace shell, smoke device set on the furnace shell, and furnace liner in the furnace shell. The four sides of furnace liner are provided with meshes. The bottom surface of furnace liner is a plate provided with holes. The furnace shell is provided with an air inlet pipe. The furnace liner is set between the inner wall of furnace shell and flow distribution plate. The distribution plate is provided with air holes.    USE - Biomass pyrolyzing furnace.    ADVANTAGE - The furnace has short pyrolysis time, uniform and high efficiency, high wood tar pyrolyzing and recycling rate, high wood tar yield, simple structure, and convenient operation and maintenance.
NOVELTY - The system has a valve whose air outlet opening is connected with an end of a high temperature gas pipe i.e. double-layer mechanism. An external sleeve and an inner air pipe are fixed together to form a water jacket that is filled with flowing cooling water. The inner air pipe is connected with the high temperature gas pipe. A main air pipe is connected with the gas pipe for taking air into a burning layer of a biomass gasification furnace. An air guide bucket is provided with the biomass gasification furnace.    USE - Air inlet system for use in a biomass gasification furnace.    ADVANTAGE - The system is convenient to maintain and simple in structure, and has high temperature resistance, high cooling efficiency and high safety. The system prolongs service life of a pipeline. The system is provided with the gas pipe to eliminate an ash outlet of the biomass gasification furnace.
NOVELTY - The method involves taking air and steam as gasifying agent for carrying out the gasification process. The gas is generated to prepare the overheated vapor in a gasification furnace (1). The overheated vapor in the gasification furnace is utilized for providing heat for the gasification process. The tar is removed from the gas contained in the gasification furnace, so as to generate silicon.    USE - Method for performing pyrolysis and gasification of biomass.    ADVANTAGE - The efficiency of the gasification process can be improved. The gasification furnace can be operated conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the process for performing pyrolysis and gasification of biomass.    Gasification furnace (1)    Inner tube (7)    Hopper (8)    Coil heater (10)    Evaporator (14)
NOVELTY - The furnace has a furnace housing that is connected with a blower by a ventilating pipe. The housing is provided with a feeding opening at the upper surface, and provided with an exhaust opening at the side wall. The housing is provided with an inner barrel device. The barrel device comprises a barrel that is fixed with a gear ring on an annular track. A chain wheel is engaged with the gear ring, and installed on the furnace housing through an electric driving device.    USE - Automatic blanking biomass gasification furnace.    ADVANTAGE - The work intensity of the worker is reduced, the working efficiency is improved, and the fuel gas quality is high. The gasification furnace is simple in structure and convenient to use.
NOVELTY - The furnace has a main furnace that is provided with a feeding opening and a material distributing mechanism. The furnace is provided with a through hole below a support saddle. The through hole is sleeved with a spring. A material distributing rod is vertically penetrated in the support saddle at the through-hole. A flange of a cloth rod is connected with a spring. The upper and lower ends of the spring and a support are connected with a pressing device. The pressing device is vertically fixed on the lower end of the material distributing rod.    USE - Double-circulation type straw gasification furnace.    ADVANTAGE - The furnace cracking gas does not directly enter into the cooling water system, the tar content in the furnace gas is reduced, and the gas production quality is improved.
NOVELTY - The device has a venturi dust remover that is positioned between a water fog drop catching device. A water fog filling scrubber is provided with the water fog drop catching device at the downstream. A ceramic Raschig ring layer is equipped with the venturi dust remover. A venture tube is connected with a pressurizing device with the water fog drop catching device. A safety water seal is respectively placed on an air cooler between the double-stage indirect cooler and an upstream electrical tar precipitator.    USE - Biomass gasifying furnace device.    ADVANTAGE - The fuel usage is low, utilization of waste is achieved, energy is saved, emission is reduced, and production cost is reduced.
NOVELTY - The device has a dry distillation structure which is provided in middle section of main gasification chamber. Ash chamber is connected with lower portion of a heat storage grid. A radiation protection cylinder is provided with spiral wall from bottom to top.    USE - Household biomass gasification device.    ADVANTAGE - The biomass gasification device has simple structure, compact structure, convenient operation, and can be manufactured with reduced cost. The heat utilization ratio of the biomass gasification device can be improved effectively. The heat efficiency of the biomass gasification device can be improved. The generation of crack and tar in the biomass gasification device can be prevented.
NOVELTY - The cover has a feeding opening which is provided in the outer side portion of a parallel track. The parallel rail is connected with the walking track that is extended along a water seal tank. The furnace cover and inclined plate are provided between the sliding blocks. A locating plate is connected with the furnace cover top plate. The locating plate is provided with the walking track which is provided with netty whetter. The left sliding block locating plate is connected with running rail which is connected with the left end portion of furnace cover top plate.    USE - Gasification furnace push-pull type water sealing furnace cover.    ADVANTAGE - The sealing performance of the furnace cover is improved effectively, so that safety of the furnace cover can be ensured. The efficiency of the furnace cover can be improved effectively.
NOVELTY - The furnace has a furnace body fixed to a bottom part of a furnace leg. A lower part of a grate is arranged on the furnace body. A panel is located at a lower part of an exhaust port. A gas channel is arranged in the furnace body. A secondary combustion chamber is provided with an oxygen chamber oxygen outlet. The oxygen outlet is connected with the furnace body that is arranged between the gas channel and a heat insulating layer. The furnace body is provided with a hearth unit and an adjustable oxygen valve.    USE - Environmental-friendly biomass particle semi-gasification cooking furnace.    ADVANTAGE - The furnace has high utilization rate, popularization value and heating efficiency and simple structure and operation.
NOVELTY - The method involves forming a partition wall which partitions off a water tank. A circular flow path (6) is provided to connect edge portions of main flow path (25). The previous aeration stirring apparatus and portion of partition wall is removed. A remainder partition wall (22) is provided in both sides of removal portion. A vertical axis aeration stirring apparatus (3) is arranged so that an impeller (9) is located between edge portions of partition (16) and remainder partition wall. The treated water of tank (1a,1b) is circulated by opening (16a) of partition.The water tank accomodates the liquid mixture of an activated sludge.    USE - Repair method of oxidation ditch.    ADVANTAGE - Even when a straightening vane of oxidation ditch is provided in a circular arc flow path, the vertical axis aeration stirring apparatus can form a circulation stirring flow efficiently in tank. The aeration stirring apparatus can be equipped easily. Thus, the repair process of oxidation ditch can be performed easily at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the oxidation ditch.    Tank (1a,1b)    Vertical axis aeration stirring apparatus (3)    Circular flow path (6)    Impeller (9)    Partition (16)    Opening of partition (16a)    Remainder partition wall (22)    Main flow path (25)
NOVELTY - Producing ethanol involves hydrogenating acetic acid from an acetic acid feed stream in a reactor to produce a caide product stream comprising ethanol and acetic acid; reacting acetic acid and ethanol in a reactive distillation column; withdrawing an overhead stream comprising ethyl acetate and a bottom stream comprising ethanol and water; and recovering ethanol from the bottom stream.    USE - For producing ethanol (claimed), used for fuels or human consumption.    ADVANTAGE - The method esterifying the unreacted acid, along with a minor portion of the ethanol, allows improved recovery of ethanol and reduces overall energy requirements.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of reaction system.    Reaction system (100)    Hydrogenation zone (101)    Purification zone (102)    Hydrogenation reactor (103)    Hydrogen feed line (104)    Acetic acid feed line (105)    Caide ethanol product (109)    Vapor stream (110)    Liquid stream (111)
NOVELTY - The gasifier has a bracket whose upper part is fixed with an air exchange processing box. A furnace disk is fixed on the bracket. An inlet is fixed on a central bottom furnace and inserted into a furnace. The furnace is provided with an umbrella cover plate and a tube wall that is formed with an air opening.    USE - Straw gasifier.    ADVANTAGE - The gasifier has simple and reasonable structure. The gasifier is provided with a gas conveying pipeline that is short in length so as to prevent water vapor from being condensed and avoid tar in the gasified gas. The gasifier saves time and space, and is convenient to install. The gasifier generates gas in high temperature, so that the water and the tar are easily condensed inside the furnace.
NOVELTY - The device has a spiral feeder provided in a feeding port of a gasification furnace. An ash outlet is arranged in the bottom region of the gasification furnace. A side wall of the gasification furnace is connected with a primary dust remover through a pipeline. The primary dust remover is connected with a secondary dust remover. The top surface of the dust catcher is provided with an output pipe. The dust catcher is provided with a funnel-shaped ash outlet.    USE - Saponin hydrolysate extraction residue gasification device.    ADVANTAGE - The reliability of the saponin hydrolysate extraction residue gasification device can be improved.
NOVELTY - The structure has a cylinder body provided with a middle part whose top surface is provided with a feeding opening. An upper end of the feeding opening is linked with an outer flange. A left end of a top part of the cylinder body is fixed with a fixing rod that is connected with a horizontal supporting rod. The supporting rod is fixed with a cover body that covers the feeding opening. A clamp plate is movably placed on a pinch plate and fixed with a movable hook. The movable hook is fixed in a strip-shaped groove of a right end of the supporting rod.    USE - Straw gasification furnace sealing structure.    ADVANTAGE - The structure has simple design and better sealing performance, and can effectively press the cover body to seal a straw gasification furnace by driving the supporting rod.
NOVELTY - The furnace has a storage compartment provided with a material receiving/delivering device that is provided with a feeding opening part. The storage compartment is connected with a furnace body and fixed in an inner wall of a tar filter chamber. The tar filter chamber is fixed with a gas channel. A pressing device is arranged in the tar filter chamber. A transmission shaft is connected with the furnace body. A dust-removing device is fixed on a gasification chamber. A circle-shaped shaft sleeve is provided with a rotary blade. A ventilating plate is provided with a net hole aperture area.    USE - Middle suction-type biomass gasification furnace.    ADVANTAGE - The furnace can prevent materials from entering into the dust-removing device by using a baffle plate and rotating a rotary blade by wind power. The furnace ensures stable gas production exempted from time limit.
NOVELTY - The furnace has a furnace body provided with a conical-shaped bottom plate. A bottom surface of the conical-shaped bottom plate is opened with an ash outlet opening that is provided with multiple baffle rods. The conical-shaped bottom plate is fixed with multiple semi-rings. Each semi-ring is arranged on a bottom surface of a chassis. An outer surface of the furnace body is fixed with a rotating shaft through the opening. A top end of the rotating shaft is connected with a handle.    USE - Conical-shaped combustion chassis gasification furnace.    ADVANTAGE - The furnace has better structure and design. The furnace utilizes the rotating shaft so as to stir fuel in a better manner. The furnace avoids accumulation of the fuel during combustion so as to fully burn the fuel.
NOVELTY - The device has a fluidized bed gasification reactor that includes air chamber provided with gasification reaction area and an air distribution plate connected with the reaction area. The sidewall and bottom of air chamber are provided with air inlet opening and slag discharging opening. The steam inlet opening and feeder are arranged in sidewall of the reactor. The reaction area is connected with a smelting furnace having air inlet and slag discharging openings. The smelting furnace is connected with exit of super-heater. A heat exchanger is connected to dirt catcher.    USE - Biomass gasification device for producing combustible gas.    ADVANTAGE - Tar, carbon particles and ash content in the combustible gas can be reduced effectively and safety and reliability of the gasification device can be improved.
NOVELTY - The device has an annular box fixed on an outer wall of a gasification furnace through a bracket. The annular box is connected with a connecting pipe. The gasification furnace is uniformly distributed with the connecting pipe. The connecting pipe is fixed with a flow rate adjusting valve for controlling air quantity. The connecting pipe is equipped with nozzles. Each nozzle is inserted into a hearth of the gasification furnace.    USE - Air inlet regulating device for a biomass gasification furnace.    ADVANTAGE - The device utilizes the flow rate adjusting valve to control biomass gasification of needed air amount in an effective manner so as to improve gas-producing efficiency of the gasification furnace.
NOVELTY - Fuel oil is prepared by (A) pulping active sludge of sewage treatment plant by wet vibration mill, at 100-200 degrees C, making slurry, separating inorganic ash allocated active sludge organic and inorganic ash by centrifugation, and inorganic ash filling; (B) concentrating active sludge organic slurry for vacuum evaporation to obtain content of active sludge of 30-40% and organic slurry; and (C) performing pyrolysis, gasification, and oiling. Organic slurry is pumped into cracking furnace for pyrolysis, where pre-heating temperature is 20-30 minutes.    USE - Method for preparing fuel oil.    ADVANTAGE - Oil producing rate is improved to 60%. Utilization rate of oil yield and unit volume furnace is improved by 3-4 times.    DETAILED DESCRIPTION - Fuel oil is prepared by (A) pulping active sludge of sewage treatment plant by wet vibration mill, at 100-200 degrees C, making slurry, separating inorganic ash allocated active sludge organic and inorganic ash by centrifugation, and inorganic ash filling; (B) concentrating active sludge organic slurry for vacuum evaporation to obtain content of active sludge of 30-40% and organic slurry; and (C) performing pyrolysis, gasification, and oiling. Organic slurry is pumped into cracking furnace for pyrolysis, where pre-heating temperature is 20-30 minutes. Temperature of vertical bundle cracking furnace is 500-700 degrees C. Vertical bundle cracking flame heating temperature is 600-800 degrees C. The temperature of drying tunnel is 300-400 degrees C. The vertical bundle cracking furnace is sealed vertical furnace lining refractory brick as insulation layer. Burner is arranged on the lower part of the vertical tube.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a method for preparing fuel oil (Drawing includes non-English language text).
NOVELTY - Manufacture of methane separation membrane and carbon dioxide separation membrane involves preparing metal alkoxide solution by stirring and mixing an acid catalyst, water and an organic solvent, then adding tetraalkoxysilane, stirring, mixing, then adding a hydrocarbon group-containing trialkoxysilane containing hydrocarbon group chosen from 1-6C alkyl group and phenyl group, stirring and mixing, coating an inorganic porous support using the prepared metal alkoxide solution, and firing the inorganic porous support coated with metal alkoxide solution at 30-300 degrees C.    USE - Manufacture of membrane used for separation of carbon dioxide and methane for fuel gas.    ADVANTAGE - The methane separation membrane and carbon dioxide separation membrane have excellent thermal resistance, durability and corrosion resistance.
NOVELTY - Preparing sitagliptin involves reacting (S)-benzyl(1,4-dioxo-4-(3-(trifluoromethyl)-5,6,7,8-tetra hydro-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-1-(2,4,5-trifluorophenyl)butan-2-yl)carbamate in presence of removal agent of amine protecting group and a carbonyl reducing agent.    USE - For preparing sitagliptin (claimed); and for treating diabetes mellitus type 2.    ADVANTAGE - The method is cost-effective and environmentally friendly in production process over the conventional techniques because the production process doesn't require expensive heavy metals such as Rh and Ru and is also advantageous in cost because the production process doesn't require chiral compounds other than a naturally occurring amino acid, L-aspartic acid.    DETAILED DESCRIPTION - Preparing sitagliptin involves reacting (S)-benzyl(1,4-dioxo-4-(3-(trifluoromethyl)-5,6,7,8-tetra hydro-(1,2,4)triazolo(4,3-a)pyrazin-7-yl)-1-(2,4,5-trifluorophenyl)butan-2-yl)carbamate of formula (X) in presence of removal agent of amine protecting group and a carbonyl reducing agent.    PG'=an amine protecting group.    An INDEPENDENT CLAIM is included for new intermediate compounds of formulae (VII)-(X) and (XIII)-(XV).
NOVELTY - The apparatus (100) has water electrolyzer (1031) to manufacture hydrogen and oxygen using natural energy. A hydrogen storage/supply unit (1021) desorbs the hydrogen of hydrogen storage element (1011) to manufacture dehydrogenation element (1012) while adding hydrogen to dehydrogenation element and manufacturing hydrogen storage element. The hydrogen is supplied to storage/supply unit during storage of natural energy. The hydrogen stored in storage/supply unit is supplied to engine generator (1022) which supplies heat to storage/supply unit, during supply to exterior as electric power.    USE - Energy storage/supply apparatus for use with large-scale power generation equipment.    ADVANTAGE - The low-cost energy storage/supply apparatus can be provided such that natural long-term energy fluctuations can be leveled out at low cost. The shortage of conventional energy can be compensated.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the energy storage/supply apparatus. (Drawing includes non-English language text)    Energy storage/supply apparatus (100)    Hydrogen storage element (1011)    Dehydrogenation element (1012)    Hydrogen storage/supply unit (1021)    Engine generator (1022)    Water electrolyzer (1031)
NOVELTY - The device has multiple steam nozzles connected with a steam pipeline. Hanging and lower disks are connected with a circulating cooling water pipeline. The hanging and lower disks are formed as a round disk-shaped structure that is uniformly formed with lower material holes. Upper and lower hanging scaffolds are fixed on a lifting plate. The lifting plate is connected with a rotating handle, and freely rotates in a range of about 36 degrees. A bottom part of a suspended plate and an upper part of a lower pallet are fixed with the steam nozzles and a temperature control probe.    USE - Steam spraying device for a down suction type biomass straw gasification furnace.    ADVANTAGE - The device is simple and convenient to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a steam spraying device.
NOVELTY - The device has a furnace body whose side is provided with a high temperature cracking chamber. Another side of the furnace body is provided with a gasification combustion chamber. Upper ends of the high temperature cracking chamber and the gasifying combustion chamber are respectively provided with two feeding openings. A feeding device is connected with an end of a draft fan. An end of a guide pipe is connected with the gasification combustion chamber. A side of the gasification combustion chamber is fixed with an output tube.    USE - Biomass gasification cracking device.    ADVANTAGE - The device is simple in structure and inexpensive, and has high heating efficiency and better dust-removing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification cracking device in partial section.
NOVELTY - The furnace has a feeding device provided with a furnace body. A furnace top viewing port is arranged on a top part of the furnace body. Height of the furnace body is 120 cm. A cone is provided with a high temperature reaction zone and a cone horn mouth burning area. A honeycomb-shaped slag discharging fire grate is arranged in the furnace body and connected with the furnace body. A bottom part of a gasification furnace is provided with a circulating air device. A lower ventilation opening and a filtering rotational flow dust remover are connected with the furnace body.    USE - Clean production biomass dry French gas purifying gasification furnace.    ADVANTAGE - The furnace is easy to clean, convenient to operate and simple in structure, has high thermal value and utilization of agriculture and forestry waste resource such as biomass straw, branch, rice hull and fruit shell. The furnace ensures better environment-friendly effect and better sewage discharge. The furnace ensures heat value of fuel gas about 5500 to 6000kj/m3.    DESCRIPTION OF DRAWING(S) - The drawing shows a cut-away front view of a clean production biomass dry French gas purifying gasification furnace.'(Drawing includes non-English language text)'
NOVELTY - Baffled discharge device has fermentation container unit, fermentation tank, feeding unit, discharge pipe, discharge opening and marsh gas exhaust opening. The fermentation container unit is present inside the fermentation tank. The feeding unit has an opening which is a hollow pipe structure. The upper end opening of upper portion of the fermentation container unit is present inside the fermentation tank.    USE - The baffled discharge device is useful for performing anaerobic fermentation of straw.    ADVANTAGE - The baffled discharge device has increased feeding efficiency and buoyancy and rising force to push raw material liquid, and utilizes gravity and biogas pressure to discharge and reuse the material.    DETAILED DESCRIPTION - Baffled discharge device has fermentation container unit, fermentation tank, feeding unit, discharge pipe, discharge opening and marsh gas exhaust opening. The fermentation container unit is present inside the fermentation tank. The feeding unit has an opening which is a hollow pipe structure. The upper end opening of upper portion of the fermentation container unit is present inside the fermentation tank. The lower end opening of the fermentation container unit is connected with the discharge pipe. The discharge pipe and the discharge opening of the fermentation tank are further provided with the marsh gas exhaust opening on the outer side of the fermentation tank.
NOVELTY - The system has circulation system (2) arranged between preprocessing device (1) and hydrolysis acidification reactor (3), and another circulation system (4) arranged between hydrolysis acidification reactor and methane-producing reactor (5). The upper and lower ends of preprocessing device are provided with preprocessing feed inlet (11) and outlet (12). The upper and lower ends of hydrolysis acidification reactor are provided with reflux feed inlet (31,34) and outlets (32,33). The lower and upper ends of methane-producing reactor are provided with gas outlets (52,53) and gas inlets (51,54).    USE - Anaerobic digestion system for sludge treatment (claimed).    ADVANTAGE - The yield of biogas produced from the less amount of sludge can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion system.    Preprocessing device (1)    Circulation systems (2,4)    Hydrolysis acidification reactor (3)    Methane-producing reactor (5)    Preprocessing feed inlet (11)    Preprocessing feed outlet (12)    Reflux feed inlet (31,34)    Reflux feed outlets (32,33)    Gas inlets (51,54)    Gas outlets (52,53)
NOVELTY - The method involves producing state of charging and amending state of charging of air-zinc-air fuel cell (100) through voltage supply. The stored fuel cell is existed in memory through the calculated remain capacitance value.    USE - Method for measuring state of charging of zinc-air fuel cell.    ADVANTAGE - The method involves producing state of charging and amending state of charging of air-zinc-air fuel cell through voltage supply, and thus performs efficient fuel cell operation, reduces error of charging state by re-computing, enhances battery stability through correct state of charging computation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic configuration for measuring state of charging. (Drawing includes non-English language text).    Air-zinc-air fuel cell (100)    Voltage sensor (210)    Current sensor (220)    Temperature sensor (230)    Memory (250)
NOVELTY - The method involves introducing biomass into thermolysis reactor. The non-oxidizing gas is introduced through bed so as to cause automatic elutriation of product carbon. The deep fluidized bed is heated so that temperature of deep fluidized bed is set to 360-490 degree. An effluent reactor stream comprising hot carbon particles, volatiles, gas, aerosols, and vapors are produced during thermolysis of shredded biomass. The elutriated carbon particles are removed from effluent reactor stream. The residence time of non-oxidizing gas in the reactor is greater than 2 seconds.    USE - Method for performing thermolysis of shredded biomass.    ADVANTAGE - The shredded biomass particles can be thermolyzed efficiently. The thermolysis process can be performed easily. The operating cost can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for performing thermolysis of shredded biomass particles.
NOVELTY - Preparing foliar-fertilizer by livestock breeding biogas slurry involves 1) anaerobic fermenting the biogas slurry produced in the livestock breeding; 2) air floating the fermented biogas slurry by dissolved gas, and removing the suspended matter and impurity; 3) membrane filtering the air floated biogas slurry by inorganic ceramic membrane; and 4) using the membrane filtered liquid partially as the foliar-fertilizer or foliar-fertilizer coarse product. The inorganic ceramic membrane in the step (3) is the special inorganic ceramic membrane with less than 200 nm of pore diameter.    USE - For preparing foliar-fertilizer or foliar-fertilizer coarse product by livestock breeding biogas slurry (e.g. poultry breeding biogas slurry) (claimed).    ADVANTAGE - The process is simple and feasible in the process flow, easy and simple to operate, and solves the problem of biogas slurry process, turns waste into wealth, and realizes the recycling of the high value-added resource. The process does not cause secondary pollution in the production process without adding any additional agent to ensure the safety, and the fertilizer is suitable for chicken, duck and so on poultry farm.
NOVELTY - Composting sludge comprises: (a) uniformly mixing straw, mud and mineralization garbage, adjusting water content mass ratio to 45-65%, flattening and paving a layer of mineralized waste on surface of the mixture by forced ventilation oxygen supply method, primarily fermenting and composting the mixture; and (b) mixing fermented compost lower layer and upper mineralized waste layer, adjusting the water content mass ratio to 45-50%, secondarily fermenting and composting the mixture, and decomposing the compost mixture.    USE - The method is useful for composting sludge.    ADVANTAGE - The method is capable of economically composting the sludge with improved nitrogen content and high quality.
NOVELTY - Method for processing vegetable waste, involves (a) subjecting the vegetable waste to high speed rotor, (b) adding alkaline substances to crushed product, (c) regulating pH of the mixture to 8-9, (d) filtering the mixture and concentrating and drying the mixture, (e) inoculating microorganisms to mixture and adding additives to the processed product, and (f) drying the product to obtain microbial fertilizer.    USE - The method is useful for processing vegetable waste.
NOVELTY - A 2-amino-4,5-bis-(2-methoxy-ethoxy)-benzoic acid (V), is new.    USE - For preparing (6,7-bis-(2-methoxy-ethoxy)-quinazolin-4-yl)-(3-ethynyl-phenyl)-amine hydrochloride (I) (erlotinib hydrochloride) useful as anticancer drug (claimed).    ADVANTAGE - The process has cheap and easily obtained starting materials; has mild conditions; does not require special device; and is suitable for industrial production. The process for synthesis of erlotinib hydrochloride, has low cost raw material; is simple synthesis method; has low pollution; and is suitable for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of the compound (V), involving: (a') reducing 4,5-bis-(2-methoxy-ethoxy)-2-nitro-benzoic acid (IV) by a reducing agent;    (2) preparation of the compound (IV) involving: (a'1) oxidizing 4,5-bis-(2-methoxy-ethoxy)-2-nitro-benzaldehyde (III);    (3) preparation of the compound (III) involving: a) taking 3,4 -dihydroxy benzaldehyde as raw material, under the organic alkali effect and reacting 3,4-dihydroxy benzaldehyde with 1-halo-2-methoxy-ethane compound of formula X-CH2-CH2-OCH3 to obtain 3,4-bis-(2-methoxy-ethoxy)-benzaldehyde (II); b) carrying out nitration in the mixed acid for the compound (II) to obtain the compound (III);    (4) preparation of (6,7-bis-(2-methoxy-ethoxy)-quinazolin-4-yl)-(3-ethynyl-phenyl)-amine hydrochloride (I) involving: a1) cyclization of the compound (V) to obtain 6,7-bis-(2-methoxy-ethoxy)-3H-quinazolin-4-one (VI); b1) subjecting the compound (VI) to chlorination to obtain 4-chloro-6,7-bis-(2-methoxy-ethoxy)-quinazoline (VII); c1) reacting the obtained compound (VII) with meta-aminophenylacetylene to obtain (6,7-bis-(2-methoxy-ethoxy)-quinazolin-4-yl)-(3-ethynyl-phenyl)-amine (VIII); and d1) reacting the obtained compound (VIII) with hydrogen chloride gas to obtain the compound (I).    x=Br, Cl or I.
NOVELTY - Preparing (M1) astragaloside involves preparing bacteria, mycete and yeast into bacteria suspension or spore suspension, inoculating into seed culture medium, culturing at 28 degrees C at 220 revolutions per minute (rpm) for 24-48 hours, obtaining seed liquid, inoculating the seed liquid into a fermenting culture medium, culturing at 28 degrees C at 220 rpm for 24-48 hours, adding astragalosides to convert for 48-96 hours, obtaining conversion liquid, extracting the conversion liquid by organic solvent, and separating and purifying by the macroporous resin, obtaining astragaloside purified product.    USE - For preparing astragaloside useful for making drug for treating cardiovascular disease, cerebrovascular disease, anticancer, antiviral or diabetes mellitus (where the cardiovascular disease is vital myocarditis).    ADVANTAGE - The method can avoid the deficiency of damage on the saponin, serious pollution and bad teleonomy while hydrolyzing astragalosides by a chemical method; can solve the problem of unstable enzyme stability while hydrolyzing astragalosides by enzyme method; has no pollution, strong specificity and high conversion rate; and the purity of the prepared astragaloside is higher than 99.9%. The method provides mild reaction condition, simple operation, low cost, little pollution and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an astragaloside injection, which is prepared into 1000 ml through compensating water for injection with astragaloside (1 g) prepared according to method (M1), ethanol (200 ml), propylene glycol (200 ml) and glucose (100 g).
NOVELTY - Preparation of ammonia comprises crushing calcium oxide, adding the calcium oxide to ammonium chloride solution and converting into ammonia and calcium chloride by-product.    USE - Process of producing ammonia.    ADVANTAGE - The process is simple and energy saving, requires less investment, and can be applied to industrial production.
NOVELTY - A new method for the preparation of active pharmaceutical drug valsartan and its intermediates, is disclosed. In the first step, biphenyl derivative is synthesized from 2-aminobenzonitrile, alkyl nitrite and benzyl alcohol. This is then oxidized to the corresponding aldehyde by using guanidine nitrate, phosphorus pentoxide (P2O5) supported on silica gel, followed by Schiff base formation with (S)-valine methyl ester and its reduction with sodium borohydride (NaBH4) supported on aluminum oxide (Al2O3). This is then subjected to N-acylation with pentanoic acid in presence of a catalyst, tetrazole formation and finally its alkaline hydrolysis afforded valsartan in a substantially pure enantiomeric form. The process developed is environmentally-friendly, economic and efficient. Image 0/0
NOVELTY - A new method for the preparation of valsartan and its intermediates, is disclosed. In the first step, 2-cyano-4- methylbiphenyl is synthesized from 2-aminobenzonitrile, alkyl nitrite and toluene. This is then subjected to side chain bromination. This is used for N-alkylation of (S)-valine methyl ester and its N-acylation with pentanoic acid in presence of a catalyst. The resulting compound is converted into tetrazole derivative and finally its alkaline hydrolysis afforded valsartan in a substantially pure enantiomeric form. The method is economically, efficiently and environmentally-friendly carried out by a simple process. Image 0/0
NOVELTY - Preparing oxazole-2-carbaldehyde comprises: adding oxazole and ester solvent in a reaction kettle; dropping n-butyllithium solution and altering a temperature of the system; dropping the n-butyllithium solution; then keeping temperature; dropping N-carboxaldehyde piperidine in the system; returning temperature of the system and keeping warm; post-treating the system and crystallizing; filtering and spraying the filter cake by an ester solvent; air-drying; and dropping the eluted water solution with concentration of 5-20% in obtained (oxazol-2-yl(1-piperidyl)methoxy)lithium.    USE - The process is useful for preparing oxazole-2-carbaldehyde.    ADVANTAGE - The process is simple and eco-friendly for preparing oxazole-2-carbaldehyde, which is stable.    DETAILED DESCRIPTION - Preparing oxazole-2-carbaldehyde comprises: (a) adding 1 g/5-50 ml of oxazole and ester solvent in a reaction kettle under stirring; (b) dropping n-butyllithium solution and altering a temperature of the system to 90-60 degrees C; (c) dropping the n-butyllithium solution at 90-60 degrees C; (d) then keeping temperature for 2-8 hours at 90-60 degrees C, where the mole ratio of the oxazole and n-butyllithium is 1:1-1.5; (e) dropping N-carboxaldehyde piperidine in the system at 90-60 degrees C; (f) returning temperature of the system to 20-30 degrees C and keeping warm for 32-72 hours at 20-30 degrees C, where the mole ratio of the oxazole and the N-carboxaldehyde piperidine is 1:1-10; (g)post-treating the system to 5-10 degrees C, stirring and crystallizing; (h) filtering and spraying the filter cake by an ester solvent; (i) air-drying under the protection of the nitrogen to obtain (oxazol-2-yl(1-piperidyl)methoxy)lithium, where the dosage ratio of the oxazole and the ester solvent is 1 g/2-10 ml; and (j) dropping the eluted water solution with concentration of 5-20% in the (oxazol-2-yl(1-piperidyl)methoxy)lithium until the system is cleared.
NOVELTY - Oxalate ester compound is dissolved in tetrahydrofuran solvent, an organic base catalyst is added, the product is dissolved in tetrahydrofuran solvent, acetate is added and stirred at 0-10 degrees C. Acetic ester/furan mixture is added into diethyl oxalate/tetrahydrofuran mixture, and reacted at 20-60 degrees C for 1-2 hours. The reaction solution is acidified using dilute hydrochloric acid, organic alkali catalyst is removed, dried with saturated sodium chloride solution, decompressed and distilled to obtain butanone diacid diester compound.    USE - Manufacture of butanone diacid diester compound used as drug intermediate.    ADVANTAGE - The butanone diacid diester compound is easily and economically manufactured at high yield under mild reaction conditions without affecting environment.
NOVELTY - The system has engine (4), generator (6) and storage battery (7) that are connected in sequence. A voltage detecting device (8), electrolytic power supply controller (9) and electrolytic cell (10) are connected in sequence. The voltage detection device and the storage battery are electrically connected with an air outlet (2) of the electrolytic cell through an air pipe. The air pipe is connected with an air inlet (3) of the engine.    USE - Electrolyzed water based fuel-efficient system for automobile.    ADVANTAGE - The electrolyzed water based fuel-efficient system can use the redundant electrical energy sent by motor efficiently, thus the efficiency of engine is improved. The fuel-efficient system can reduce discharge amount of carbon dioxide. The energy consumption of the fuel-efficient system is reduced. The voltage detection device can avoid the exhaustion of electric energy stored in storage battery. The damage to the electrolytic cell due to excessive air pressure is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyzed water based fuel-efficient system.    Air outlet (2)    Air inlet (3)    Engine (4)    Generator (6)    Storage battery (7)    Voltage detecting device (8)    Electrolytic power supply controller (9)    Electrolytic cell (10)
NOVELTY - A Brettanomyces mutant strain (deposit number: KCCM11216P) is new, where the strain has selenium cis-side group for converting effective carbon source into ethanol.    USE - Brettanomyces mutant strain for producing biofuel.    ADVANTAGE - The Brettanomyces mutant strain increases the yield of biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing Brettanomyces mutant strain (deposit number: KCCM11216P) involving cultivating the culture medium, and fermenting carbon source of ethanol including Brettanomyces mutant strain.
NOVELTY - The system has a flange (1) which is provided with vacuum rubber ring (5). A glass tube (2) with blackened surface (3) at one end is provided. A parabolic reflector (6) is located with the flange.    USE - Hydrogen production system using solar energy.    ADVANTAGE - The obtained energy is very economical and ideal. The system does not produce any pollution to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production system.    Flange (1)    Glass tube (2)    Blackened surface of glass tube (3)    Vacuum rubber ring (5)    Parabolic reflector (6)
NOVELTY - A crystallized methane biogas reactor is flowed into the organic waste, and digested liquid generated from anaerobic digestion reaction is treated. The settling tank is entered to the decomposition of organic wastes, and suppressed by separation film installed at the settling tank. The organic loading reduction is inflowed to settling tank, high concentrated organic waste is injected to the methane reaction bath, and treated water is introduced into the methane reactor through an acid reactor. Thus, pretreatment of high concentrated organic waste is enabled.    USE - Pretreatment of high concentrated organic waste produced during upflow anaerobic sludge blanket.    ADVANTAGE - The high concentrated organic waste is economically and efficiently pretreated.    DETAILED DESCRIPTION - A crystallized methane biogas reactor is flowed into the organic waste, and digested liquid generated from anaerobic digestion reaction is treated. The decomposition of organic wastes and load of the organic wastes are reduced in the weight ratio of 10-20. The settling tank is entered to the decomposition of organic wastes, and oil is reduced. The settling tank is suppressed by separation film installed at the settling tank for 3-5 hours. The organic loading reduction is inflowed to the settling tank and passed through precipitation process. The high concentrated organic waste is injected to the methane reaction bath, and treated water is introduced into the methane reactor through an acid reactor by removing upper and lower portion of settling tank. Thus, pretreatment of high concentrated organic waste is enabled.
NOVELTY - The method involves forming a fiber reinforced resin layer (21) in an outer periphery of an inner container (20), and thermosetting the fiber reinforced resin layer, where the fiber reinforced resin layer comprises a hoop winding layer in which a fiber is wound at a right angle direction with respect to an axis of the inner container. An induction heating coil (40) is arranged on an outer periphery of the fiber reinforced resin layer and moved to an axial direction of the inner container along a surface of the fiber reinforced resin layer.    USE - Method for manufacturing a gas holder of a fuel cell system of a motor vehicle.    ADVANTAGE - The method enables performing the thermosetting of the fiber reinforced resin layer by using induction heating at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas holder.    Inner container (20)    Fiber reinforced resin layer (21)    Thermosetting apparatus (30)    Induction heating coil (40)    Coil movement apparatus (41)
NOVELTY - A fuel reforming system comprises modifier (40) provided with vaporization part (41) which vaporizes modified water and modification part (42) which produces fuel gas by steam reforming reaction of raw fuel and modified water vaporized in vaporization part and S/C control part (120) which controls ratio (S/C) of the number of moles of water vapor with respect to the number of moles of carbon in raw fuel in modifier.    USE - A fuel reforming system for fuel cell system.    ADVANTAGE - The control method of the fuel reforming system and the fuel reforming system can appropriately control volume of water vapor supplied to the modifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for control method of fuel reforming system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system containing the fuel reforming system. (Drawing includes non-English language text).    Modifier (40)    Vaporization part (41)    Modification part (42)    Combustion chamber (50)    Control part (120)
NOVELTY - A hydrogen generating apparatus (1) comprises burner (2) which burns fuel and produces combustion gas, inner cylinder (14) heated by combustion gas of burner, outer cylinder (15) positioned on outer side of inner cylinder, and modification catalyst (4) which modifies supplied source gas to produce reformed gas and provides modification-catalyst layer (16) arranged between inner and outer cylinder, wherein diameter of inner cylinder to downstream of inner cylinder is larger than that upstream of flow.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Damage to modification catalyst is reduced during repeated start-stop operation of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a hydrogen generating apparatus which has an evaporation part. (Drawing includes non-English language text).    Hydrogen generating apparatus (1)    Burner (2)    Modification catalyst (4)    Inner cylinder (14)    Outer cylinder (15)
NOVELTY - Producing a liquid fuel from a cellulose-containing solid starting material, comprises contacting the solid starting material with a mixture comprising diethylene glycol, glycerol and p-toluenesulfonic acid, where ratio of diethylene glycol to glycerol in the mixture is 1:1-20:1 by weight.    USE - The method is useful for producing liquid fuel from cellulose-containing solid starting material, where the liquid fuel is useful for combustion engines (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a liquid fuel produced by the method.
NOVELTY - Handling transportation and supply of large amount of small particles like pellets, granules, small-chips, powder and the like obtained by biomass and peat, comprises: (a) providing a liquid fluid adapted to be mixed with the small particles; (b) mixing the small particles with the liquid fluid to obtain a mixture to be delivered; (c) providing a suitable pipeline and connected unit for pumping a fluid along the pipeline; (d) pumping the mixture along the pipeline from first location to a second location; (e) collecting the mixture at the second location.    USE - The method and apparatus are useful for handling transportation and supply of large amount of small particles like pellets, granules, small-chips, powder and the like obtained by biomass and peat (all claimed).    ADVANTAGE - The method and apparatus can be efficiently and reliably used in handling transportation and supply of torrefied biomasses and peat, in particular in the form of agro-pellet.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is apparatus for handling transportation and supply of large amount of small particles like pellets, granules, small-chips, powder and the like obtained by biomass and peat, comprising: unit for producing a mixture of the small particles and a liquid fluid vessel; unit for pumping the mixture along a suitable pipeline adapted to deliver the mixture at a required distance.
NOVELTY - Auto-combustible torch made of a combustible component with the shape of a log that has a diameter of 48-16 inches and length of 6-48 inches, is claimed. A vertical chimney of diameter one half -4 inches and length of 10-22 inches, is connected to an air intake at angle of 90-135 degrees , preferably 90 degrees . The torch is treated to destroy any invasive insects or fungi and the combustible component is solid wood, wood particles, densified wood products or recycled wood products, preferably solid wood.    USE - Used as auto-combustible torch.    ADVANTAGE - The auto-combustible torch: can be transported from one region to another without the risk of spreading invasive insects or diseases; and exhibits reduced duration for heat treatment and renders drying more efficient.    DETAILED DESCRIPTION - Auto-combustible torch made of a combustible component with the shape of a log that has a diameter of 48-16 inches, preferably 12 inches and a length of 6-48 inches, preferably 12 inches is claimed. At least one main vertical chimney of the diameter of one half -4 inches, preferably 2.25 inches and length of 10-22 inches, preferably 10.5 inches is connected to at least one air intake of the diameter one quarter -2.5 inches, preferably 2 inches, at an angle of 90-135 degrees , preferably 90 degrees . The torch is treated to destroy any invasive insects or fungi and the combustible component is solid wood, wood particles, densified wood products or recycled wood products, preferably solid wood
NOVELTY - The method comprises dipping ground magnesium and transition metal in an electrolyte solution. The electrolyte solution is soluble transition metal salt. Alkali-metal chloride is used as the electrolyte.    USE - The method is useful for producing hydrogen from water.    ADVANTAGE - The method is capable of simply producing hydrogen with increased productivity.
NOVELTY - Producing hydrogen comprises immersing metal chips in container with electrolyte solution, where for the purpose of an increase in the volume of isolated hydrogen, through chips, passing electrical current and accelerating dissolution of metal with current power.    USE - The method is useful for producing hydrogen (claimed) for fuel cells.
NOVELTY - Transporting compost, where the compost is transported at a temperature of less than 20 degrees C, comprises subjecting a mass of compost to subatmospheric pressure and removing water vapor from the mass of compost resulting in a cooled mass of compost, and transporting the cooled mass of compost.    USE - The method is useful for transporting compost.    ADVANTAGE - The method can be carried out in a simple and cost-effective manner. The method can be possible to contact the compost with a piece of cloth, which may help to accelerate evaporation of water from the compost.
NOVELTY - A reduced type titanium oxide is synthesized by synthesizing reduced type titanium oxide by reducing rutile type titanium oxide at less than or equal to 400 degrees C.    USE - Synthesis of reduced type titanium oxide for solar cell or fuel cell.    ADVANTAGE - The method synthesizes reduced type titanium oxide with desired nano structures.
NOVELTY - The apparatus (100) has a hollow shaft that is provided with an opening (21) through which electrolyte solution flows in and discharged out. Specific rotating-electrode (32) is positioned by spacing apart with respect to another rotating-electrode (31). A pair of outflow component (41,42) discharges out the electrolyte solution. A pair of partition (61,62) partition off the inner side of the housing into spaces (51,52) facing the outflow components.    USE - Apparatus for decomposing electrolyte solution e.g. water.    ADVANTAGE - The flow of electrolyte solution can be controlled. Efficiency of the apparatus can be improved. The gas of oxygen and hydrogen can be recovered efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the apparatus for decomposing electrolyte solution. (Drawing includes non-English language text)    Opening (21)    Rotating-electrodes (31,32)    Outflow components (41,42)    Spaces (51,52)    Partitions (61,62)    Electrolyte solution decomposition apparatus (100)
NOVELTY - The manufacturing method involves forming a multilayer film structure which includes a fuel electrode layer (5), a solid oxide electrolyte layer (6), and an oxidizing agent electrode layer (7) on the surface of a sacrificial component. The sacrificial component has an external shape corresponding to the shape of a gas passage. The sacrificial component is removed after the completion of the formation of the multilayer film structure.    USE - Manufacturing method for fuel cell structure.    ADVANTAGE - Eliminates the need for an assembly process, thus ensuring excellent mass productivity.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of a fuel cell structure.    Inlet port (1)    Exhaust port (2)    Fuel electrode layer (5)    Solid oxide electrolyte layer (6)    Oxidizing agent electrode layer (7)
NOVELTY - The apparatus has a connecting pipe for the input of workable medium and selection of a target component. A heat exchanger and a static mixer are used for mixing of vegetable oil and methanol. A reaction chamber is preheated in the ring-shaped peripheral cavity. The reaction chamber is divided into zones through the installation of the changeable insert and is filled with ferromagnetic particles and catalyst. The catalyst is composed of sodium/sodium hydroxide/aluminum oxide or potassium/potassium hydroxide/aluminum oxide.    USE - Apparatus for production of biodiesel fuel.
NOVELTY - The system comprises a material container, a pretreatment component for cutting, drying and grinding the material, a classification component for classifying the pretreated material, a material silo, a feed device for containing the classified material and feeding a constant amount of the classified material, a curing and shaping device adapted to extrude the classified material to form solid shaped products, a conveyor for distributing the material to the pretreatment component, and a control unit for controlling the distribution of material to the pretreatment component.    USE - The system is useful for manufacturing shaped solid products.    DETAILED DESCRIPTION - The system comprises a material container, a pretreatment component for cutting, drying and grinding the material, a classification component for classifying the pretreated material, a material silo, a feed device for containing the classified material and feeding a constant amount of the classified material, a curing and shaping device adapted to extrude the classified material to form solid shaped products, a conveyor for distributing the material to the pretreatment component, and a control unit for controlling the distribution of material to the pretreatment component, where: the classifying component, the material silo, the feed device, the curing and shaping device are designed for forming the totally automatic operation system; and the material silo, the feed device, the curing and shaping device and other components automatically adjust the conditions of the system according to the properties of different materials.
NOVELTY - The method involves pre-processing solid biomass to produce modified solid biomass. The pre-processed biomass is contacted with inorganic material e.g. aluminum sulfate, present in an effective amount for increasing pyrolysis yield of an organic liquid product to form pre-treated biomass. The solid pre-treated biomass is subjected to pyrolysis reaction in the presence of the inorganic material to produce the organic liquid product. The solid biomass is subjected to heat treatment at temperature ranging from 100 degree Celsius to 375 degree Celsius.    USE - Method for producing an organic liquid product e.g. liquid pyrolysis product (claimed) such as volatile condensable oil or bio-oil product, from solid biomass derived from forestry, agriculture and cellulosic waste materials. Can also be used for producing a low value product e.g. unsaturated product, oxygen containing product and annular hydrocarbon product, and a higher value product e.g. petrol and jet fuel product.    ADVANTAGE - The method enables pretreating biomass material to allow biomass conversion via pyrolysis to result in higher yields of organic liquids and to improve quality of bio-oil. The method enables selecting solvent to improve penetration of catalyst into biomass when dry biomass can be more difficult to penetrate and allowing demineralization to improve control over reaction of the biomass. The method enables solid biomass particles to be agitated to reduce size of the solid biomass particles. The method enables removing metals to reduce ash content and prevent metal contamination of waste products, thus facilitating disposal of waste by providing an uncontaminated waste product and reducing cost of disposing of the waste product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for pretreating solid biomass for pyrolysis.
NOVELTY - The apparatus (100) has a reformer (1) that forces a raw material to undergo a reforming reaction to generate a hydrogen-containing gas. A hydrodesulfurizer (4) removes the sulfur compounds in the raw material. A controller (12) uses the switches (17,18) to change the flow of raw material to the lower raw material flow path (15) when the oxygen concentration in the raw material is relatively low, and to change the flow of the raw material to the upper raw material flow path (16) when the oxygen concentration in the raw material is relatively high.    USE - Hydrogen generating apparatus for fuel cell system equipped with fuel cell (all claimed).    ADVANTAGE - The density of the sulfur compound in the raw material supplied to the reformer can be reduced due to the oxygen concentration in the raw material that de-sulfurizes in the high state using the hydrodesulfurization device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Reformer (1)    Hydrodesulfurizer (4)    Controller (12)    Lower raw material flow path (15)    Upper raw material flow path (16)    Switches (17,18)    Hydrogen generating apparatus (100)
NOVELTY - The apparatus (100) has a modifier (1) which is provided to force a raw material to undergo reforming-reaction to generate a hydrogen-containing-gas. The modifier is heated by combustor (2). A controller (5) is provided to set control temperature of modifier to primary temperature, when oxygen concentration in raw material during primary state is low. The control temperature of modifier is changed into secondary temperature that is higher than primary temperature, when oxygen concentration in raw material during secondary state is higher than primary state.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The control temperature of modifier is changed into secondary temperature that is higher than primary temperature, so that the oxygen concentration in raw material is determined to be excessive temperature rise of modifier can be reduced. The electric power generation efficiency of the hydrogen generating apparatus can be improved. The deterioration of the modifier of generating apparatus can be prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) 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)    Modifier (1)    Combustor (2)    Temperature detector (3)    Controller (5)    Hydrogen generating apparatus (100)
NOVELTY - Preparing a catalyst comprises (a) providing a catalyst-shaped body (40) containing a number of flow channels, which have one inlet opening and an outlet opening, and (b) impregnating the flow channels with a solution (12, 13) of a compound of a catalytically active component, in a stepwise manner.    USE - The catalyst is useful for: stationary and/or mobile exhaust gas purification, operating fuel cells, shift-reactions and/or reforming (claimed).    ADVANTAGE - The method conserves the activity of the catalytically active component, thus it is cost savings, and is simple to achieve the desired gradient of catalytically active component, and provides an improved catalyst in an improved manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the catalyst obtainable or obtained by the above method.    DESCRIPTION OF DRAWING(S) - The drawings (1 and 2) show a schematic representation of the method for preparing the catalyst.    Storage vessel (10)    Solution (12)    Stamp (20)    Cylindrical container (30)    Pipe (32)    Catalyst-shaped body (40)
NOVELTY - The method comprises performing the combustion of the fossil fuel sub-stoichiometrically while essentially producing carbon monoxide in fossil fuel power plants, and supplying hydrogen produced in the combustion process to make the carbon monoxide to react with hydrocarbon-containing fuels. The fossil fuel comprises coal, natural gas or heavy oil. The hydrogen production is carried out using renewable energy such as wind-, solar- or geothermal energy.    USE - The method is useful for reducing carbon dioxide emissions from combustion processes in fossil fuel power plants for producing hydro carbonaceous fuel such as methane, methanol, gasoline or diesel fuel (claimed).    ADVANTAGE - The method ensures economic, effective and simple reduction of carbon dioxide emissions in the fossil fuel power plants thus increasing energy efficiency of the power plant and improving purity and quality of the fuel.
NOVELTY - The method comprises supplying an agent acting in a reducing manner and/or reacting with oxygen in a competing reaction to an exhaust gas (OG), introducing a supplementary agent directly in a furnace vessel (2) of the furnace, and supplying a catalytic effective solid material accelerating a reduction reaction or the competing reaction. A temperature of the exhaust gas is measured at a sampling point, and a metering of the agent takes place when this exceeds a predetermined value. The metering in flow direction of the exhaust gas is observed according to the sampling point.    USE - The method is useful for reducing emission of nitrogen oxides in an exhaust gas of a furnace during melting ferrous starting materials in an arc furnace.    ADVANTAGE - The method is capable of effectively and economically reducing the emission of nitrogen oxides in the exhaust gas of the furnace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an arc furnace for thermal treatment of materials.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a furnace for thermal treatment of materials.    Furnace vessel (2)    Exhaust pipe (12)    Analysis device (20)    Supply pipe (28)    Exhaust gas. (OG)
NOVELTY - Manufacture of episulfide compound involves reacting epoxy compound (B) with thia-forming agent (C) in presence of polyhydoxyl compound (A) having 2 or more hydroxyl groups.    USE - The method is useful for manufacturing episulfide compound which is used in herbicide, insecticide for controlling harmful insect and pests e.g. fly and mosquito, and medical agent for preventing and/or treating diseases e.g. inflammation, allergic disease, inflammatory bowel disease, arteriosclerosis, thrombosis, respiratory disease, dermatological disorders, autoimmune disease, endocrine system disease, diabetes, cancer and infectious disease. Uses include but are not limited to plastic raw material, adhesive agent, shower gel, switch gear, motor vehicle, fabric softening agent, electronic display board, mobile telephone, electric torch, etc.    ADVANTAGE - The method economically provides episulfide compound at high yield within a short period of time, by environmentally-friendly process.
NOVELTY - Composting material reaction device comprises an automatic constant temperature curing box connected with a centrifugal crushing and processing box, a liquid outlet and a solid outlet derived from the centrifugal crushing and processing box. The liquid outlet is connected with a sewage processing device. The solid outlet is connected with a microwave processing device.    USE - Used as a composting material reaction device.    ADVANTAGE - The device is clean and environment-friendly, processes the organic material in an integrated manner, shortens the composting reaction time, capable of intensively, largely and rapidly processing the municipal solid waste to solve the serious municipal waste deposition problem, and completely processes wastewater and material without secondary treatment.
NOVELTY - The production equipment comprises a pre-processing tank, a comprehensive reaction tank, a mud press filter, a dryer and a granulator connected in series by a conveyor.    USE - Production equipment of environment-friendly mud biomass fuel.    ADVANTAGE - The production equipment realizes reduction, harmless, stabilization and recycling of mud treatment, thus effectively solving the secondary pollution problem of mud and obtaining the environment-friendly biomass fuel. The fuel can substitute coal and burn in boiler, so the mud processing cost is reduced, and the social problem of energy shortage is solved effectively.
NOVELTY - A catalyst composition comprises carbon oxide(s) conversion catalyst, and dehydration/hydrogenation catalyst including silicoalumino phosphate (SAPO) molecular sieve and metal (M).    USE - Catalyst composition is used for converting from carbon oxide(s) to saturated hydrocarbon (claimed) e.g. liquefied petroleum gas, and production of liquid fuel e.g. gasoline.    ADVANTAGE - The catalyst in the composition has improved selectivity, catalytic activity and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst composition;    (2) process for generation of saturated hydrocarbon from carbon oxide(s) and hydrogen; and    (3) apparatus.
NOVELTY - A solid biomass material and fluid hydrocarbon feed are contacted with catalytic cracking catalyst at more than 400 degrees C in catalytic cracking reactor, to obtain cracked products. The obtained cracked product is fractionated, to obtain product fractions. The obtained product fractions are hydrodeoxygenated to obtain hydrodeoxygenated products.    USE - Process of converting solid biomass material to hydrodeoxygenated products used for biochemical and/or biofuel (claimed) for automobile engine.    ADVANTAGE - The process of converting solid biomass material to hydrodeoxygenated products is efficiently enabled.
NOVELTY - Converting a solid biomass material comprises contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400 degrees C in a riser reactor to produce one or more cracked products, where the riser reactor is an internal riser reactor.    USE - The processes are useful for converting solid biomass material; preparing biofuel component and/or biochemical component; and for producing biofuel and/or biochemical (all claimed).    ADVANTAGE - The process provides improvements to meet nowadays conversion, robustness maintenance and/or safety requirements.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a process for preparing a biofuel component and/or biochemical component comprising the process above; and    (2) a process for producing a biofuel and/or biochemical comprising blending a biofuel and/or biochemical component obtained in the process above with one or more other components to produce the biofuel and/or biochemical.
NOVELTY - A methane gas recycling device comprises sewage treatment pool, reusing device, dirt inlet set on lower part of sewage pool, and drain port. The sewage pool is provided with a sealing cover. An air outlet pipe is connected with the sealing top. The sealing cover is provided with a seal valve.    USE - Device for recycling methane gas.    ADVANTAGE - The device has simple structure and low cost, and can effectively prevent the methane gas generated in the process caused by air pollution.
NOVELTY - Use of Chinese barberry root in purifying livestock and poultry breeding biogas slurry, is claimed. The Chinese barberry root is planted in livestock and poultry breeding biogas slurry polluted environment.    USE - The Chinese barberry root is useful in purifying livestock and poultry breeding biogas slurry, and treating damp-heat dysentery, diarrhea, jaundice, eczema, ulcer, aphtha, red eyes and throat pain.    ADVANTAGE - The Chinese barberry root ensures high absorption effect on the pollutants containing ammonium ion and nitrogen, total nitrogen, total phosphorus and chromium chemical oxygen demand, has strong vitality, can be directly planted and grown for multiple years, does not need specific management and perennial characteristics, prevents the pollution problem of the livestock and poultry breeding biogas slurry, ensures simple operation with less investment and low operation cost, and guarantees purifying effect of an artificial wetland in winter.
NOVELTY - Producing microorganism organic fertilizer using poultry feather, comprises inoculating microorganism fermentation liquor containing the bacteria onto puffing feather, rapeseed meal compost and pig manure compost, processing solid fermentation, turning for one time every day in the fermentation process, fermenting for 5 days, where the content of microorganism is more than 1x 108/g after fermentation and obtaining microorganism solid bacteria, using the microorganism solid bacteria to evaporate the moisture of the microorganism organic fertilizer to less than 30%, and packing.    USE - The method is useful for producing microorganism organic fertilizer, which is useful for improving microorganism functions and promoting growth.    DETAILED DESCRIPTION - Producing microorganism organic fertilizer using poultry feather, comprises inoculating microorganism fermentation liquor containing the bacteria amount of more than 1x 108/g onto 5-15% of puffing feather, 0-10% of rapeseed meal compost and 85-95% of pig manure compost according to an amount of 50 l/t, processing solid fermentation, turning for one time every day in the fermentation process, where the temperature is less than 50 degrees C, fermenting for 5 days, where the content of microorganism is more than 1x 108/g after fermentation and obtaining microorganism solid bacteria, using the microorganism solid bacteria to evaporate the moisture of the microorganism organic fertilizer to less than 30% at less than 60 degrees C, and packing to obtain the microorganism organic fertilizer. An INDEPENDENT CLAIM is included for a microorganism organic fertilizer product produced by the above method.
NOVELTY - Reacting an iso-pentane comprises: (a) partially converting an olefinic feedstock (1) comprising at least 15 wt.% of iso-pentene to make a converted olefinic feedstock, where the iso-pentene is reduced and 2-pentene is retained; and (b) alkylating the iso-pentane with the converted olefinic feedstock to make naphtha and middle distillate.    USE - The process of reacting iso-pentane with olefinic feedstock is useful for making naphtha and middle distillate (claimed).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for reacting iso-pentane.    Olefinic feedstock (1)    Iso-alkane (2)    Effluent (3)    Alkylate products (5)    Reactor. (10)
NOVELTY - The furnace has main portion that is equipped with furnace liner and water tank. A water channel from water tank is connected with gas outlet pipe, and furnace cover is covered on water tank. The gas outlet pipe is connected with gas input pipe that is connected with purifying barrel, and gas outlet pipe is composed of purifying barrel connected to tar bottle whose outlet is connected with purifying cylinder. A lower end of main portion is provided with furnace dust hole that is covered with furnace ash cover.    USE - Cyclone straw gasification furnace.    ADVANTAGE - The furnace can provide easy combustion of gas, and continuous supply time of fuel can be reduced. The smoke, odour smell, and release of coke tar from the furnace can be avoided.
NOVELTY - The furnace has main portion that is connected with grate, and provided with flow equalizing device and storage device. The main portion is divided into upper portion of reaction chamber and lower portion of catalytic cracking chamber. The catalytic cracking chamber is connected with reaction chamber, and main portion is provided with air inlet and gas outlet. A bottom of main portion is provided with carbon outlet that is connected with catalytic cracking chamber.    USE - Multi-joint biomass gasification furnace.    ADVANTAGE - The furnace having simple structure can be used in safe, convenient, and reliable manner.
NOVELTY - The tower has a heating pipe whose lower end is connected with an inlet collecting box opening for cooling water. The upper end of the heating pipe is connected with an outlet header for leading cooling water. An upper part tube wall of a water cooling portion is provided with a joint opening. The lower portion of the water cooling portion is provided with an outlet joint for processing the synthesis gas. The conical bottom portion of the water cooling portion is provided with a slag discharging opening.    USE - Water quench tower for cooling biomass synthesis gas.    ADVANTAGE - Since the quench tower is featured with a simple structure, the weight of the tower is reduced so that it can be conveniently installed and maintained.
NOVELTY - Machine comprises machine frame, rolling unit, rail groove and oil container, where front and back portion of the machine frame are provided with hole, and are set with a perforated ear plate, right end of the front and upper longitudinal beams are hinged by pin shaft, right end of the front and back vertical beam is hinged on the machine frame, front and back track seat are respectively provided with drilled plate.    USE - The machine is useful for turning compost (claimed).    ADVANTAGE - The machine is simple and cost-effective.
NOVELTY - A strain compound comprises Bacillus natto powder, lactic acid bacteria powder and Acidithiobacillus powder in a mass ratio of 1:0-50:0-30; and lactic acid bacteria powder and Acidithiobacillus powder are not zero at the same time.    USE - The strain compound is useful for processing industrial sludge (claimed).    ADVANTAGE - The invention is featured in simple operation management, low running cost and safety and reliability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for processing industrial sludge by using strain compound comprising inoculating the strain compound into the industrial sludge in a mass ratio of 1:10-100000; and culturing for more than 12 hours.
NOVELTY - Preparation of N-alkyl-N-trialkylsilylamide, comprises reacting an N-alkyl amide with a triakylsilylhalide in the presence of an organic base (OB) to form the N-alkyl-N-trialkylsilylamide and the salt of the protonated organic base (OB)H+X-, and separating the N-alkyl-N-trialkylsilylamide from the salt of the protonated organic base (OB)H+X-.    USE - The processes are useful for preparing N-alkyl-N-trialkylsilylamide; and for manufacturing a peptide or peptide analog (all claimed).    ADVANTAGE - The processes are cost-effective and environment friendly.    DETAILED DESCRIPTION - Preparation of N-alkyl-N-trialkylsilylamide of formula (I), comprises reacting an N-alkyl amide of formula (II) with a triakylsilylhalide of formula (III), in the presence of an organic base (OB) to form the compound of formula (I) and the salt of the protonated organic base (OB)H+X-, and separating the compound of formula (I) from the salt of the protonated organic base (OB)H+X-, where the process is carried out in a reaction medium which consists essentially (at least 90%) of the compound of formula (II), the compound of formula III, the organic base (OB) and the reaction products formed during the reaction and where 0.8 to 4 moles of the organic base (OB) are used per mole of the compound of formula (II).    R1, R2, R3, R4 and R5=independently of each other represent 1-6C alkyl; and    X=a halogen.    An INDEPENDENT CLAIM is a process for the manufacture of a peptide or peptide analog, comprising preparing the N-alkyl-N-trialkylsilylamide of formula (I), reacting the N-alkyl-N-trialkylsilylamide of formula (I) with an amino acid, a peptide or a peptide analog to obtain a persilylated amino acid, peptide or peptide analog reacting the persilylated amino acid, peptide or peptide analog with a compound of formula (IV): Y-A-COOH.    Y=an amino protecting group;    A=an amino acid, peptide or peptide analog residue; and    COOH=an optionally activated carboxylic group.
NOVELTY - A three-dimensional planting of Pleurotus geesteranus at the banana tree bottom by taking banana stalks and leaves as main material, involves using the banana stalks and leaves as main material which are abundant resources to prepare Pleurotus geesteranus bacteria bag; proper arranging the production time; and receiving fresh mushroom in three-dimensional planting the banana tree.    USE - For planting of Pleurotus geesteranus at the banana tree bottom by taking banana stalks and leaves as main material (claimed).    ADVANTAGE - The method avoids weed and banana contention fertilizer, which causes disease, effectively improve the soil to reach comprehensive recycling, and avoids environmental pollution.
NOVELTY - Preparing solid organic fertilizer, comprises (a) intercepting off dregs of large particles of wet sludge with a grid network and then introducing into a collection pool, (b) pre-processing and adding the heavy metal extracting agent into the collected sludge, and performing microwave oscillation, (c) putting the pre-processed sludge into drying system to dry, (d) crushing dried the sludge, transferring the dried sludge into pulverizer to crush, (e) adding organic microbial and active microbial to ferment, (f) stoving the fermented fertilizer, and (g) packaging, warehousing and preserving.    USE - The method is useful for preparing solid organic fertilizer, which is useful for crops such as soybean, wheat and corn.    ADVANTAGE - The method is capable of simply preparing the solid organic fertilizer high stimulation effect in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing solid organic fertilizer, comprises (a) intercepting off the dregs of large particles of wet sludge with a grid network and then introducing into a collection pool to collect sludge, (b) pre-processing and adding the heavy metal extracting agent into the collected sludge, uniformly stirring and then performing microwave oscillation for 1-5 hours, (c) putting the pre-processed sludge into drying system with a conveyor, drying the sludge to the water content of less than 10% in the drying system, (d) crushing dried the sludge to produce caking, transferring the dried sludge into pulverizer to crush, (e) adding an organic microbial into the crushed sludge and then uniformly mixing, adding active microbial to ferment for 5-10 days and then turning at every day for one time, (f) stoving the fermented organic fertilizer to 7-9 into dry, and (g) after stoving, packaging the organic fertilizer, warehousing and preserving the fertilizer.
NOVELTY - A garbage percolate is processed by starting of microbial fuel cell having an active sludge and controlled at 30 plus minus 1 degrees C and current at 1000 A, anode power generating, subjecting to hot pressing with cation exchange membrane and carbon cloth, adding domesticated microbial fuel battery and active sludge, reacting with microorganism, and monitoring output voltage and concentration of water outlet organic substance.    USE - Method of processing a garbage percolate.    ADVANTAGE - The method is efficient and simple, has high processing efficiency, and is stable.
NOVELTY - Air dried biomass raw material is carbonized in oxygen free atmosphere, and cooled to obtain biomass coke. The biomass coke is crushed and sieved until granularity is less than 150 mu m. A binder is added to the mixture and the mixture is pressed into carbon-containing pellets. The biomass coke powder is paved on refractory material to a thickness of 5-10 mm at the bottom of the rotary hearth furnace. A single layer material is provided, and the obtained pellets are reduced to obtain metalized pellets.    USE - Manufacture of carbon-containing pellets.    ADVANTAGE - The carbon-containing pellets with reduced impurity content and high quality is manufactured with improved productivity and reduced environmental pollution.    DETAILED DESCRIPTION - Air dried biomass raw material is carbonized in oxygen free atmosphere at 400-900 degrees C for 30-90 minutes, and cooled to obtain biomass coke. The biomass coke content is more than 70%, the volatile material content is less than 20%, and remaining is water and ash. The biomass coke is crushed and sieved until granularity is less than 150 mu m. The ratio of sieved biomass coke and mineral powder is 1.1-1.4. A binder is added in the mass ratio of 2-4% with respect to the total mass of the mixture. The mixture is pressed into carbon-containing pellets. The biomass coke powder is paved on refractory material to a thickness of 5-10 mm at the bottom of the rotary hearth furnace. A single layer material is provided, and the obtained pellets are reduced at 125-1450 degrees C for 10-40 minutes to obtain metalized pellets.
NOVELTY - Water purifying agent comprises cobalt doped nano titanium dioxide catalyst, and chitosan as carrier. The nano titanium dioxide is doped with cobalt to ensure the catalyzing effect, and is embedded chitosan by using polyvinyl alcohol and sodium alginate to form cobalt doped nano titanium dioxide/chitosan composite microsphere.    USE - The water purifying agent is useful for purifying organic phosphorus pesticide wastewater.    ADVANTAGE - The water purifying agent reduces organic phosphorus in water, and achieves organic phosphorus removal rate of 75%.
NOVELTY - Honeycomb microbial carrier comprises (in wt.%) sludge (30-60), a carbonaceous material (20-40), an adhesive (2-20) and an additive (1-10).    USE - Used as a honeycomb microbial carrier.    ADVANTAGE - The carrier: solves the environmental hazards and pollution caused by the sludge and thus realizes the utilization of sludge and decrease of microbial carrier cast; is economical, converts waste into usable material, has high mechanical strength, long service life and increases the growth of microorganism environment, and thus it is an economical, high-efficient, durable, novel and stabilized carrier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the honeycomb microbial carrier comprising: (i) drying and grinding the sludge and carbonaceous material and passing through the 100 mesh sieve; (ii) mixing the sludge, carbonaceous material, adhesive and additive (the total mass percentage of the four materials is 100%); (iii) fully stirring the obtained mixture in step (ii) and mediating, molding the mediated plastic pug by the honeycomb steel mold on extruder with the pressure of 10-15 MPa to prepare the cylinder with smooth surface and whole honeycomb pore canal structure or the strip-type honeycomb body, then drying for 20-24 hours at 110-130 degrees C; (iv) carbonizing the obtained drying honeycomb body under the anaerobic or oxygen deficient condition to obtain the carbonized honeycomb body in which the carbonization temperature is 300-400 degrees C, and the time is 1-3 hours; (v) activating the obtained carbonization honeycomb body with water vapor or carbon dioxide, in which activation temperature is 700-1000 degrees C, and the time is 2-4 hours.
NOVELTY - An antioxidant comprises alkanolamide and molybdenum source dissolved in an organic phase in a homogeneous phase. It comprises 0.1-8 mass % molybdenum.    USE - An antioxidant used for biodiesel oil and ester synthetic oil.    ADVANTAGE - The antioxidant is environment-friendly, and improves oxidization starting temperature of the biodiesel oil and ester synthetic lubricating oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the antioxidant, comprising:    (A) dissolving a molybdenum source in water or sulfuric acid to obtain an aqueous phase of molybdenum source;    (B) regulating pH value of organic phase through sulfuric acid, and washing the organic phase with distilled water twice;    (C) mixing the organic phase with the solvent to obtain an extraction agent;    (D) mixing the extraction agent with the water phase for 20 minutes, standing the mixture in a separating funnel and delaminating, and separating an upper layer to obtain the molybdenum source dissolved in the organic phase; and    (E) dehydrating and reacting the alkanolamide and molybdenum source dissolved in the organic phase in vacuum at 100-200 degrees C for 0.5-6 hours.
NOVELTY - The device has a pressure container that is divided to two separation chambers by a baffle for separating hydrogen and oxygen. The two chambers are hydrogen separation chamber and oxygen separation chamber. The holes are connected with two separation chambers arranged on the baffle and below the liquid level of electrolytic liquid.    USE - Integrated water electrolysis hydrogen/oxygen separation and cooling de-alkalization device of hydrogen production system.    ADVANTAGE - The integrated water electrolysis hydrogen/oxygen separation and cooling de-alkalization device with simple structure can be provided. The occupied space of the hydrogen production system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated water electrolysis hydrogen/oxygen separation and cooling de-alkalization device of hydrogen production system.
NOVELTY - The system is provided with a container and main portion. The main portion is arranged in the container. The cooling devices are arranged on the upper portions of the separating chambers. The gas outlets are formed on the hydrogen and oxygen separating chambers at top portion of pressure container and cooling device.    USE - Hydrogen production system used in chemical machinery.    ADVANTAGE - The space occupied by the hydrogen production system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production system used in chemical machinery.
NOVELTY - An integrated hydrogen production system comprises a reforming reactor provided with a reforming catalyst, a gas inlet and a material outlet; a shift reactor unit provided with a shift catalyst; a carbon monoxide purification reactor unit provided with a carbon monoxide purifying catalyst and having a material outlet connected with a fuel cell; and a catalytic combustion evaporator provided with a catalyst for catalytic combustion and a material outlet.    USE - An integrated hydrogen production system for use as an on-site hydrogen generator for a 1-200kW grade fuel battery.    DETAILED DESCRIPTION - An integrated hydrogen production system comprises:    (1) a reforming reactor provided with a reforming catalyst, a gas inlet and a material outlet;    (2) a shift reactor unit provided with a shift catalyst;    (3) a carbon monoxide purification reactor unit provided with a carbon monoxide purifying catalyst and having a material outlet connected with a fuel cell;    (4) a catalytic combustion evaporator provided with a catalyst for catalytic combustion and a material outlet;    (5) five heat exchangers;    (6) material flow distributor;    (7) a mixer;    (8) two raw material storage tanks; and    (9) two air compressors.    The storage tanks and air compressors are connected with a raw material inlet and a gas inlet of the catalytic combustion evaporator, respectively.
NOVELTY - The method comprises supplying waste water in a first tank, subsequently pumping purified waste water in a second tank, increasing the degree and speed of purification in the first tank by an active aeration of the waste water with the ratio (0.2-0.3) of diameter to the height of filled portion of the first tank by water based on the specific flow rate of air for achieving effect of boiling layer, conditionally mixing pure water of large volume (ponds, bath and showers) in the second tank, and mixing the purified waste water from the first tank, which carry a small content of dissolved air.    USE - The method is useful for the purification of waste water via activated sludge in the suspended state.    DETAILED DESCRIPTION - The method comprises supplying waste water in a first tank, subsequently pumping purified waste water in a second tank, increasing the degree and speed of purification in the first tank by an active aeration of the waste water with the ratio (0.2-0.3) of diameter to the height of filled portion of the first tank by water based on the specific flow rate of air for achieving effect of boiling layer, conditionally mixing pure water of large volume (ponds, bath and showers) in the second tank, and mixing the purified waste water from the first tank, which carries a small content of dissolved air and the suspended matter of sludge for the purification of water of ponds, baths and showers. An INDEPENDENT CLAIM is included for an activation purification device for waste water via biological way with the activated sludge in suspended state.
NOVELTY - System comprises (a) first cultivation processing housing unit for cultivating larvae hatched from eggs, (b) second cultivation processing housing unit, (c) drop portion that allows the larvae to fall by utilizing the fact that the larvae crawl, (d) organic fertilizer base, (e) organic fertilizer base gathering unit for gathering the produced organic fertilizer base material, and (f) larvae gathering unit for gathering the larvae group that crawled and fell from the final section of the cultivation processing housing unit.    USE - The system is useful for producing organic fertilizer, which is useful for treating livestock manure using M.domestica larvae.    ADVANTAGE - The system is simple and requires less manual labor for operation.    DETAILED DESCRIPTION - System comprises (a) first cultivation processing housing unit for cultivating larvae hatched from eggs, (b) second cultivation processing housing unit that is divided into several sections below the first cultivation processing housing unit, (c) drop portion that allows the larvae to fall by utilizing the fact that the larvae crawl, (d) organic fertilizer base prepared by letting the larvae fall from the drop portion into the next stage of the second cultivation processing housing unit and repeating the process several times, where in each of the cultivation processing housing units, the excreta is enzymatically hydrolyzed within the larvae during the process of rearing the larvae and is subsequently excreted by the larvae, (e) organic fertilizer base gathering unit for gathering the produced organic fertilizer base material and discharges the produced organic fertilizer base material, and (f) larvae gathering unit for gathering the larvae group that crawled and fell from the final section of the cultivation processing housing unit, where the organic fertilizer base and larvae group are discharged.
NOVELTY - The system (10) has a pressure drop device (24) that is provided in coolant channels (20) and configured to provide a sub-atmospheric pressure within a coolant passage. A compression device (26) is fluidly interconnected to downstream from internal coolant passage by a coolant steam loop configured to convey a sub-atmospheric pressure coolant steam. The compression device is configured to increase the pressure and a temperature of the sub-atmospheric coolant steam to a super-atmospheric pressure and maintain the coolant steam within a steam region of a pressure-enthalpy curve.    USE - Fuel cell system for generating steam within fuel cell stack.    ADVANTAGE - The compression device can be a scroll compressor which can be driven by an electric motor to sufficiently increase the overall fuel cell efficiency, and can reduce the losses associated with the compression device. The steam can be generated at sub-atmospheric pressures within the fuel cell stack, so that the sub-atmospheric pressure coolant steam can be quasi-isentropically compressed by the compression device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing steam within fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system with steam generation internal to fuel cell stack.    Fuel cell system (10)    Fuel cell stack (12)    Pressure drop device (24)    Compression device (26)    Reformate line (40)
NOVELTY - Converter gas is purified and mixed with coke oven gas, and utilizing the reaction of obtained mixed gas to produce methanol.    USE - Production of methanol.    ADVANTAGE - The method increases the use ratio of useful elements in the raw material, enhances production efficiency, reduces pollution from waste gas to the environment, decreases production cost, and increases economic benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methanol-production device.
NOVELTY - The cracker (800) has a conduit having an air entering inlet (801) for receiving a premixed, ammonia-rich gaseous mixture containing ammonia and oxygen. A portion of heat is transferred from an outgoing mixture of products, to the incoming mixture containing ammonia and oxygen. The incoming mixture is provided with ammonia and oxygen which are heated to attain a maximum gas temperature higher than 1400 degrees c. An outlet is provided for expelling mixture of products, resulting from the reactions, from the conduit, including non-combusted hydrogen gas.    USE - Heat exchanged ammonia flameo?=cracker.    ADVANTAGE - The structure is simple and convenient to use. The sensitivity of the cracker can be increased. The cost involved in the manufacture of the device can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for cracking ammonia and combusting fuel in separate conduits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of heat exchanged ammonia flame cracker.    Ammonia flame cracker (800)    Air entering inlet (801)    Tubings (802,805)    Igniter (808)    Vacuum space (818)
NOVELTY - Producing ethyl hexanoate involves mixing synthetic medium malt extract with soybean oil, and agro-industrial waste as substrate e.g. cassava residue for the production of the ester by using Neurospora sitophila FGSC 1135 strain.    USE - Method for producing ethyl hexanoate used for obtaining natural aroma containing products, food products and scents (all claimed).
NOVELTY - Growing phototrophic biomass (202) in a reaction zone (10) involves: treating an operative carbon dioxide supply comprising gaseous material feed (24) to produce a carbon dioxide-rich product material (26) having a carbon dioxide concentration greater than that of the operative carbon dioxide supply-comprising gaseous material feed, where production of at least a fraction of the gaseous material feed is effected by gaseous exhaust material (14) producing process; and supplying at least a fraction of the material to reaction zone to effect growth of the biomass by photosynthesis.    USE - For growing a phototrophic biomass in a reaction zone (claimed), particularly for growing microalgae or photosynthetic bacteria, in a bioreactor, for use as fuel source.    ADVANTAGE - By using exhaust gases, the process reduces environmental impact, and in parallel produces a potentially useful fuel source. The process is economically attractive and can be incorporated within the existing facilities. During modulating the volume of the reaction mixture disposed within the reaction zone is maintained constant for a period of time such that the predetermined phototrophic biomass growth indicator value, as well as the predetermined molar rate of growth of phototrophic biomass, is maintained constant during this period, with a view to optimizing economic efficiency of the process.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the process for growing a phototrophic biomass in a reaction zone.    Reaction zone (10)    Photobioreactor (12)    Gaseous exhaust material (14)    Operative carbon dioxide supply-comprising gaseous material feed (24)    Carbon dioxide-rich product material (26)    Phototrophic biomass (202)
NOVELTY - The method involves forming a graphite layer on the surface of a metallic substrate, crimping the formed graphite layer, and heat-processing the substrate. The graphite powder used to form the graphite layer has, as main constituent, flaky-graphite powder, expanded graphite powder or thermal decomposition graphite powder.    USE - Manufacturing method of separator of fuel cell used in various applications. Uses include but are not limited to a fuel cell electric vehicle, a home-use cogeneration system, or a portable apparatus, such as a mobile telephone or a personal computer.    ADVANTAGE - Raises rate with which graphite layer covers base-material top and improves adhesiveness of metallic substrate and graphite layer by using appropriate graphite powder in forming graphite layer, thus fuel cell separator excellent in workability can be manufactured with sufficient productivity while high electroconductivity can be maintained for long period of time.
NOVELTY - The electric power as main product is generated by using electrolytic process of decomposing water to hydrogen and oxygen in a spiral magnetic electrolyzer (1) under surface of water environment (3). The dynamization of water environment in water supply system at inlet (2) of electrolyzer is induced by negative pressure resulting from water being decomposed at outlet (4) of electrolyzer. The decomposition process is followed by separation of hydrogen and oxygen in a gas separator (5). The energy output of hydrogen fuel cell (6) which is in whole or in portion is used to power electrolyzer.    USE - Combined magnetohydrodynamic and electrochemical method for electric power generation in energy and water management industries.    ADVANTAGE - The energy required for electrolysis can be reduced. The amount of hydrogen entering the fuel cell or a system can be reduced while controlling the output power and stability of the system. Since minimum number of mechanical components is used, the combined magnetohydrodynamic and electrochemical system can be installed without the need for costly and time consuming work to any water environment. The progressive, safe, environmentally friendly and economical solution can be achieved for sea water processing. The water can be conveyed to higher and/or remote areas without the need to use pumping technologies or water pumping and/or transportation units.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combined magnetohydrodynamic and electrochemical facility for electric power generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined magnetohydrodynamic and electrochemical facility for electric power generation.    Spiral magnetic electrolyzer (1)    Inlet (2)    Water environment (3)    Outlet (4)    Gas separator (5)    Hydrogen fuel cell (6)
NOVELTY - The catalytic converter has cell plates (12) that consists of top cell plate (A), middle cell plate (B), and bottom cell plate (C) each with holes that are varied in sizes and positioned on rings. The permanent magnets (11) are completely covered with stainless steel case and attached to interior wall of hydrogen separation chamber. The permanent magnets create electromagnetic energy while DC power supply supplies the current to electrolyte solution.    USE - Catalytic converter for hydrogen powered engine.    ADVANTAGE - Allows catalyzing the hydrogen separation process and balancing the process when power from DC power supply is changed since hydrogen gas produced is led into the engine combustion chamber through hydrogen pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the cell plate connections.    Permanent magnets (11)    Cell plates (12)    Top cell plate (A)    Middle cell plate (B)    Bottom cell plate (C)
NOVELTY - The method involves thermally heating and dissociating magnesium hydride by a solar heater in a hydrogen generator using non-imaging concentrator, which produces hot fluid up to required high temperatures to release hydrogen with or without a catalyzer, where thermal requirements e.g. electricity load and fuel cell conversion rate, are scaled up or down depending on demand. The released hydrogen is stored in a hydrogen collector e.g. dry solid, to power various energy needs of navy and homes.    USE - Method for producing hydrogen used to power energy needs of houses, ships of moderate sizes for naval or cruise, and ocean liners (all claimed). Can also be used for automobile.    ADVANTAGE - The method allows providing thermal and hydrogen storage capability for overall energy storage of 20-30 percent, thus providing smooth energy needs of a building. The method allows exhibits high gravimetric capability of 7.6 weight percentages and volumetric storage capability of 130 kg Hhydrogen per cubic meter, low cost hydrogen production, endothermic desorption reaction, surface oxidation and pyrophoricity, sluggish hydrogen diffusion kinetics, metal-hydride volume mismatch, large nucleation energy barrier, high temperature and pressure for activation, large enthalpy of hydride formation, low-toxicity of a non-explosive and inert storage medium. The method allows dissociating the hydrides at low temperatures for transportation use in automobiles.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a hydrogen generator    (2) a solar power producing system    (3) a heater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a solar power producing system.
NOVELTY - A transcription factor comprising amino acid sequence chosen from (a) a 727 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, and (b) amino acid sequence of SEQ ID NO: 1 in which one or more amino acids are deleted, substituted or added, is new.    USE - The transcription factor is useful for controlling transcription of cellulase and hemicellulase gene in filamentous fungi, preferably A.aculeatus for producing cellulase and/or xylanase used for saccharifying plant-derived biomass (all claimed), preferably cellulose biomass e.g. rice straw for producing biofuels e.g. bioethanol. The biomass includes refuse, grass, timber, agricultural waste, paper, and food waste material.    ADVANTAGE - The method performs saccharification on mild conditions, is environmentally-friendly and does not excessively decompose monosaccharides. The gene enhances the production of cellulase and hemicellulase.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene hybridized under stringent conditions with the gene encoding the above-mentioned transcription factor, or its complementary strand;    (2) vector comprising the above-mentioned gene integrated artificially;    (3) transformant comprising the above-mentioned vector;    (4) method for producing cellulase and/or xylanase involves culturing the above-mentioned transformant;    (5) method for saccharifying plant-derived biomass involves performing saccaharification in the presence of culture solution containing the above-mentioned transformant; and    (6) method for making the transcription factor, and raising the production amount of cellulase and/or xylanase in filamentous fungi.
NOVELTY - The apparatus (1) has a fuel cell producing electric power according to electrochemical reaction of fuel gas and oxidizing agent gas, and an exhaust port (17) formed in an upper-surface part (14) of a main body (13). An air supplying opening (18) connects a housing and the main body, and is formed in a side part of the main body. A water draining hole (19) is formed in a lower-surface part (15) of the main body. A hydrogen generating apparatus is equipped with a combustor. An air supply device supplies air to the combustor.    USE - Exhaust apparatus for a fuel cell apparatus (claimed) e.g. polymer electrolyte fuel cell and solid oxide fuel cell, of a home-use fuel battery cogeneration system.    ADVANTAGE - The water draining hole is formed in the lower-surface part of the main body, thus preventing external deterioration of the housing, and ensuring discharge of waste gas from the exhaust port even if large amount of rain water flows into the exhaust apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an exhaust apparatus.    Exhaust apparatus (1)    Main body (13)    Upper-surface part (14)    Lower-surface part (15)    Exhaust port (17)    Air supplying opening (18)    Water draining hole (19)
NOVELTY - Producing a hydrocarbon or a mixture of hydrocarbons, comprises: subjecting a feed of biological material into a reactor, which comprises at least two catalyst layers, comprising hydrodeoxygenation (HDO) and hydrodewaxing (HDW) catalysts, where the proportion of the HDW catalyst grows towards the bottom of the reactor; treating the feed material in the reactor to produce at least one hydrocarbon; and recovering the hydrocarbon or the mixture of hydrocarbons.    USE - The hydrocarbon is useful as a fuel or an additive in fuel compositions (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:An apparatus for producing at least one hydrocarbon, comprising at least one reactor (1) comprising at least two catalyst layers (3, 3 approximately ) and comprising HDO and HDW catalysts, a feed material inlet conduit (4) for introducing the feed material to the reactor, a hydrogen inlet conduit (5) for introducing hydrogen to the reactor, and a product outlet pipe (10) for recovering the hydrocarbon from the reactor; #a reactor comprising at least two catalyst containing layers and comprising HDS and HDW catalysts; and #fuel meeting specification EN 590 diesel comprising at least one hydrocarbon fraction produced by the process.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an apparatus for producing at least one hydrocarbon comprising one reactor, where the catalyst system is packed in two separate layers in the reactor.    Reactor (1)    Two catalyst layers (3, 3~)    Feed material inlet conduit (4)    Hydrogen inlet conduit (5)    Product outlet pipe. (10)
NOVELTY - The desulfurizer has a container (1) which is filled with desulfurizing agent forming desulfurizing agent layer (2). A heater (3) is positioned at center portion of desulfurizing agent layer. A fuel inlet (7) is provided in order to introduce fuel into bottom portion of container. A fuel outlet (8) is formed in order to take out fuel de-sulfurized from upper portion of container. The position of the fuel inlet is varied in horizontal surface in container.    USE - Desulfurizer used for hydrogen production apparatus in fuel cell system.    ADVANTAGE - The drift of the fuel within container of desulfurizer can be prevented effectively. The region of the desulfurizing agent layer can be used effectively. The service life of the desulfurizer can be prolonged. The desulfurization performance of the desulfurizer can be improved effectively.    DETAILED DESCRIPTION - Several partition walls (4) are radially positioned from heater, in order to partition off desulfurizing agent layer into fuel channels (5). The partition wall is thermally contact with heater and serves as heat-conducting fin, in order to transmit heat of heater to outer side of desulfurizing agent layer along radial direction.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross sectional view of the desulfurizer.    Container (1)    Desulfurizing agent layer (2)    Heater (3)    Partition wall (4)    Fuel channel (5)    Fuel inlet (7)    Fuel outlet (8)
NOVELTY - The system has the feedback pipe (20) injects the supernatant of digested sludge stabilization bath to the hydrogen fermenter (14). The denitrification tank (17) denitrogenizes nitrate nitrogen returned to aeration tank and removes nitrogen. The portion of the denitrified supernatant is transferred to digested sludge stabilization bath through feedback pipe and mixed in denitrification tank for controlling alkalinity. The food category slurry is transferred from digested sludge stabilization bath to hydrogen fermenter for controlling pH of hydrogen fermenter.    USE - System for recovering hydrogen and methane in food waste.    ADVANTAGE - The alkalinity of the methane fermentation liquid lowering the hydrogen partial pressure is controlled so that the production of the hydrogen gas is improved and the pH of the hydrogen fermenter is maintained between 5.5 through 6.0. The activation of the methane fermentation microorganism and hydrogen fermentation organisms is suppressed. The drug input cost and the running cost are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for recovering hydrogen and methane. (Drawing includes non-English language text)    Slurry type material storage tank (12)    Hydrogen fermenter (14)    Digester (15)    Denitrification tank (17)    Feedback pipe (20)
NOVELTY - Method for preparing biogas comprising hydrogen and/or methane involves preparing moon jellyfish substrate, injecting reaction solution containing anaerobic microorganisms or anaerobic microorganisms into substrate, and culturing the substrate at pH of 4-9 and temperature of 20-50 degrees C.    USE - The method is useful for preparing biogas comprising hydrogen and/or methane from moon jellyfish.    ADVANTAGE - The method is environmentally-friendly and cost-effective, as moon jellyfish disposed as waste is utilized.
NOVELTY - Method for preparing biofertilizer from garbage, involves mixing crushed garbage, grass peat, rice hull powder, weathered coal powder, rice bran and composite microbial inoculum uniformly, composting mixture under tubular heating hole ventilating mode in a fermentation tank to obtain biofertilizer, where the compost stack height is 5 m, width is 4 m and plastic tube diameter is 1.5.    USE - The method is useful for preparing biofertilizer from garbage (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - A new method for the preparation of active pharmaceutical drug valsartan and its intermediates, is disclosed. In the first step, 4-halomethyl-2-cyanobiphenyl is synthesized from 2-aminobenzonitrile, alkylnitrite and benzyl halides. This was then utilized for N-alkylation of (S)-valine methyl ester. N-acylation of this compound with pentanoic acid in presence of a catalyst followed by tetrazole formation and finally alkaline hydrolysis afforded valsartan in a substantially pure enantiomeric form. The process is efficiently, economically and environmentally-friendly carried out. Image 0/0
NOVELTY - Cyano acetate, hydrocarbon as solvent, and dimethylamine are reacted to obtain N,N-dimethylcyanoacetamide.    USE - Manufacture of N,N-dimethylcyanoacetamide used as intermediate for nicosulfuron.    ADVANTAGE - The method efficiently and economically provides N,N-dimethylcyanoacetamide having high yield, by simple method without affecting the environment.
NOVELTY - Methane synthesis device comprises a feed gas inlet, a mid catalyst bed layer and a downstream reaction product outlet. The upstream of the catalyst bed layer is equipped with a first-stage gas distribution system and the downstream of the catalyst bed layer is equipped with a second-stage gas distribution system.    USE - Used as a methane synthesis device.    ADVANTAGE - The device has simple manufacturing method with simple structure; has continuous reaction process; improves the energy performance and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for synthesizing methane using the methane synthesis device.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the methane synthesis device.
NOVELTY - The method comprises dewatering the material oil by scouring and degumming to obtain pure fatty acid, mixing the fatty acid, sodium hydroxide and bioenzyme used as catalytic agent and carbinol, adding the mixture to a reaction kettle to agitate and heat continuously, finishing esterification after the temperature ascends to 80 degrees C and generating fatty acid methyl ester, taking out the reacted matter to filter large particle by a filter to obtain the pure fatty acid methyl ester, and adding the refined fatty acid methyl ester to a part of petro-diesel to obtain the biodiesel.    USE - The method is useful for preparing biodiesel, which is useful for vehicle.    ADVANTAGE - The method is capable of simply, conveniently and economically preparing the clean biodiesel with excellent combustibility and low sulfur content and without corrosivity in an environmentally friendly manner thus reducing abrasion of the machine parts.    DETAILED DESCRIPTION - The method comprises dewatering the material oil by scouring and degumming to obtain pure fatty acid, mixing the fatty acid, sodium hydroxide and bioenzyme used as catalytic agent and carbinol, adding the mixture to a reaction kettle to agitate and heat continuously, finishing esterification after the temperature ascends to 80 degrees C and generating fatty acid methyl ester, taking out the reacted matter to filter large particle by a filter to obtain the pure fatty acid methyl ester, and adding the refined fatty acid methyl ester to a part of petro-diesel to obtain the biodiesel. The material oil of the biodiesel prescription is hogwash oil and illegal cooking oil. The weight percentages of the fatty acid, sodium hydroxide, bio-enzyme, carbinol and petro-diesel are 55:10:5:8:22. The purity of the carbinol in the biodiesel prescription is 98.8%. The bio-enzyme is extracted as soya bean bran and as peanut bran in the biodiesel prescription.
NOVELTY - Methane synthesis device comprises a centrifugal compressor, a sealing device and a synthesis tower. A first outlet of the centrifugal compressor is connected to the synthesis tower. The sealing device is set at two ends of the centrifugal compressor. The sealing device is connected with the synthesis tower through a sealing pipeline. The synthesis device further comprises a gas-liquid separating coalescer parallely set with the sealing pipeline.    USE - Used as a methane synthesis device.    ADVANTAGE - The synthesis device: efficiently separates condensed fluid in the sealing device, and thus solves the problem of the sealing surface being washed away by sealing gas liquid; ensures safe and stable operation of the centrifugal compressor and long-term operation of the complete device; saves energy; and prevents production efficiency loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methane synthesis device (Drawing includes non-English language text).
NOVELTY - Gas cryogenic separation and liquefaction device for methanated coal gas comprises a heat exchanger, a first gas-liquid separator, first nitrogen washing tower and first Joule-Thomson (J-T) valve, where the heat exchanger is provided with multiple liquid channels. The inlet of the first gas-liquid separator is connected with heat exchanger. The upper part of outlet of the first gas-liquid separator is connected with the first nitrogen washing tower and the lower part of outlet is connected with heat exchanger. The lower outlet of first nitrogen washing tower is connected with heat exchanger.    USE - The gas cryogenic separation and liquefaction device is useful for methanated coal gas.    DETAILED DESCRIPTION - Gas cryogenic separation and liquefaction device for methanated coal gas comprises a heat exchanger, a first gas-liquid separator, first nitrogen washing tower and first Joule-Thomson (J-T) valve, where the heat exchanger is provided with multiple liquid channels. The inlet of the first gas-liquid separator is connected with the heat exchanger. The upper part of the outlet of the first gas-liquid separator is connected with the first nitrogen washing tower and the lower part of the outlet is connected with the heat exchanger. The lower outlet of the first nitrogen washing tower is connected with the heat exchanger. The inlet of the first J-T valve is connected with the heat exchanger, and the outlet is connected with the first nitrogen washing tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the gas cryogenic separation and liquefaction device for methanated coal gas (Drawing includes non-English language text).
NOVELTY - Extracting 5,7-dihydroxyflavone glycoside from Nalussieboldji involves adding ethyl alcohol to crushed Nalussieboldji, extracting, decompressing the liquid, filtering, adsorbing by a macroporous resin column, eluting by ethyl alcohol, decompressing and concentrating, adjusting the pH to 8-9, adding water-saturated n-butyl alcohol and extracting, decompressing and concentrating, adding ethyl alcohol to an extract paste, and crystallizing.    USE - Method for extraction of 5,7-dihydroxyflavone glycoside (claimed).    ADVANTAGE - The method has simple process, non toxic agent, and environment-friendly proportion, and is suitable for the industrial production.    DETAILED DESCRIPTION - Extraction of 5,7-dihydroxyflavone glycoside from Nalussieboldji involves crushing Nalussieboldji to 20-40 meshes; adding 5-10 times of 50-70% ethyl alcohol and ultrasonically extracting for 2-3 times; decompressing the extraction liquid and recycling the ethyl alcohol; filtering; adsorbing by a macroporous resin column; washing by water to the sugar color; eluting by 4-6 BV of 40-70% ethyl alcohol; collecting the elution liquid; decompressing and concentrating; adjusting the pH of concentrate liquid to 8-9; adding water-saturated n-butyl alcohol and extracting; remaining the water phase and adjusting the pH to 3-5; adding the water-saturated n-butyl alcohol and extracting; collecting n-butyl alcohol layer; decompressing and concentrating; adding 70-90% ethyl alcohol to an extract paste; flowing back and dissolving; filtering; concentrating to 1/2-1/3 of volume; staying and crystallizing; filtering the crystal; washing by hot water for 2-3 times; flowing back and dissolving the crystal by the ethyl alcohol; and drying the crystal to obtain the product.
NOVELTY - A mixed alkane, comprises propane, isobutane and butane, where, based on the total amount of the mixed alkane, content of propane is more than 89 wt.% to less than or equal to 99 wt.%, the content of isobutene is greater than or equal to 0.5 wt.% to less than 10 wt.%, the content of butane is greater than or equal to 0.5 wt.% to less than 10 wt.%.    USE - The mixed alkane is useful in a refrigerant (claimed).    ADVANTAGE - The mixed alkane has improved refrigerating effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a refrigeration method, comprising making R290, R600 and R600a after sending to the compressor of the refrigeration device in the compression, where, based on the total amount of the like R290, R600a and R600, R290 is more than 89 wt.% to less than or equal to 99 wt.%, the adding amount of R600a is greater than or equal to 0.5 wt.% to less than 10 wt.%, the adding amount of R600 is greater than or equal to 0.5 wt.% to less than 10 wt.%.
NOVELTY - Primary separation of biodiesel product is carried out from glycerol product of transesterification. The biodiesel is stored in one or more storage vessels, and heated at temperature more than boiling point of methanol to obtain methanol vapor. The methanol vapor is removed from top of the vessel via a vacuum system and cooled to temperature less than condensation point of methanol. The condensed methanol at bottom of the vessel is collected, extracted and recycled.    USE - Method for recovery of methanol from biodiesel.    ADVANTAGE - The methanol is recovered from biodiesel without using chemical reagent.    DETAILED DESCRIPTION - Primary separation of biodiesel product is carried out from glycerol product of transesterification. The biodiesel is stored in one or more storage vessels, and heated at temperature more than boiling point of methanol to obtain methanol vapor. The methanol vapor is removed from top of the vessel via a vacuum system and cooled to temperature less than condensation point of methanol. The condensed methanol at bottom of the vessel is collected, extracted and recycled. The storage vessel is made of stainless steel. The transesterification is performed using potassium hydroxide or sodium hydroxide as a base catalyst.
NOVELTY - Method for purifying biogas, involves carrying out hydrogen fermentation of raw material biomass to obtain gas containing hydrogen and carbon dioxide gas as main component, carrying out methane fermentation of biomass which passed through hydrogen fermentation process with methane and carbon dioxide gas as main component, adding the gas, removing carbon dioxide and other impurities from biogas which passed through hydrogen gas addition process, reacting and removing hydrogen in biogas, and performing deoxidation process by removing oxygen as impurity.    USE - The method is useful for purifying biogas (claimed) and sewage sludge, e.g. organic refuse, foodstuff waste material, waste material and wood chips.    ADVANTAGE - The method reduces installation and running cost.
NOVELTY - The system (100) has a fuel cell (5) producing electric power using fuel gas and oxidizing agent gas. A hydrogen generation part (1) produces the fuel gas supplied to the fuel cell. A water collection part (7) collects water contents in the exhaust gas emitted from the hydrogen generation part and the fuel cell. A control part (101) is controlled to stop operation of a supplementary water part (12) when accumulation operating time of the supplementary water part is above a predetermined time. A water-purifying part (10) comprises ion exchange resin (11b) and activated carbon (11a).    USE - Fuel cell system i.e. distribution type electric power generation system.    ADVANTAGE - The control part is controlled to stop operation of the supplementary water part when accumulation operating time of the supplementary water part is above the predetermined time, so as to maintain the water-purifying performance of the water-purifying part, thus avoiding need of replacement of a hydrogen generating apparatus at the time of a failure stop of the system, and hence reducing repairing cost of the system and improving reliability of the system.    DETAILED DESCRIPTION - The fuel cell is selected from one among polymer electrolyte fuel cell, phosphoric acid-type fuel cell or solid oxide fuel cell. An INDEPENDENT CLAIM is also included for a method for operating a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.'(Drawing includes non-English language text)'    Hydrogen generation part (1)    Fuel cell (5)    Water collection part (7)    Water-purifying part (10)    Activated carbon (11a)    Ion exchange resin (11b)    Supplementary water part (12)    Fuel cell system (100)    Control part (101)
NOVELTY - Kraft pulp wastewater is anaerobically treated by oil/water-separating kraft pulp wastewater to separated sludge containing fats and oil and a supernatant liquid, performing methane fermentation treatment of separated sludge, and anaerobically processing treated water and supernatant liquid of methane fermentation process.    USE - An anaerobic treatment method of kraft pulp wastewater (claimed).    ADVANTAGE - Kraft pulp wastewater containing fats and oil can be biologically treated stably efficiently, and stabilization of methane fermentation treatment and efficiency improvement can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic treatment apparatus of kraft pulp wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of an anaerobic treatment method of kraft pulp wastewater. (Drawing includes non-English language text).    Oil-water separation tank (1)    Methane fermentation tank (3)    PH control tank (8)    Anaerobic processing tank (12)
NOVELTY - Producing biogas comprises (a) carrying out anaerobic fermentation of an organic starting material (14) such that biogas (30) and a primary fermentation product (32) are formed, (b) supplying an oxidant (24) to the primary fermentation product, in such a manner that a hydrolyzate (34) is formed, and (c) fermenting the hydrolyzate under anaerobic conditions.    USE - The method is useful for producing biogas.    ADVANTAGE - The method produces biogas with higher yield, and shortens the residence time of the starting material in the fermentation tank of the biogas plant that is easy to retrofit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant comprising (i) an anaerobic-fermentation tank, in which at least intermittently organic starting material is fermented under anaerobic conditions to produce biogas and the primary fermentation product, and (ii) an oxidizing agent-supplying means for supplying the oxidizing agent to the primary fermentation product.    DESCRIPTION OF DRAWING(S) - The drawings (1 and 2) show a schematic representation of the biogas plant, the Drawing includes non English language text.    Starting material (14)    Oxidizing agent (24)    Biogas (30)    Primary fermentation product (32)    Hydrolyzate (34)
NOVELTY - Compost container comprises box with double lid structure for injecting material, box main unit in which upper and lower surfaces are opened, upper cover and lower cover attached to the box main unit, where the upper cover is opened, material to be injected is thrown into the box main unit, upper cover is closed, lower cover is opened, material structure is injected and lower cover is closed after dropping material into the container.    USE - The compost container is useful for composting materials including organic waste.    ADVANTAGE - The compost container reliably prevents jumping out of vermicule including fly from container at the time of injecting organic waste as it is automatically closed after injecting materials.
NOVELTY - Preparing highly purified benidipine hydrochloride by ultrasound technology, comprises: acyl chloridizing dihydropyridine and then linking side chain to synthesize benidipine hydrochloride directly, introducing ultrasound technology, and dispersing and dissolving reactant material by the ultrasound, and/or ultrasound technology, obtaining crude crystal or product by heating benidipine hydrochloride to dryness obtained via method or other possible synthetic routes during pre-treatment stage and obtaining highly purified benidipine hydrochloride by ultrasound during the post-treatment stage.    USE - The method is useful for preparing highly purified benidipine hydrochloride by ultrasound technology.    ADVANTAGE - The method: avoids separation process by column chromatography, and simplifies the process to make operation easier; reduces use and discharge of organic solvents; and allows saving of human and material resources, time and cost, and is in favor of environmental protection.    DETAILED DESCRIPTION - Preparing highly purified benidipine hydrochloride by ultrasound technology, comprises: acyl chloridizing the main ring of dihydropyridine and then linking the side chain to synthesize directly benidipine hydrochloride, introducing ultrasound technology, and dispersing and dissolving the reactant material by the ultrasound, and/or ultrasound technology, obtaining crude crystal or product by heating the benidipine hydrochloride to dryness obtained via method or other possible synthetic routes during pre-treatment stage and then obtaining highly purified benidipine hydrochloride by ultrasound during the post-treatment stage.
NOVELTY - Manufacturing a solid oxide fuel cell element (2) by layer-wise buildup, in which at least one section of the solid oxide fuel cell element is built up by: applying a layer section of a particulate ceramic material with predefined dimensions onto a base layer in a predefined area; and heating the layer section by a heat source such that the particles of the ceramic material connect to one another within the predefined dimensions.    USE - For manufacturing a single-piece solid oxide fuel cell element by layer-wise buildup (claimed).    ADVANTAGE - The method manufactures solid oxide fuel cell element in one piece; is highly compact; and has a low weight.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic lateral section of a solid oxide fuel cell element.    Solid oxide fuel cell element (2)    Center axis (4)    First cover (12)    Second cover (18)    Cathode (24)    Air duct (28)    Supporting structures (32)
NOVELTY - Process of converting solid biomass material (102) involves producing cracked products by contacting solid biomass material with catalytic cracking catalyst (108) at more than 400 degrees C in a riser reactor (107) comprising a riser reactor pipe having diameter which increases in downstream direction, and a bottom section (106) having diameter more than the riser reactor pipe. The solid biomass material is supplied to the riser reactor in the bottom section.    USE - Process of converting solid biomass material into biofuel and/or biochemical (claimed).    ADVANTAGE - The method efficiently and economically converts solid biomass material into biofuel and/or biochemical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofuel and/or biochemical, which involves mixing one or more other components.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the process of converting solid biomass material into biofuel and/or biochemical.    Solid biomass material (102)    Steam feed (104)    Bottom section (106)    Riser reactor (107)    Cracking catalyst (108)
NOVELTY - Producing (P1) bio-distillate fraction involves converting biomass in a conversion reactor containing a catalyst to produce conversion reactor effluent comprising vapor conversion products; condensing at least portion of the vapor conversion products to provide bio-oil having total oxygen content of less than 15 wt.%; and separating bio-distillate fraction from the bio-oil, where the bio-distillate fraction (at least 75 wt.%) has boiling point 180-380 degrees C, and where the bio-distillate fraction comprises oxygen-free hydrocarbons (at least 50 wt.%).    USE - For producing bio-distillate fraction; and for producing renewable distillate (claimed).    ADVANTAGE - The bio-distillate fraction is of high quality, having a low oxygen content, undetectable carboxylic acids, and significant amounts of cyclic/aromatics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing (P2) renewable distillate involving separating bio-oil into at least a bio-distillate fraction, where the bio-distillate fraction (at least 75 wt.%) has boiling point 180-380 degrees C, where the bio-oil has not previously been subjected to oxygen-removing hydrotreatment step; and combining at least a portion of the bio-distillate fraction with petroleum-derived-distillate-range stream and stabilizing additive having surfactant properties, to produce a renewable distillate having a single clear phase, where the renewable distillate comprises (wt.%) petroleum-derived-distillate-range stream (5-99), bio-distillate fraction (at least 0.5), and stabilizing additive (0.5-25).
NOVELTY - The manufacturing method involves attaching a separator to a membrane electrode assembly (2) to produce a unit cell (16), such that the separator contacts a gas diffusion layer. A fuel cell stack is produced by stacking the unit cells. The membrane electrode assembly, on which the gas diffusion layer is laminated, is immersed in an alkaline solution.    USE - Manufacturing method for fuel cell.    ADVANTAGE - Enables efficient ion exchange of electrolyte layer, and ensures a high operativity at the time of preparation of the fuel cell, thus reducing manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic views of a manufacturing method for fuel cell.    Membrane electrode assembly (2)    Electrolyte layer (5)    Anode electrode (6)    Cathode electrode (7)    Unit cell (16)
NOVELTY - The method involves mixing binding material and powder material for a mixture for forming an anode with low melting point organic substance, and preparing a molded mask with a penetration opening. The mixture is heated beyond the melting point of a low melting point organic substance e.g. polyethyleneglycol, which is in liquid-phase. Fluid is made to flow in into the penetration opening of the molded mask installed in a surface of an electrolytic membrane (2), and the fluid is solidified. The anode is baked up to a green state in a calcination-temperature region.    USE - Method for manufacturing an anode support type solid oxide fuel cell.    ADVANTAGE - The method enables the fluid to flow into the penetration opening of the molded mask installed on the surface of the electrolytic membrane, so that the anode is molded on the surface of an electrolytic membrane, thus allowing the low melting point organic substance to solidify in a rapid manner and maintaining strength and shape retention property of the anode. The method enables solvent that does not evaporates in a normal temperature region to maintain or store the anode, so that evaporation of the solvent from the anode is suppressed, thus suppressing crack accompanying evaporation of the solvent before-baking the anode, and hence simplifying manufacturing process of the cell. The method enables a laminated body to be integrally baked in the calcination-temperature region in a kiln at atmospheric condition, so that the laminated body is provided with a baked reaction barrier layer, thus improving oxygen ion conductivity along thickness direction.    DETAILED DESCRIPTION - The melting point of the organic substance is 40 to 90 degree centigrade.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an anode support type solid oxide fuel cell.    Reaction barrier layer (1)    Electrolytic membrane (2)    Laminated body (3)    Table (50)    Installation surface (50u)    Film (53)
NOVELTY - An organic substance fertilizer formation-processing apparatus (10) consists of a container main component (11) provided with an opening (11a) for taking out biodegraded organic substance, while organic substance (W) and oxygen generation substance (O) are injected, a lid (12) which can open and close the opening, and a sealing unit (14) which seals the clearance gap between the lid and container main component in a state in which the opening is closed.    USE - Apparatus is used for formation-processing of organic substance fertilizer (claimed).    ADVANTAGE - The apparatus enables efficient utilization of fermentation heat produced from oxygen supply substance and efficient fertilizer formation of organic substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for formation-processing of organic substance fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the internal structure of the organic substance fertilizer formation-processing apparatus.    Organic substance fertilizer formation-processing apparatus (10)    Container main component (11)    Opening (11a)    Heat insulation walls (11d,12a)    Lid (12)    Sealing unit (14)    Stirring unit (15)    Oxygen generation substance (O)    Organic substance (W)
NOVELTY - Method for processing gas containing methane as main component, involves adding hydrogen to target gas containing oxygen and carbon monoxide as an impurity and methane as a main component, and reacting the product using ruthenium catalyst to generate methane and water, where the oxygen content ratio and carbon monoxide content rate of the target gas are reduced by reaction.    USE - The method is useful for processing gas containing methane as main component.    ADVANTAGE - The method prevents degradation of biogas and reduces the content of oxygen and carbon monoxide in gas.
NOVELTY - Methane generating device comprises a residential building, kitchens, organic waste discharge pipes, toilets, windows, light-emitting diode head lamps, toilet stools, excrement discharge pipes, a methane pool, an efficient methane bacteria throwing pipe, methane slurry, a methane residue outlet, a methane conveying pipe, a methane storage tank and a methane generator. The organic waste discharge pipes are extended into the kitchens. The lower ends of the organic waste discharge pipes are extended into methane pool. The excrement discharge pipes are extended into toilets.    USE - The device is useful in independent residential building for treating waste and excrement.    ADVANTAGE - The device decomposes the organic waste and the excrement by using efficient methane bacteria in the methane pool for generating methane, which is introduced into the methane storage tank, and then introduces into a methane generator for generating current which is introduced into light-emitting diode head lamps of each floor for supplying power and lighting.
NOVELTY - A synergism device comprises solar battery, photovoltaic strut, electrical lead, controller, inverter, energy storage battery, electrical water pump, geothermal water storage tank, geothermal water, methane storage chamber, output water radiating pipe, methane pool, geothermal water pumping pipe, biogas slurry, floor surface layer, warm water spraying micro-hole nozzle, bottom water storage chamber, and geothermal layer. The lower half part of the methane pool is buried in the earth layer under the floor surface layer.    USE - Synergism device for conveying warm water for pipeline network in methane pool wall through geothermal heat.    ADVANTAGE - The heat of out-flowing geothermal heat water is uniformly sprayed to the biogas slurry through an output water radiating pipe distributed in the pool wall from top to bottom. The warm water is properly sprayed out from warm water spraying micro-hole nozzle mounted on the output water radiating pipe wall so as to adjust the humidity and temperature of the methane pool inner. The proper temperature environment is provided by the circulation of geothermal heat water so that the methane bacteria accelerate the decomposition of organic matter; and the gas yield of the methane pool is improved.
NOVELTY - Thermal decomposition gasification of solid-state primary raw material containing carbon and hydrogen in a molecule is carried out to obtain a gas (G1) containing hydrogen and carbon monoxide. Steam gasification of solid-state raw material same or different from primary raw material and containing carbon and hydrogen in molecule is carried out to obtain gas (G2) containing hydrogen and carbon monoxide. The gases (G1,G2) are mixed based on molar ratio of hydrogen and carbon monoxide, and synthesis gas is produced. Alcohol is then produced from synthesis gas.    USE - Manufacture of alcohol e.g. methanol.    ADVANTAGE - Alcohol is easily, economically and stably produced with improved energy efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for alcohol manufacturing apparatus, which has a primary reactor (1) for carrying out thermal decomposition gasification of solid-state primary raw material, a secondary reactor (2) for carrying out steam gasification of solid-state secondary raw material, tertiary reactor (3) for producing alcohol, and a synthesis gas supply unit for mixing gases (G1,G2).    DESCRIPTION OF DRAWING(S) - The drawing shows the flow sheet explaining synthesis of alcohol. (Drawing includes non-English language text)    Reactors (1-3)    Heater (11)    Heat exchanger (14)    Intermediate tank (15)    Gas analysis apparatus (24)
NOVELTY - Apparatus comprises container unit, rotating shaft, rotor blade, raw material inlet, and product outlet. The container unit is provided with base with lid. The rotating shaft is rotated with drive source (X) which is provided in center part of container unit. The rotating shaft has several rotor blades. The upper surface of raw material inlet is provided with container unit containing lid. The product outlet is provided in bottom part of container unit and heat source (Y) for blowing hot air.    USE - The apparatus is useful for manufacturing compost (claimed), preferably organic fermented fertilizer.    ADVANTAGE - The apparatus produces compost rapidly and is suitable for large scale production.    DETAILED DESCRIPTION - Apparatus comprises container unit, rotating shaft, rotor blade, raw material inlet, and product outlet. The container unit is provided with base with lid. The rotating shaft is rotated with drive source (X) which is provided in center part of container unit. The rotating shaft has several rotor blades. The upper surface of raw material inlet is provided with container unit containing lid. The product outlet is provided in bottom part of container unit and heat source (Y) for blowing hot air. The thermocouple (Z) carries out temperature control of heat source (Y) provided in inner wall face of container unit.
NOVELTY - The method involves diluting enzyme liquid phase, microbial metabolites and citric acid in the liquid biological product. The perfume is mixed with purified water and sprayed using injector or humidifier in indoor/outdoor air.    USE - Odor removal method of organic waste from livestock excretions, liquid, food, human excrement and drink waste dump site, for use in dwelling and stockbreeding farmhouse.    ADVANTAGE - The generation of bad smell from the organic waste due to metabolite ammonia, trimethylamine and formaldehyde reaction can be prevented. The foot-and-mouth disease virus can be destroyed from the organic waste. The processing cost of livestock excretions in stockbreeding farmhouse is reduced.
NOVELTY - Manufacturing methanol from methane and oxygen in a single step where methane and oxygen are reacted over a heterogeneous catalyst comprising the chlorides of copper, potassium, lead and zinc to produce methanol, the reaction being conducted at 375-475 degrees C and under a pressure of 1-20 atmospheres.    USE - For manufacturing methanol from methane and oxygen (claimed).    ADVANTAGE - The method provides for the direct i.e. one-step, conversion of methane to methanol using a robust catalyst which offers high selectivity under operating conditions.
NOVELTY - Method for producing microalgae containing high content of lipid, involves collecting the effluent from wastewater disposal, pre-processing the collected effluent, and cultivating the microalgae in preprocessed effluent.    USE - The method is useful for producing microalgae containing high content of lipid, which is useful for biofuel (claimed).    ADVANTAGE - The method produces high content of lipid with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for increasing productivity of the microalgae, involves performing above-cited steps.
NOVELTY - Method for producing vehicle urea, involves (a) passing urine sample through first, second and third grade crystallizer, removing the crystals at first and second level crystallizer temperature section, and retaining the crystallization temperature of third temperature section, (b) dissolving the obtained crystals in hot desalted water, and stirring the mixture continuously, (c) controlling the temperature of the mixture, cooling the mixture, and (d) formulating the mixture into solution containing urea and pure water.    USE - The method is useful for preparing urea which is used in vehicles.    ADVANTAGE - The method is simple, convenient to perform, safe, environmentally-friendly, and suitable for industrial production, and produces urea with high market value.
NOVELTY - Method for manufacturing 2,6-dichloro-3-nitropyridine, involves adding sulfuric acid as solvent, 2,6-dichloropyridine as raw material, nitric acid as nitrating agent and sulfamic acid as catalyst to obtain mixture, and reacting the mixture at 20-150 degrees C for 10-40 hours.    USE - The method is useful for manufacturing 2,6-dichloro-3-nitropyridine (claimed).    ADVANTAGE - The method is simple, stable and environmentally-friendly, provides high yield of 80% or more, and reduces usage of nitric acid and sulfuric acid.
NOVELTY - Composite compact-type biomass fuel comprises (in part by wt.) house refuse (15-70, preferably 25-35), kitchen waste (5-40, preferably 5-20), drainage sludge (10-80, preferably 15- 25), human and livestock excrements (10-30, preferably 15-25) and agricultural and forestry waste (10-30, preferably 15-25).    USE - Used as a composite compact-type biomass fuel.    ADVANTAGE - The biomass fuel is obtained by the treating the house refuse, the kitchen waste, the agricultural and forestry waste, the drainage sludge and the human and livestock excrements, and can be produced by a wet process in a large scale under normal temperature and normal pressure without the heat value loss. The method has simple preparation process, is feasible and ecofriendly, and ensures low investment and operating costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biomass fuel, comprising: (a) collecting separately the raw materials, deodorizing and sterilizing the house refuse, the kitchen waste, the drainage sludge and the human and livestock excrements; (b) at least sorting the house refuse and the kitchen waste for removing the plastic and the rigid substances, and pre-treating the sorted raw materials by crushing; (c) mixing completely the materials obtained in step (b), sampling to measure sulfur content, and adding the desulfurizing agent according to a ratio of (1.2:1)-(1.8:1) of the desulfurizing agent and the sulfur content; (d) transferring into a kneading device for kneading the material for at least once; and (e) adding the kneaded materials into a molding device for obtaining a crude sample of the composite compact-type biomass fuel, and drying.
NOVELTY - System comprises molecular sieve material zeolite, clusters of devices and units for normalization and recovery of alcohol from wastewater    USE - The system is useful in devices for refining alcohol to produce pure alcohol (99.5 wt.%) for production of alcoholized gasoline using an automatic operation technology.    ADVANTAGE - The system refines the alcohol with less energy consumption and high purity and without pollution.    DETAILED DESCRIPTION - The system comprises a molecular sieve material zeolite 4A, and clusters of main devices, and a unit for material normalization, adsorption and desorption and recovery of alcohol from wastewater. The system refines the alcohol by normalizing the material, refining alcohol and returning alcoholized water.
NOVELTY - A water electrolysis hydrogen production groove device comprises two independent parallel electrolysis grooves having adjacent polar plates connected by a conductive connection piece.    USE - A water electrolysis hydrogen production groove device.    ADVANTAGE - The device improves work pressure of electrolysis groove and increases yield.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a water electrolysis hydrogen production groove device.
NOVELTY - An energy conversion system device comprises power supply source, electrolysis tank, electric quantity recovery device, and controller. Power supply source is connected with electrolysis tank and controller for providing electricity to electrolysis tank and controller. Electrolysis tank is connected with electric quantity recovery device. Electric quantity recovery device is provided with cathode plate and anode plate. The electric quantity consumed by electrolysis is recovered through the electric field comprising anode plate and cathode plate on one hand.    USE - System device for converting solar energy into hydrogen energy.    ADVANTAGE - The device can recover consumed electric quantity for electrolysis, can recycle recovered electric quantity to make hydrogen, thus solving bottleneck of large electric consumption for electrolysis water, and low-cost industrialization of system device.    DETAILED DESCRIPTION - Energy conversion system device comprises power supply source, electrolysis tank, electric quantity recovery device, and controller. Power supply source is connected with electrolysis tank and controller for providing electricity to electrolysis tank and controller. Electrolysis tank is connected with electric quantity recovery device. Electric quantity recovery device is provided with cathode plate and anode plate. The electric quantity consumed by electrolysis is recovered through the electric field comprising anode plate and cathode plate on one hand. Recovered electric quantity is transported to electrolysis tank by one or multiple times and the required voltage for electrolysis is supplied. Controller is connected with electric quantity recovery device to control electric quantity recovery time and quantity. Controller comprises process logic controller (PLC) programmable program controller and automatic control system.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an energy conversion system device.
NOVELTY - A trityl olmesartan is reacted with medoxomil chloride in presence of alkali metal iodide, 18-crown-6 and toluene, xylene and/or acetone at 20-35 degrees C, to obtain trityl olmesartan medoxomil.    USE - Preparation of trityl olmesartan medoxomil.    ADVANTAGE - The method enables quick and economical preparation of trityl olmesartan medoxomil, without environmental pollution.
NOVELTY - The system (100) has a frame (120) that is formed on a base (110). A hollow (121) is formed inside the frames. The fuel (130) of the hydrocarbon class is filled in the hollow of frames. A fuel reformer (160) is connected to the frame for accommodating fuel and water so as to generate hydrogen through the reformate reaction. A fuel cell (170) is connected to the fuel reformer.    USE - Fuel cell system for vehicle.    ADVANTAGE - The space utilization can be improved. The mechanical strength of the fuel cell system can be secured. The vibration resistance/impact resistance of the fuel cell system can be improved. The recovery efficiency of the generated water can be improved. The maintenance and repair of the fuel cell system can be facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell system.    Fuel cell system (100)    Base (110)    Frame (120)    Hollow (121)    Fuel (130)    Fuel reformer (160)    Fuel cell (170)
NOVELTY - The hydrogen and oxygen generator has an electrolysis device that includes an insulation case (10) forming a space for accommodating an electrolyte and electrode plates (12) which are parallelly placed within insulation case. An electromagnetic field generation unit (18) generates an electromagnetic field in the circumference of the electrode plates.    USE - Hydrogen and oxygen generator.    ADVANTAGE - Energy efficiency of the hydrogen and oxygen generator can be improved and the reaction zone formed between electrode plates can be maintained uniformly. Optimum temperature of the electrolyte can be maintained and electrolysis process can be performed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen and oxygen generator.    Insulation case (10)    Electrode plate (12)    Connection terminal (14)    Electromagnetic field generation unit (18)    Circulating pipe (20)
NOVELTY - Method consists in loading of ground raw materials - biomass - to a thermochemical reactor, biomass pyrolysis without air access to temperature of thermal decomposition to produce appropriate products and synthesis gases discharged from a reactor to a circulating flow and to a load. The pyrolysis process in the reactor is carried out with simultaneous introduction of coolant in it based on gaseous products heated to pyrolysis temperature, such as synthesis gases drained from a circulating flow, at the same time coolant used in process of pyrolysis additionally contains water vapours and/or carbonic acid, the latter of which or water is introduced into a flow of gaseous products prior to their heating to pyrolysis temperature. Amount of specified products introduced into a gaseous flow corresponds to (0.2-1.5)G, where G is the amount of loaded biomass into a thermochemical reactor. The process of biomass processing in the reactor is carried out at the pyrolysis temperature of 600 degrees C-1100 degrees C and pressure of gaseous products equal to 0.1-10 MPa. Ground raw materials - biomass - may be wood chips or kindlings with fraction size from 2-15 mm, or wood flour with particle size of not more than 0.15 mm. Carbonic gas and water used in a coolant have ratio of 1:1.    USE - Power engineering.    ADVANTAGE - Method improvement. 3 cl, 1 dwg
NOVELTY - Biodiesel has become more attractive recently because of its environmental benefits and the fact that it is made from renewable resources. There are two aspects of the cost of biodiesel, i.e. the cost of raw material and the cost of processing. In order to reduce the cost of processing, a novel technology like bubble washing method before the transesterification process, is introduced. This method is very useful for doing the research work for small batch-type unit and large scale unit for producing the biodiesel from the nonedible oils. It is cost effective and simple method. This method is performed with an experimental setup using a small air pump for bubble washing the oil. The water-soluble saturated and unsaturated fat present in the oil are completely removed from the bubble washing method. The experiment results proved that after bubble washing technology, the yield of biodiesel production has improved by 2% and the amount of each of solvent and catalyst are reduced by 40%. Biodiesel produced from the purified oils using bubble washing method gives 2% of excess yield compared than ordinary method. At the same time, it consume less amount of the solvent and catalyst when compared to biodiesel produced from ordinary method. Image 0/3
NOVELTY - The method involves mixing fresh raw material oil with solvent or diluting agent i.e. heavy naphtha, naphtha, light hydrocarbon, light distillate oil, diesel fuel, hydrocarbon oil vacuum gas oil (VGO) and hydrogen. Hydrogen gas is passed in the mixed fresh raw material oil. The mixture is made to flow to a reactor. A gas-liquid separation part is executed from a reactor catalyst bed layer by an outflow part of the reactor. The solvent or diluting agent is circularly separated by the gas-liquid separation part. The reactor is divided into two sections.    USE - Two-phase hydrogenation method.    ADVANTAGE - The method enables avoiding recycling of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a two-phase hydrogenation method.
NOVELTY - Device comprises a feeding port, a feeding auger, a pyrolysis chamber, a burner, a furnace body, a temperature probe, a temperature control system, a chimney, a first condensing tower, a second condensing tower, a cleaning system, a discharging hopper and a discharging packing auger. The pyrolysis chamber is set in the furnace body, which is set with a burner. An actuator is connected to the burner. The pyrolysis chamber is provided with a feeding front end port. The feeding port is provided with a feeding auger. The first condensing tower is connected with the second condensing tower.    USE - The device is useful for automatically controlling the temperature of biological carbon continuous production.    ADVANTAGE - The device: utilizes the self-generated pyrolysis gas to supply energy to the subsequent biomass pyrolysis; reduces the operation cost; automatically separates the bio-char, tar, wood vinegar and combustible gas; solves the problem of the biomass constant-temperature pyrolysis, continuous production and supplying energy; has simple operation; produces the biological carbon and by-products with stable quality; and is suitable for biomass and biological carbon production with different sizes and different types.
NOVELTY - Dehydrating bio-1-alcohol, comprises: providing at least one bio-1-alcohol, where the bio-1-alcohol has 1 ppm to 90% of water; heating the bio-1-alcohol with at least one desired catalyst; and controlling dwell time and temperature with at least one purge gas at a rate of 0.01-1/mass of the catalyst/hour to produce bio-1-alkene with high selectivity (greater than 95%).    USE - The method is useful for dehydrating bio-1-alcohols to bio-1-alkenes including bio-1-butene, where the bio-1-alcohol is bio-1-butanol (all claimed). The bio-1-alkenes are useful for preparing high flashpoint diesel biofuels and jet biofuels.    ADVANTAGE - The method is capable of dehydrating bio-1-alcohols to produce bio-1-alkenes with high selectivity and purity.
NOVELTY - Method for generating at least one fermentable sugar, involves contacting a substrate comprising cellulose with an enzyme mixture comprising two or more cellulose hydrolyzing enzymes, where at least one of the two or more cellulose hydrolyzing enzymes is produced by a Myceliophthora fungal cell that has been genetically modified to reduce the amount of endogenous cellobiose oxidizing enzyme activity that is produced by the fungal cell.    USE - The method is useful for generating at least one fermentable sugar and obtaining at least one end product from fermentable sugar. The fermentable sugar comprises glucose or cellobiose. The end product is a fuel alcohol or a precursor industrial chemical. The fuel alcohol is ethanol or butanol (all claimed).    ADVANTAGE - The method improves yield of the fermentable sugar.    DETAILED DESCRIPTION - Method for generating at least one fermentable sugar, involves contacting a substrate comprising cellulose with an enzyme mixture comprising two or more cellulose hydrolyzing enzymes, where at least one of the two or more cellulose hydrolyzing enzymes is produced by a Myceliophthora fungal cell that has been genetically modified to reduce the amount of endogenous cellobiose oxidizing enzyme activity that is produced by the fungal cell, and the fungal cell has been genetically modified by deleting endogenous cellobiose dehydrogenase enzymes having at least about 90% or at least about 95% sequence identity to a 828 amino acid sequence (SEQ ID NO: 6) fully defined in the specification or a 787 amino acid sequence (SEQ ID NO: 8) fully defined in the specification.
NOVELTY - Method for producing ethanol involves contacting a mixture comprising xylose with a Spathaspora passalidarum yeast cell under conditions suitable to allow the yeast to ferment at least a portion of the xylose to ethanol.    USE - The method is useful for producing ethanol.    ADVANTAGE - The method enables to produce 0.3 g of ethanol/gram of sugar in the mixture. The method enables to produce ethanol at rate of greater than or equal to 0.5 g/1 hour.
NOVELTY - The process involves contacting a solid biomass material (102) and a fluid hydrocarbon feed (110) with a catalytic cracking catalyst (122) at temperature of more than 400 degrees Celsius in a riser reactor (107) to produce cracked products (120), where the solid biomass material is supplied to the riser reactor at a location upstream of the location, and the fluid hydrocarbon feed is supplied to the riser reactor. The riser reactor is provided with a riser reactor pipe having diameter that increases in a downstream direction, and includes a bottom section (106).    USE - Process for converting a solid biomass material into renewable biofuels and biochemical utilized in an automotive engine. Uses include but are not limited to wood, sawdust, straw, grass, bagasse, corn stover, aquatic plants and algae, agricultural waste, forestry waste and paper waste.    ADVANTAGE - The process enables using an internal riser reactor to reduce risk of plugging due to polymerization and to reduce the risk of corrosion, thus ensuring safety and hardware integrity. The process allows the solid biomass material to be suspended in liquid such as water, thus improving processibility, and avoiding dusting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for converting a solid biomass material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a structure for converting a solid biomass material.    Solid biomass material (102)    Bottom section (106)    Riser reactor (107)    Fluid hydrocarbon feed (110)    Cracked products (120)    Catalytic cracking catalyst (122)
NOVELTY - Composition comprises waste products produced by oil mills, enzymes and at least one polyphenol resistant bacterium, preferably the bacterium comprises a bacterium from Bacilli class.    USE - The composition, kit, process and system are useful for the treatment of waste product produced by oil mills (all claimed).    ADVANTAGE - The composition, kit, process and system are environment friendly, and efficiently purify waste water.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) kit of parts for the treatment of waste product produced by oil mills comprising at least one polyphenol resistant bacterium and enzymes; (2) a process for the treatment of waste products produced by oil mills comprising: (a) contacting the waste product with at least one polyphenol-resistant bacterium to form a waste solution; (b) adding enzymes and, optionally, a pH regulator to maintain the pH of the solution between 6 and 9; (c) adding one or more fungi from Basidiomycetes class, and let rest for a time sufficient to provide a treated-waste product having a chemical oxygen demand lower than 125 mg/L, preferably lower than 110 mg/L; and (3) system for the treatment of waste products produced by oil mills comprising: extracting unit for extracting oil from plants or fruits, the extracting unit having a daily oil extraction capacity; separating unit, in fluid communication with the extracting unit, for separating oil from waste products, the latter being in fluid communication with a retention basin having a capacity of at least 2 fold the capacity in waste products of the extracting unit; a lagoon in fluid communication with the retention basin, the lagoon having a capacity at least 40 fold the capacity of the retention basin, preferably at least 50 fold.
NOVELTY - The system has a biomass gasification furnace receiving biomass raw materials through a screw feeder. A cyclone separator is connected with a dust air pre-heater. A gas purifier is connected with an air storage cabinet through a draught fan. A fuel gas internal combustion engine is connected with the air storage cabinet. A mechanical driving power output shaft drives an electric generator. A speed reducer controls rotating speed of the electric generator.    USE - Movable integrated high density biomass fuel preparation system.    ADVANTAGE - The system realizes zero-power consumption, reduces biomass fuel cost, and is flexible to operate.
NOVELTY - Temperature is applied to an organic substance initially, carbonization is advanced by self-heating, and inorganic carbon is produced. In using organic substance, such as organic waste, as carbonization product in a carbonization furnace, the carbon dioxide conversion value of greenhouse gases, such as heat amount in the case of carbonization product manufacture and generated dinitrogen monoxide, becomes carbon dioxide emission during manufacture of carbonization product.    USE - Fixing of carbon dioxide as inorganic carbon raw material by carbonization of organic substance, by using as soil improvement material, agricultural-place improvement material, construction cultivating soil improvement material, and construction waste soil improvement material (all claimed).    ADVANTAGE - The method efficiently reduces carbon dioxide in atmosphere.    DETAILED DESCRIPTION - Temperature is applied to an organic substance initially, carbonization is advanced by self-heating, and inorganic carbon is produced using a small amount of heat. In using organic substance, such as organic waste, as carbonization product in a carbonization furnace, the carbon dioxide conversion value of greenhouse gases, such as heat amount in the case of carbonization product manufacture and generated dinitrogen monoxide, becomes carbon dioxide emission during manufacture of carbonization product. The discharge amount of carbon dioxide of carbonization product manufacture becomes less than the carbon dioxide equivalent amount of inorganic carbon as a product. When the carbonization product (inorganic carbon) made by such a manufacturing method is used effectively as soil improvement material and fixed in soil, carbon dioxide in atmosphere is reduced and global warming is prevented.
NOVELTY - A groove type compost turning machine comprises a machine frame, a walking mechanism, a transmission mechanism and a turning device. The right part comprises oil cylinder bracket, first connecting rod, lifting mechanism, second connecting rod and rocker. A long hole groove is provided to the upper part of machine frame. The oil cylinder bracket hinged on top end is installed with an oil cylinder by a pin shaft and oil cylinder piston rod of cylinder. The back end section of the target rod shaft is connected with the lifting device.    USE - Groove type compost turning machine.    ADVANTAGE - The machine has adjustable height, simple structure, and safe and reliable use, effectively increases the accumulation of the compost, and improves the compost drying rate.
NOVELTY - The element (100) has a porous heat-emitting part (102a) provided in a porous heat generating body (101), which comprises continuous air holes (101b). A porous electro conductive part (104a) is provided in a porous conductor (111) comprising continuous air holes, where the porous heat-emitting part and the porous electro conductive part are provided in a common porous body and formed by formation of a heat-generating body or the porous conductor in a predetermined area of the common porous body. A conductive layer is formed in a surface of the predetermined area of the heat generating body.    USE - Porous heater element for use in a gas decomposing element (claimed) of a gas decomposition apparatus for removing ammonia during exhaustion process in compound semiconductor manufacture of a phosphoric acid fuel cell.    ADVANTAGE - The element allows the porous electro conductive part to be formed with the porous body of the same form and porosity, so that flow resistance of gas is same in the electro conductive part and the porous body, thus making the gas to flow uniformly within a porous body, and hence allowing the gas to be heated efficiently, while reducing size of the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a porous heater element.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a porous heater element.    Porous heater element (100)    Porous heat generating body (101)    Continuous air holes (101b)    Porous heat-emitting parts (102a, 102b, 102c)    Electrode plate (103a)    Porous electro conductive parts (104a, 104b, 104c, 104d)    Porous conductor (111)
NOVELTY - The solid oxide fuel cell (12) includes a solid electrolyte layer (2) arranged at the outer peripheral edge (3a) of a fuel electrode layer (3) and surrounded by the outer peripheral edge (5a) of a separator (5). An excessive gas, which is not consumed by a power generation reaction, is released from the outer periphery of an electric power generation cell (1).    USE - Solid oxide fuel cell for generating electric power.    ADVANTAGE - Prevents cracking of an electric power generation cell by preventing oxidation of the fuel electrode layer. Suppresses crack initiation of solid electrolyte layer due to volume expansion of the fuel electrode layer.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of a solid oxide fuel cell with a flat electric power generation cell.    Electric power generation cell (1)    Solid electrolyte layer (2)    Fuel electrode layer (3)    Outer peripheral edge (3a)    Separator (5)    Outer peripheral edge (5a)    Solid oxide fuel cell (12)
NOVELTY - The apparatus has a mixture acceptance part (70) for accepting a mixture (60) supplied from a mixture supply part (26). A suction part (37) is mounted on a porous board (16), where a coating table (36) moves relatively with respect to two coating chambers (20, 21). The suction part is arranged in a position opposite to two mixture exit parts (29, 30) along downward direction of the mixture exit parts, respectively when the coating table exists in a downward position of the coating chambers. An exhaustion blower (40) discharges sucked air downwardly from the suction part.    USE - Apparatus for manufacturing a fuel cell electrode that is utilized in a battery.    ADVANTAGE - The apparatus allows a catalyst layer to be formed without a gap of an interface by sucking only the coating chamber and masking an opening, so that an oxidizing agent electrode is used for manufacturing the catalyst layer, thus suppressing gas diffusion defect in downstream of the oxidizing agent electrode to achieve stable characteristic of the electrode, and hence enabling easy manufacturing of the fuel cell electrode having distribution inside a surface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell electrode manufacturing apparatus.    Porous board (16)    Coating chambers (20, 21)    Mixture supply part (26)    Mixture exit parts (29, 30)    Coating table (36)    Suction part (37)    Exhaustion blower (40)    Mixture (60)    Mixture acceptance part (70)
NOVELTY - A hybrid type hydrogen production and electric power generation system consists of a dehydrogenation device (2) and a high-temperature-form electric power generator (1). The dehydrogenation device is a multitubular-type heat-exchange-type reactor using a fixed bed of dehydrogenation catalyst consisting of a uniform highly dispersed type platinum-alumina catalyst. Heat recovered from the waste gas of electric power generator is introduced into the dehydrogenation device as one portion of or entire portion of heat required for dehydrogenation.    USE - Hybrid type hydrogen production and electric power generation system is used for producing electric power.    ADVANTAGE - The hybrid type hydrogen production and electric power generation system achieves efficient improvement of synthetic heat-use combining manufacture of hydrogen.    DETAILED DESCRIPTION - A hybrid type hydrogen production and electric power generation system consists of a dehydrogenation device and a high-temperature-form electric power generator. The dehydrogenation device is a multitubular-type heat-exchange-type reactor using a fixed bed of dehydrogenation catalyst consisting of a uniform highly dispersed type platinum-alumina catalyst. Dehydrogenation of a hydrogenated aromatic compound is carried out in the presence of the catalyst and hydrogen is produced. While introducing the obtained hydrogen into the electric power generator, heat recovered from the high-temperature waste gas of electric power generator is introduced into the dehydrogenation device as one portion of or entire portion of heat required for dehydrogenation.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the process flow of the hybrid type hydrogen production and electric power generation system.    High-temperature electric power generator (1)    Dehydrogenation device (2)    Raw-material tank (6)    Reaction-product extraction line (8)    Heat exchanger (15)
NOVELTY - Hydrogen is generated by supplying apple press residue to fermentation tank (100) and producing hydrogen from carbohydrate and pectin contained in apple press residue by fermentation which uses hydrogen generation bacteria.    USE - Hydrogen generation method (claimed).    ADVANTAGE - Recovery of hydrogen is improved, composting is easily performed, and methane fermentation of biomass is efficiently carried out.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for 2-stage fermentation process which involves performing 1st stage fermentation by supplying substrate containing pectin to fermentation tank, performing hydrogen fermentation process using hydrogen generation bacteria, and carrying out methane fermentation process using methanogenic bacteria and performing 2nd stage fermentation by adding contents of fermentation tank in 1st stage to fermentation tank for 2nd stage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fermentation apparatus used for batch experiment of methane fermentation.    Fermentation tank (100)    Culture solution (101)    Head space of tank (102)    Stirring motor (110)    Airtight bearing (111)
NOVELTY - The system has water distribution pipes that are located on the top of front end of underflow and upper flow constructed wetlands, and are connected with water distribution regulating reservoir respectively. Several water outlet collecting pipes are connected with water outlet collecting pond. A composite padding of haycite and coal cinder is filled in lower end of upper wetlands. Several aquatic plants are planted on surface of composite padding of haycite, coal cinder and soil filled in upper end of upper wetlands. The composite padding of gravels and volcanics is filled on lower wetlands.    USE - Double-deck underflow constructed wetlands system for dispersive type sewage treatment in cold region of small and medium towns.    ADVANTAGE - The wetlands system can be operated stably in high and cold areas, even in the freeze-up period, by operating the upper flow constructed wetlands in summer and operating the underflow constructed wetlands in winter. The material cost and the operation cost of the wetlands system are reduced. The dispersive type sewage treatment can be performed on the sewage by the wetlands system efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of operating double-deck underflow constructed wetlands system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the double-deck underflow constructed wetlands system.
NOVELTY - The mesh is supported by a frame (1). The frame is comprised of one supporting cross element (6) in contact with to one surface of the mesh. The mesh surfaces are in contact with the supporting elements on both the sides. The mesh is arranged between the positive and negative metal electrode plates with one aperture at the perimeter edges for penetration and suspension by the cell assembly rods (2).    USE - Mesh used for separation of water atomic element such as oxygen and hydrogen used to cook, heat or boil liquids in domestic appliance, liquid vessel and in home heating system.    ADVANTAGE - The oxygen and hydrogen elements can be separated efficiently during electrolysis. The separation of the gas elements of water can be enabled on either side of the mesh. The mesh can be prevented from coming into proximity with the gas exit holes and metal electrode plates. The mesh can be prevented from being flaccid and blocking the gas exit holes in the adjacent components.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the mesh.    Frame (1)    Cell assembly rods (2)    Continuous raised rib (3)    Supporting cross element (6)    Node (7)
NOVELTY - Fuel oil composition comprises fuel oil blend, at least one ethylene-vinyl ester polymer and at least one polyalkylmethacrylate polymer, where the fuel oil blend comprises middle-distillate fuel oil and hydrotreated vegetable, animal or fish oil, and amount of hydrotreated vegetable oil in the fuel oil blend is sufficient to provide the blend with an increase in n-alkane distribution of at least 3 wt.% over the n-alkane distribution of middle-distillate alone.    USE - As fuel oil composition.    ADVANTAGE - The fuel oil composition has improved low temperature properties as measured by cold filter plugging point (CFPP), as it contains ethylene-vinyl ester polymer and polyalkylmethacrylate polymer, and reduced sulfur content and impurities.    DETAILED DESCRIPTION - Fuel oil composition comprises fuel oil blend, at least one ethylene-vinyl ester polymer and at least one polyalkylmethacrylate polymer, where the fuel oil blend comprises middle-distillate fuel oil and hydrotreated vegetable, animal or fish oil, and amount of hydrotreated vegetable oil in the fuel oil blend is sufficient to provide the blend with an increase in 15-20C n-alkane distribution of at least 3 wt.% over the 15-20C n-alkane distribution of middle-distillate alone.
NOVELTY - Defecated matter, if left untreated will cause environmental pollution and serious health hazards, which is evident from the offensive malodor and growing pathogenic population associated with fecal matter. Described is a bioprocess that uses a defined formulation comprising of microorganisms and harmless chemicals. The bioprocess results in accelerated degradation of organic matter that reduces the environment polluting organic load associated with fecal excreta. The bioprocess also inhibits the health compromising microbial pathogens that are inhibited by various metabolites produced by Lactobacillus component of microbial formulation. The bioprocess also results in the generation of methane gas subsequent to organic matter degradation and can be used as a source of fuel. The process also generates organic slurry that can be used as fertilizer/organic manure. Thus, described is a process for treatment of fecal excreta in closed or open environment to inhibit pathogens, malodor, and pollution associated with untreated fecal excreta. Image 0/0
NOVELTY - The method involves subsiding domestic sewage. The anaerobic microorganism fermentation treatment is performed in anaerobic tank (2) to produce sludge sediment, recycled water and methane. The recycled water and methane are passed to anaerobic tank. The sludge sediment and separated sewage are mixed, concentrated, and dried in concentration tank (3). The recycled water is flown into solid-liquid separator (6), and sterilized. The sterilized water is heated with heater (9) and boiler (10). The hot water is controlled by valve (12). The temperature of anaerobic tank is controlled.    USE - Comprehensive utilization method for domestic sewage.    ADVANTAGE - The comprehensive efficiency of sewage treatment is improved.    DETAILED DESCRIPTION - The aeration microbial decomposition is performed in aerobic tank (5) through recycled water. The produced sludge is refluxed to the anaerobic tank. The sludge is pumped and discharged into the concentration tank. The produced sludge sediment is pumped and discharged into the concentration tank. The filtered clean water is pumped into high tower sterilization tank (8). The temperature of the anaerobic tank bottom space is maintained keeping at the range of 35 plus or minus 5 degrees C. The pressure of the produced methane of the anaerobic tank is transferred to gasholder (13).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating comprehensive utilization process of domestic sewage.    Anaerobic tank (2)    Concentration tank (3)    Aerobic tank (5)    Solid-liquid separator (6)    High tower sterilization tank (8)    Solar water heater (9)    Gas-fired boiler (10)    Control valve (12)    Gasholder (13)
NOVELTY - Processing organic solid waste involves processing the raw materials: grinding the organic solid waste, obtaining the ground materials; naturally stack retting the ground material; earthworm compost: adding earthworm into the naturally stack retting materials, producing percolation liquid in the process; and drying anaerobic fermentation: turning and stirring the fermenting materials at fixed period, obtaining the fermented biogas residue, producing percolation liquid in the process.    USE - For processing organic solid waste (claimed).    ADVANTAGE - The method accelerates the degradation rate of organic matter; increases the recycling rate; and improves the quality of the product.    DETAILED DESCRIPTION - Processing organic solid waste involves processing the raw materials: grinding the organic solid waste, obtaining the ground materials; naturally stack retting the ground material; earthworm compost: adding earthworm into the naturally stack retting materials, producing percolation liquid in the process; and drying anaerobic fermentation: turning and stirring the fermenting materials at fixed period, obtaining the fermented biogas residue, producing percolation liquid in the process. The method also involves high temperature aerobic fermentation after the drying anaerobic fermentation, regulating the water content of the fermented biogas residue to reach the range capable of conducting high temperature aerobic fermentation, conducting high temperature aerobic fermentation.    DESCRIPTION OF DRAWING(S) - The figure shows a view of solid organic waste process method to process.
NOVELTY - The regulator has discharge port (23) with water inlet that is connected to exhaust valve (6). A pressure regulating valves (5) are set between exhaust valve and the water inlet pipe (24). The pressure regulating valve is connected with gas outlet port of the air pipe (4). The bottom of gas-water separator (1) is connected with the bottom of the positive and negative pressure protector (2) by a one-way valve (7). The distance of water level between pressure regulating valves and exhaust valve is equal to the height of the pressure water level line.    USE - Multifunctional automatic regulator.    ADVANTAGE - The design of the regulator can be improved. The energy saving effect of the regulator can be improved. The automatic gas can be discharged effectively. The synchronous biogas leakage can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional automatic regulator. (Drawing includes non-English language text)    Gas-water separator (1)    Positive and negative pressure protector (2)    Air pipe (4)    Pressure regulating valves (5)    Exhaust valve (6)    One-way valve (7)    Discharge port (23)    Water inlet pipe (24)
NOVELTY - Using nitrogen containing fertilizers recovered from contaminated water for feeding plants and algae, comprises: (a) collecting contaminated waters with nitrogen waste; (b) decontamination processing of the contaminated waters using ion exchange, where the decontamination process produces a nitrogen waste brine having increased concentration of nitrogen waste and a decontaminated water with decreased concentration of nitrogen waste; (c) processing of nitrogen waste brine to produce a nitrogen feed mixture; and/or (d) applying the nitrogen feed mixture into a plant or algae crop as nutrients.    USE - The method is useful for using nitrogen containing fertilizers recovered from contaminated water for feeding plants and algae. No biological data given.    ADVANTAGE - The method is: cost effective; and able to clean existing water for safe drinking, reduce contamination of other waters through mixing, and reduce air contamination.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of using nitrogen containing fertilizers recovered from contaminated water for feeding plants and algae, where even minute amounts are removed so nitrates and nitrites are removed from contaminated water using anion exchange.
NOVELTY - Renewable distillate composition comprises a petroleum derived distillate range stream (5-99 wt.%), a bio-distillate fraction (0.5 wt.%), and a stabilizing additive having surfactant properties (0.5-25 wt.%).    USE - The renewable distillate composition is useful as a feedstock to produce biofuels and/or specialty chemicals.    ADVANTAGE - The renewable distillate composition is capable of producing biofuels in an economical and environmentally friendly manner.
NOVELTY - The system has feed port that supplies biomass material. The processing unit removes the tar delivered to the half carbonizing machine and carbon gas generated in the half carbonizing machine. The molding unit molds the solid portion to the half carbonizing machine of the processing unit. The dust collector collects the biomass dried in the dryer.    USE - Biomass solid portion manufacturing system.    ADVANTAGE - The tar of the half charring process can be removed effectively, the investment cost is reduced, the quality of the biomass solid portion is improved and cracking gas generated in the half charring process of the biomass is produced in an environment friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass solid portion manufacturing method.
NOVELTY - Biomass containing nitrogen is decomposed using pressurized hot water to form a decomposition product containing hot water component including ammonia, and fuel gas. Strong alkali is added to the decomposition product such that ammonia contained in the hot water component is gasified and a gas-liquid mixture is formed. The gas-liquid mixture containing gasified ammonia, fuel gas and liquid component is subjected to separation process and ammonia gas is removed from the mixture.    USE - Removal of ammonia from waste liquid.    ADVANTAGE - The method economically removes ammonia from waste liquid by a simple process and using a simple installation, and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ammonia removal equipment, which consists of ammonia gasifying portion and separation portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass gasification system. (Drawing includes non-English language text)    Biomass gasification system (1)    Biomass decomposition portion (10)    Gas-liquid separator (30)    Gas holder (40)    Stirrer (110)    Feed pump (120)
NOVELTY - A hydrogen generator (1) comprises modification part (2) which generates reformed gas which makes raw material and water react and contains hydrogen, carbon monoxide reduction part (3) which accommodates carbon monoxide reduction catalyst for reducing carbon monoxide in reformed gas, heating part which heats modification part and carbon monoxide reduction part, gas flow path (10) which one end connects with carbon monoxide reduction part and the other end connects with modification part, and space (11) which is arranged downward to the gravitational direction of carbon monoxide reduction part.    USE - Hydrogen generator for supplying fuel gas to fuel cell.    ADVANTAGE - Production of the gas temperature shift which reaches the carbon monoxide reduction part is suppressed.    DETAILED DESCRIPTION - A hydrogen generator (1) comprises modification part (2) which generates reformed gas which makes raw material and water react and contains hydrogen, carbon monoxide reduction part (3) which accommodates carbon monoxide reduction catalyst for reducing carbon monoxide in reformed gas, heating part which heats modification part and carbon monoxide reduction part, gas flow path (10) which one end connects with carbon monoxide reduction part and the other end connects with modification part, and space (11) which is arranged downward to the gravitational direction of carbon monoxide reduction part, and connects the end and carbon monoxide reduction part of gas flow path. The recessed part opened to gravitational direction upward is formed in the space.    DESCRIPTION OF DRAWING(S) - The drawing shows a principal part sectional view of the hydrogen generator. (Drawing includes non-English language text).    Hydrogen generator (1)    Modification part (2)    Carbon monoxide reduction part (3)    Gas flow path (10)    Space (11)
NOVELTY - A desulfurizer has cylindrical container (1) which forms a fuel channel, and desulfurizing agent layer (2) with desulfurizing agent. The fuel channel is filled with desulfurizing agent. The container has two or more fuel inlets (3a,4a,5a) whose positions are varied along flow direction of the fuel channel.    USE - Desulfurizer is used for hydrogen-producing apparatus for fuel cell system.    ADVANTAGE - The desulfurizer has excellent durability. The desulfurizing agent in the desulfurizer is efficiently used.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal cross-sectional view of the desulfurizer.    Cylindrical container (1)    Desulfurizing agent layer (2)    Fuel inlet tubes (3,4,5)    Fuel inlets (3a,4a,5a)    Fuel outlet (6)
NOVELTY - The present invention relates to a manufacturing process for plant fuel with high combustion efficiency, which recycles plant waste to make green eco-friendly fuel and includes the following steps: A. drying process: pre-drying a plurality of plant wastes to contain an average water content of 0.1% to 3%; B. pulverizing and even mixing said dried plant wastes to form a plurality of powder particles; C. surface carbonization/molding: compression molding said plant waste powder to be a block and then sintering at 200 DEG C to 400 DEG C to carbonize the surface of the block to form a blocked fuel.
NOVELTY - Hydroconversion of biomass comprising lignocellulosic biomass and/or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose or lignin to produce fuel bases comprises: (a) preparing a suspension of biomass particles in a solvent; (b) hydroconversion of the suspension in the presence of hydrogen in at least one reactor (9) containing a slurry of catalyst and optionally a solid additive; (c) separating the effluent from step (b), where the biomass is subjected to a pretreatment comprising a roasting step prior to the preparation of the suspension.    USE - The process is useful for hydroconversion of biomass comprising lignocellulosic biomass and/or one or more components of lignocellulosic biomass comprising cellulose, hemicellulose or lignin to produce fuel bases.    ADVANTAGE - The process provides higher conversion rates compared to process not including the roasting step, while maintaining an excellent rate of deoxygenation. The hydroconversion is easier as the water content of the biomass is low. The roasted biomass is hydrophobic, and remains dry and is insensitive with the humidity of the atmosphere. The roasting step causes chemical changes with the structure of the biomass, i.e. the biomass loses its mechanical resistance and elasticity, so that it is much easier to crush. The crushing step is facilitated by the roasting step and makes it possible to reduce energy consumption compared to a crushing without preliminary roasting. The process provides liquid products of good quality at low treatment and production cost.    DESCRIPTION OF DRAWING(S) - The figure shows the schematic view of the process for hydroconversion of biomass.    Roasted biomass (1)    Crusher (2)    Chamber for forming suspension (3)    Oven (4)    Hydroconversion reactor containing a slurry of catalyst. (9)
NOVELTY - Large and medium-sized multi-cavity combined biogas anaerobic fermentation device comprises a multiple of fermentation tanks, which are adjacently arranged to form a multi-cavity anaerobic fermentation tank, and a discharging device. The fermentation tanks are provided with an equal diameter opening A. The opening A is provided with a sealing pipe. The top of the adjacent cavity of the fermentation tanks are provided with a gas-guide pipe A. The bottom of the fermentation tank cavity is provided with a mud pipe A. The mud pipe A at the bottom of tank is provided with a mud pipe outlet.    USE - Used as a large and medium-sized multi-cavity combined biogas anaerobic fermentation device.    ADVANTAGE - The device improves the fermentation efficiency, chooses the number of the fermenter cavity according to the size of the amount of biogas projects to achieve the adjustment of the total volume of size; and achieves the classification interception, a solid retention period and microbial retention period greater than the hydraulic retention period.
NOVELTY - Preparing a metal oxide catalyst support (I), comprises: preparing a two aqueous solutions one with urea and a metal salt and the other with poly(ethylene glycol)-block-poly(propylene glycol)-block poly(ethylene glycol); correcting pH until solubilization of the mixture; heating the mixture (hydrothermal treatment) to obtain a precipitate; and drying and calcination the precipitate to obtain the metal oxide support with surface area superior to 80 m2.g-1.    USE - The method is useful for preparing: the metal oxide catalyst support, which is used in methanol steam reforming at temperatures of above 160 degrees C (preferably 180-220 degrees C), in dimethyl ether steam reforming and in water-gas shift reaction; the composite catalyst used in cell or fuel cell which is a high temperature polymer electrolyte membrane fuel cell (HT-PEMFC) type (all claimed); and synthesizing metal oxide supports comprising zinc oxide.    ADVANTAGE - The method: provides metal oxide catalyst support in cost-effective manner; utilizes copper based catalyst that improves thermal stability, when operated at lower temperatures; controls morphology of the metal oxide support; and utilizes promoter that suppress carbon monoxide production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing (II) a metal oxide catalyst support, comprising incorporating metal active particles of catalyst in the metal oxide catalyst support;    (2) composite catalyst of the metal oxide support, comprising metal or a combination of nanoparticulated metals, metal oxide support, where the metal or nanoparticulated metals are deposited and the support; and    (3) the composite catalyst and the support are obtained by the method.
NOVELTY - Compost groove comprises a bottom plane, which is provided with multiple parallel grooves. Each groove is respectively arranged with a through-hole air distributing pipe and a gas distribution pipe. The coated gravel is filled in each groove cavity. The paving stone is laid on a cast iron grate. The upper cover of the cast iron grate and the groove bottom are plane.    USE - Used as a compost groove.    ADVANTAGE - The compost groove realizes uniform distribution; and does not cause material leakage, and simultaneously satisfies the loading mechanism in the sludge compost tank for feeding and discharging operations.
NOVELTY - Gas distribution plate comprises a gas distribution panel, a cover plate, an additional air distribution pipe and a main pipe. The multiple inverted U-shaped long strips are located at the bottom of a fermentation tank of the gas distribution panel. The top surface of the gas distribution panel is provided with a hole. An air passage is formed between the gas distribution panels. The air passage is covered with cover plate, and the multiple additional air distribution pipes passing through the bottom of the fermentation tank are connected with the air passage.    USE - Used as a gas distribution plate.    ADVANTAGE - The plate ensures uniform distribution and at the same time meets the request of vehicle access (in and out).
NOVELTY - A positive and negative pressure air distributing device comprises a distribution automatic control system, fermentation tanks, and air gathering pipe connected with fan, pipe fitting and valve. The air gathering pipe is composed of valve inlet and valve outlet. When the temperature is lower than or equal to the preset temperature, the air in the air collecting pipe is in a positive pressure mode for blowing oxygen to the fermenting groove. When the temperature in fermenting groove is higher than preset temperature, the fan oxygen supply has negative pressure from suction in the fermenter.    USE - Positive and negative pressure air distributing device for compost engineering.    ADVANTAGE - The device can adjust the negative pressure and positive pressure of air distribution switch at gas distribution states.
NOVELTY - The apparatus has a stirred tank (10) that is provided with an opened and closed vent (11) in lower portion. The operation of heat line and drive motor (12) are controlled by a control panel (15). A temperature sensor (60) is provided to detect the temperature of disposable edible oil within the stirred tank. A first pipe (20) is extended from the vent of the stirred tank. An oil pump (40) is provided to inhale the disposable edible oil passing through filter assembly (30) which filters and discharges disposable edible oil from a second pipe (50).    USE - Apparatus for manufacturing environment-friendly diesel using waste edible oil.    ADVANTAGE - The high-quality diesel can be safely obtained by using waste edible oil. The production efficiency of the biodiesel can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the environment-friendly diesel manufacturing device.    Stirred tank (10)    Opened and closed vent (11)    Drive motor (12)    Control panel (15)    First pipe (20)    Filter assembly (30)    Oil pump (40)    Second pipe (50)    Temperature sensor (60)
NOVELTY - Anaerobic treatment system comprises a catering waste pre-processing part comprising a food waste tank, a material conveyor, a crushing-separating device, a slurry tank and a slurry lifting pump; and an anaerobic digestion part comprising a sludge feeding pipe, a waste feeding tube, an anaerobic digestion device, a stirrer, a gas storage device, a sludge feeding pipe and a food waste feeding tube. A catering waste storage tank outlet is connected to the material conveyor. A discharging port of the material conveyor is connected to a feeding port of the crushing-separating device.    USE - The system is useful for treating catering waste mixed with organic sludge.    ADVANTAGE - The system is facilitated with continuous online processing of wastes; can process large amount of wastes; comprising the crushing-separating device ensures the working efficiency of the system, and improves the recovery rate of organic matter, and material conveying capacity; and transports the material liquid to undergo digestion reaction in a tank body.
NOVELTY - Fresh bamboo shoot shell bio-gasification centralized gas supply system comprises a fermentation tank connected with fermentation room, an anaerobic fermentation tank to produce biogas by anaerobic microbial decomposition, and a biogas slurry storage pool for storing the storage biogas slurry. The biogas slurry storage tank and the fermentation tank are connected through a circulating reflux pipe. The reflux pipe is provided with a reflowing pump. The anaerobic fermentation tank is provided with a gas pipeline for output.    USE - Used as a fresh bamboo shoot shell bio-gasification centralized gas supply system.    ADVANTAGE - The system recycles waste and is environmental friendly.
NOVELTY - Processing cattle excrement involving taking out the natural cattle excrement; stacking the excrement in a cattle excrement stacking field and finishing it into a conical shape; covering the cattle excrement to ferment, where the moisture content of cattle excrement is 26-80%, the cattle excrement stack field is provided with a rain-proof shed; performing fermentation at night temperature of not less than 8 degrees C for 3-10 days; and after fermentation, directly classifying into a pile, placing vent pipes in the pile at an interval of 1-20 m of width and height for drying.    USE - For processing cattle excrement (claimed) for obtaining biological energy.    ADVANTAGE - The method provides harmless and energy-oriented use; avoids pollution to the environment; does not need to adopt a processing device such as a solid-liquid separator; does not generate peculiar smell; and processes excrement produces small ash after burning that return to farmland, thus which almost has no emission.
NOVELTY - The bed has a side bed plate (3) fixed on two ends of a transverse support (8). The transverse support is provided with two strip-shaped boards. A gap is formed between the strip-shaped boards. A breeding bed (10) is fixed with a fence (2) and provided with a sheep head extending hole (12). A fermentation bed (7) is arranged on the breeding bed. The fence is provided with a feeding trough hole (11) and a water tank (15). A fermentation bed bottom plate (16) is movably connected with a baffle plate (4). The fermentation bed bottom plate is made of concrete material.    USE - Sheep healthy cultivation double-layer bed.    ADVANTAGE - The bed can carry out harmless treatment for sheep excrement so as to provide better living environment, thus ensuring better health protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a sheep healthy cultivation double-layer bed operating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a sheep healthy cultivation double-layer bed in partial section.    Fence (2)    Side bed plate (3)    Baffle plate (4)    Fermentation bed (7)    Transverse support (8)    Breeding bed (10)    Feeding trough hole (11)    Sheep head extending hole (12)    Water tank (15)    Fermentation bed bottom plate (16)
NOVELTY - Composting herb trash rapid organic waste comprises cutting and crushing grass, adding effective microorganisms (EM) composite microbial inoculum into the crushed grass and then mixing uniformly, carrying out high temperature aerobic fermentation process to the crushed grass using a fermentation device for stacking, manually turning the temperature to 50-80 degrees C, and maintaining the temperature for 8 days and reducing the carbon/nitrogen ratio to less than 20.    USE - The method is useful for composting grass organic waste.    ADVANTAGE - The method is capable of rapidly composting the grass organic waste with high quality and improved nitrogen content in an environmentally friendly manner.
NOVELTY - Process (P1) for enzymatic refining of pretreated cellulosic material, involves (a) contacting pretreated cellulosic material with one or more esterase enzymes to form refined pretreated cellulosic material, or (b) (i) processing pretreated cellulosic material to form solid/liquid mixture of pretreated cellulosic material, (ii) separating liquor from the solid/liquid mixture of pretreated cellulosic material, and (iii) treating the liquor with feruloyl esterase.    USE - The process (P1) is useful for enzymatic refining of pretreated cellulosic material that is used in saccharification process. The process (P3) is useful for producing fermentation product including alcohol, ketone, amino acid, alkane, alkene, protein and gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process (P2) for hydrolyzing pretreated cellulosic material, involves saccharifying pretreated cellulosic material treated and refined with the esterase enzyme composition;    (2) process (P3) for producing fermentation product, involves (a) saccharifying pretreated cellulosic material with enzyme composition, where the pretreated cellulosic material is contacted or treated with esterase, (b) fermenting the saccharified pretreated cellulosic material with one or more fermenting microorganisms to produce fermentation product, and (c) recovering the fermentation product; and    (3) process (P4) for fermenting pretreated cellulosic material, involves fermenting pretreated cellulosic material with one or more fermenting microorganisms, where the pretreated cellulosic material is treated, refined, and/or saccharified.
NOVELTY - The container has temperature regulation device that is provided with heat exchanger mounted in tank casing (19). The regulation device is connected to inlet (14) and outlet of heat conducting working medium. The bottom surface of heat exchanger is connected to cooling water discharging pipe which extends out of the tank casing. A fermentation liquor output valve (11) and fermentation liquor sampling valve (6) are arranged on inclined surface (7) of tank casing. An upper portion of tank (20) is provided with liquid level alarming device and chemical sterilizing nozzle.    USE - Straw juice fermentation container.    ADVANTAGE - The fermentation temperature condition and product weight can be ensured. The container is convenient to operate and use. The straw juice production efficiency of the container is improved. The cleaning efficiency of the container is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw juice fermentation container.    Fermentation liquor sampling valve (6)    Inclined surface of tank casing (7)    Fermentation liquor output valve (11)    Inlet of heat conducting working medium (14)    Tank casing (19)    Tank (20)
NOVELTY - A lignin-containing component contains lignin and thermoplastic resin. The lignin is bonded with the thermoplastic resin.    USE - Lignin-containing component is used for soil improvement (claimed).    ADVANTAGE - The lignin-containing component is economically manufactured, and efficiently reduces cadmium concentration in soil. Since lignin-containing component filled up on soil can be easily removed after cadmium component adsorption and removal of surrounding soil is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for soil improvement, which involves filling the lignin containing component on the soil surface.
NOVELTY - Composition comprises gas supersaturated water.    USE - The composition is useful for delivering drug into cell including human and non-human cells (claimed). The drug is peptide, antibody, gene, oligonucleotide, antisense oligonucleotide, small interfering RNA (siRNA), viral vector, plasmid or low molecular weight compound, where the gene is inserted into plasmid or viral vector.    ADVANTAGE - The composition produces microbubbles that is stable for a long period of time and can be easily delivered into a cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for manufacturing gas supersaturated water, involves (a) pumping liquid, (b) injecting gas into the pumped liquid, (c) pressurizing the liquid in which gas is injected and dissolving the gas, and (d) reducing the pressure to atmospheric pressure and pumping the liquid in which the gas dissolved;    (2) method (M2) for delivering drug into a cell in in vitro, involves dissolving drug in aqueous solution comprising gas supersaturated water, contacting cell with the above solution, and physically stimulating the cell; and    (3) method (M3) for delivering drug into non-human cell or human cell in in vivo, involves performing the above method (M2).
NOVELTY - A soil stabilizer is mixed with sludge to solidify the sludge. The soil stabilizer is PX300. The sludge is sewage sludge, sewage sludge dehydrated cake, underground water tank sludge or dredged soil.    USE - Solidification of sludge used for forming solid material used as construction material and solid fuel (all claimed).
NOVELTY - Preparing 1,4-bis(chlorodifluoromethyl)benzene comprises adding trichloro-methyl benzene with a catalyst.    USE - The 1,4-bis(chlorodifluoromethyl)benzene is useful in agricultural chemical and pharmaceutical field.    ADVANTAGE - The process is cost-effective and eco-friendly for preparing 1,4-bis(chlorodifluoromethyl)benzene.
NOVELTY - Preparing Cinchona series alkaloids comprises: using Cinchona bark as a raw material; and applying advanced and highly-efficient extraction, separation and purification technology.    USE - The Cinchona series alkaloids are useful for industrial mass production of good manufacturing practice (GMP) level crude drugs and food additives.    ADVANTAGE - The method: ensures higher extract recovery rate and low carbon process flow, and is ecofriendly as compared to that of existing methods; has simple preparation; and produces highly pure (99.5%) Cinchona alkaloids.
NOVELTY - The method involves connecting a disk-flow disintegrator (2) to a filter (3). Speed of a two-shaft mixer (4) is controlled at targeted shaft speed. The two-shaft mixer is connected to a molding machine (5) and a cutting device (6). The molding machine and the cutting device are combined with a hybrid drum granulator (7). Microwave generators (9), a separation chamber (10) and a biofuels container (11) are arranged with each other. A fan (12) and a particulate filter (13) are utilized for sanitizing a column (14) with a circulating pump (15) and a flow-through static mixer (16).    USE - Method for production of biofuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for production of biofuels.    Disk-flow disintegrator (2)    Filter (3)    Two-shaft mixer (4)    Molding machine (5)    Cutting device (6)    Hybrid drum granulator (7)    Microwave generators (9)    Separation chamber (10)    Biofuels container (11)    Fan (12)    Particulate filter (13)    Column (14)    Circulating pump (15)    Flow-through static mixer (16)
NOVELTY - Annealing organic waste to humus compost, comprises: (a) finely chopping organic waste matters collected from domestic waste/green waste; (b) mixing the obtained material obtained with a starter as ripened humus compost; (c) piling the obtained material into beds; (d) hot-annealing the obtained beds using strains comprising e.g. Aspergillus terreus DSM 5770 and maintaining the temperature, the humidity and pH of the annealed beds; (e) cool-annealing the obtained material and maintaining the humidity of the annealed beds; and (f) obtaining ripened compost.    USE - The process is useful for annealing organic waste to humus compost (claimed), where the humus compost is useful for the cultivation.    DETAILED DESCRIPTION - Annealing organic waste to humus compost, comprises: (a) finely chopping organic waste matters collected from domestic waste or green waste to a maximum size of 400 mm; (b) mixing the material obtained in step (a) with a starter as ripened humus compost; (c) piling the material obtained in step (b) into beds in triangle cross section with the height and base width depending on the size of material, as given in the specification; (d) hot-annealing the beds obtained in step (c) for a period of 2-3 weeks using groups of strains of organisms consisting of Aspergillus terreus DSM 5770 , Aspergillus niger DSM 11167, Trichoderma viride DSM 63065, Trichoderma reesei QM 9414, Gloeophyllum sepiarium DSM 6420, Phanerochaete chrysosporium DSM 1556, Cellulomonas uda DSM 20108, or Streptomyces cellulosae DSM 40362 and maintaining the temperature of the annealed beds of 50-65 degrees C, the humidity of 35-45% and pH of 6-7.5 by mixing, air-blowing and watering; (e) cool-annealing the material obtained in step (d) for a period of 3-6 weeks further using bacterium strain of Bacillus subtilis FZB-24 and maintaining the humidity of the annealed beds of 30-35%; and (f) obtaining ripened compost as the product.
NOVELTY - The system has a fuming device provided with a combustion chamber (5), where a top part of the combustion chamber is provided with a feeding device. A bottom part of the combustion chamber is provided with a discharging device. A firing device (11) and an air blowing device (10) are connected to an air inlet (9). The combustion chamber is equipped with grooves. A smoke outlet pipe (17) passes through a flue gas component detecting device (18). An automatic control system is connected with the feeding device, the discharging device, the firing device and the flue gas component detecting device.    USE - Sawdust and crop straw rubbish fuel smoke gasification processing system.    ADVANTAGE - The system is convenient to operate, and has high combustion efficiency, high production efficiency and better economic and social benefits, and protects environment from being polluted while processing organic waste. The system converts solid organic waste into combustible gas and realizes full automatic control effect.
NOVELTY - Wastewater having pH is adjusted to alkalescence, and then organic amine is added in organic solvent to extract water by sodium hydroxide aqueous solution and organic phase, to obtain chiral amine crude product. The obtained product is decompressed and recycle solvent is concentrated using organic solvent to wash and recrystallized, to obtain chiral amine.    USE - Recycling of chiral amine.    ADVANTAGE - The chiral amine is economically and efficiently recycled with high recycling rate, by a simple method.
NOVELTY - The reformer has a reaction chamber provided with an internal space. Air supplying part (120) sprays air to the internal space of the reaction chamber. A vent is provided with synthetic gas. A high voltage supplier supplies voltage to the reaction chamber. A fuel supplying hole (141) supplies hydrocarbon fuel to inside of a ground electrode (130) that is fixed in the internal space. A secession preventing projection part (132) blocks secession of the hydrocarbon fuel supplied in both parts of the vent.    USE - Plasma fuel reformer for use in a vehicle such as passenger car, bus, lorry and ship.    ADVANTAGE - The reformer enhances production rate of hydrogen combined with nitrogen oxide by utilizing hydrocarbon fuel supplied with air during reformate reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a plasma fuel reformer.    Air supplying part (120)    Ground electrode (130)    Secession preventing projection part (132)    Fuel supplying hole (141)    Body part (142)
NOVELTY - Robotic algae harvest comprises transporting collected carbon dioxide (CO2) to an algae broth location, the algae broth location being an ocean going platform, and a set of floating interconnecting photobioreactors creating the ocean going platform; and continuously feeding and re-circulating the algae broth through photobioreactors.    USE - The method is used for robotic algae harvest (claimed).    ADVANTAGE - An economically and environmentally sustainable system and method for the production of algae for bio-fuel use or production of biomass material to be used as fuel, including but not limited to, ethanol, are provided. The method above produces multiple products and generates multiple sources of income from: biodiesel; ethanol; carbon credits; tax subsidies; and dry algae briquettes. The method does not require significant changes to the current infrastructure, does not require large landmasses, and each individual technology is currently available. The use of algae will not have adverse effects on food prices, nor result in a 'bio-fuel carbon debt' unlike bio-fuels products based on food products.    DETAILED DESCRIPTION - Robotic algae harvest comprises transporting collected carbon dioxide (CO2) to an algae broth location, the algae broth location being an ocean going platform, and a set of floating interconnecting photobioreactors creating the ocean going platform; continuously feeding and re-circulating the algae broth through photobioreactors; suspending the photobioreactors and the algae broth in the ocean; transforming the CO2 into biomass in a continuous process of photosynthesis; changing the buoyancy of the platform and photobioreactors using the CO2 available; extracting algae; transferring the extracted algae using wave energy; and preprocessing the extracted algae into a stable mix of oil and one or more by-products.
NOVELTY - Converting a solid biomass material (102), comprises contacting the solid biomass material with a catalytic cracking catalyst (108) at more than 400 degrees C in a riser reactor to produce at least one cracked products, where the riser reactor is an external riser reactor (107) with a curve and/or low velocity zone at its termination, and a part of the catalytic cracking catalyst has deposited in the curve and/or low velocity zone.    USE - The process is useful for converting a solid biomass material to produce cracked products, which is useful for preparing a biofuel and/or a biochemical (all claimed).    ADVANTAGE - The process: utilizes the external riser reactor, which reduces the risk of erosion, thus increasing safety and hardware integrity, and operates for a longer period; allows for easier feeding of the solid biomass material to the riser reactor, thus increase the conversion of the solid biomass material; and allows for a longer residence time for the solid biomass material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of converting the solid biomass material.    Solid biomass material (102)    Bottom section (106)    External riser reactor (107)    Catalytic cracking catalyst (108)    Fluid hydrocarbon feed (110)
NOVELTY - The system has a biomass gasification furnace and a focus follower that are connected with a gas outlet of a dust removing device. A gas outlet of the biomass gasification furnace is connected with a gas burner.    USE - Biomass combined cool, heat and power supply system.
NOVELTY - Sewage treatment apparatus (1) comprises a pre-processing tank (B), an aerobic-treatment tank which carries out the aerobic treatment of the to-be-processed water, a carrier filtration tank (E) which filters the to-be-processed water by which the aerobic treatment is carried out, a transfer control unit (22) by which the to-be-processed water in the pre-processing tank is transferred to the aerobic-treatment tank and that controls the amount of transfers, a sewage treatment unit, and a sludge storage tank (I).    USE - As sewage treatment apparatus.    ADVANTAGE - The sewage treatment apparatus can reduce the load of carrier filtration tank by simple structure, and can be installed in small sized, medium sized or large sized purification tank.    DETAILED DESCRIPTION - Sewage treatment apparatus (1) comprises a pre-processing tank (B) which performs solid-liquid separation and biological treatment of to-be-processed water, an aerobic-treatment tank which carries out the aerobic treatment of the to-be-processed water, a carrier filtration tank (E) which filters the to-be-processed water by which the aerobic treatment is carried out, a transfer control unit (22) by which the to-be-processed water in the pre-processing tank is transferred to the aerobic-treatment tank and that controls the amount of transfers, a sewage treatment unit, and a sludge storage tank (I) which can store sludge in the adjacently arranged aerobic-treatment tank and connects with the aerobic-treatment tank in the upper portion.    DESCRIPTION OF DRAWING(S) - The drawing shows vertical side view of sewage treatment apparatus. (Drawing includes non-English language text)    Sewage treatment apparatus (1)    Transfer control unit (22)    Pre-processing tank (B)    Carrier filtration tank (E)    Sludge storage tank (I)
NOVELTY - Producing charcoal from olive kernels, comprises: producing a kernel powder by the incomplete combustion of limestone with kernel wood; after drying the kernel powder in a dryer, firstly mixing kernel powder with starch and then with hot water, so that a mixture is obtained; conveying the mixture to a press to acquire the shape of a briquette; and drying the mixture in a dryer of the closed air circuit type, to form the final product.    USE - The method is useful for producing charcoal from olive kernels (claimed), where the charcoal is useful in domestic or industrial applications.    ADVANTAGE - The method provides kernel charcoal with high heating value, which constitutes alternative and ecological fuel, ideal for domestic or industrial applications. The method is cost-effective for producing kernel charcoal.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of process for producing kernel charcoal from kernel wood as raw material and intermediate products.
NOVELTY - Thermal utilization of mixture of dried sewage sediment originated from dried sewage sediments and biomass by/through gassing of the mixture of renewable fuel and dried sewage sediment (1-50 mass%) and wood wastes (1-50 mass%), straw (1-50 mass%), willow Salix viminalis (1-50 mass%), and willow of Pennsylvanian mallow Althaea (1-50 mass%), is claimed.    USE - The method is useful for the thermal utilization of mixture of dried sewage sediment originated from dried sewage sediments and biomass, preferably for the ecological usage of solar energy contained in plants in the process of coal accumulation in tissues.    ADVANTAGE - The gasification allows more efficient utilization of a great range of wastes leading to the reduction of the waste mass in the scale of 70-80%, than in the case of classic burning.
NOVELTY - Producing pretreated biomass, involves: applying a treatment method to biomass to produce a pretreated biomass composition, where the pretreated biomass composition comprises a pretreatment liquor and pretreated biomass solids; densifying the pretreated biomass solids to a solids content of 20-90% by removing liquid; adding at least one hydrolysis enzymes to the pretreated biomass solids to form an enzyme-treated biomass; and storing the enzyme-treated biomass.    USE - For producing pretreated biomass for producing sugars (claimed), bioproduct and biofuel.    ADVANTAGE - The method makes it possible to store or transport pretreated biomass that has been somewhat densified by partial dewatering, and has had enzymes applied in a way that can reduce or eliminate the requirement to add enzymes prior to a final conversion process. The method allows: the coexistence of the pretreated lignocellulosic biomass and the hydrolytic cellulase enzymes during storage and transportation; the combination of a partial hydrolysis of the pretreated lignocellulosic biomass at a higher density during storage and a more complete hydrolysis upon its dilution to a lower density without further enzyme addition after storage; the immediate hydrolysis of the pretreated lignocellulosic biomass to produce sugars, without further addition of enzymes, in a biofuel or bioproduct production site; the enhancement of the final hydrolytic activity of the pretreated lignocellulosic biomass; and the reduction in sensitivity of the inhibitors in the pretreated lignocellulosic biomass.
NOVELTY - The method involves permitting negative ionization of atoms or molecules to enter field or apertures of substance, and controlling insertion of electrons into an atom or molecule for production of greater negative ions. Simultaneous production of positive and negative ions is controlled. Multiple constituent atoms to be extracted from selected molecules are controlled. Larger molecules to be selectively decomposed into smaller molecules are controlled. Complete decomposition of selected molecules is controlled. The composition of selected molecules is controlled.    USE - Method for selectively extracting electrons from atoms/molecules and/or selectively inserting electrons into atoms/molecules and/ or partial/complete decomposing of molecules e.g. carbon dioxide molecule and carbon monoxide molecule, and composition of molecules in different fields. Uses include but are not limited to molecular decomposition of virus, bacteria, pollen, mold, mildew, fungus, plankton and cell and treatment of tumors, cancers and maladies in medical field, scientific field, commercial field and industrial field.    ADVANTAGE - The method enables facilitating deliberate extraction of electrons from atoms and molecules to form positive ions. The method enables extracting and capturing electrons, producing positive ions and selectively decomposing molecules or constructing molecules in an energy efficient manner. The method enables speeding up the operation process and requiring only small maintenance energy to sustain the operation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of an extraction unit, a positive field plate with a collector, an attached ion diverter and control units coupled with a complex multipart grid group extraction unit.    Power source (20)    Negative field plate (22)    Valves (28, 36)    Charge collector (34)    Field plate monitor and control unit (40)
NOVELTY - A hydrogen-generating agent comprises 100 parts weight of mixed powder containing zeolite powder containing aluminum, silicon and/or alkali metal, and calcium compound powder, 0.1 part weight or more of active charcoal powder having specific surface area of 1000 m2/g or more, and beta -iron silicide. The hydrogen-generating agent generates hydrogen, when immersed in water.    USE - Agent is used for manufacturing hydrogen (claimed) used in chemosynthesis of ammonia and methanol, and in petroleum refining field.    ADVANTAGE - The agent efficiently and economically provides hydrogen with high yield without burning fossil fuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen, which involves immersing hydrogen-generating agent in water; and    (2) hydrogen-generating apparatus.
NOVELTY - The method uses electrolysis to transform electric energy into chemical energy and internal gas energy of hydrogen and oxygen mixture. The high pressure gas formed is supplied for storage to a high pressure gas tank. The stored energy is used employing and unit comprising a CPU, gas tanks, a feed system, a capacitor, a liquid storage tank, a pump, liquid valves and an engine. The engine uses the high pressure hydrogen and oxygen gas mixture for conversion into power. The engine working cycle consists of two strokes: piston movement from top dead center to the bottom dead centre and back. The engine has a heat connection with the capacitor and the feed system.    USE - For storing electric energy using electrolysis for transforming electric energy into chemical energy and internal energy of hydrogen and oxygen mixture    ADVANTAGE - The closed working cycle has a high efficiency rate and minimum harmful emissions.
NOVELTY - The system (10) has a tank (12) including an internal chamber (16) for containing food waste and sufficient water for fully submersing the waste. A filtration and discharge system (700) filters and discharges the water and the waste from the chamber. A grinder system (500) is positioned in the chamber and adapted to be fully submersed in the water for grinding the waste. A circulation system (600) is positioned in the chamber, and circulates the water and the food waste. A control system (800) controls operation of the system in accordance with a desired control process.    USE - System for managing food waste produced in a supermarket, a hospital and a restaurant.    ADVANTAGE - The system allows food waste to be dealt with onsite. The system draws the food waste that descends to the bottom of the interior chamber with the water into an inlet, grounds the waste into smaller pieces, and ejects the waste in an upward and outward direction under pressure through an outlet to circulate in the tank about a circulation axis, thus ensuring decomposition and reduction of biochemical oxygen demand (BOD) and suspended solid levels, and reduction of fats, oils and greases.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a food waste management system.    Food waste management system (10)    Tank (12)    Internal chamber (16)    Grinder system (500)    Circulation system (600)    Filtration and discharge system (700)    Control system (800)
NOVELTY - The fuel cell stack (100) has fuel anode chamber (20) that is provided with fuel injection pipe for supplying fuel to the micro cylindrical solid oxide fuel cells (10). A fixing unit is provided for fixing micro cylindrical solid oxide fuel cells. The air supplying unit is connected to the air electrode tube and air-injecting pipe for injecting air to the air supplying unit. The air electrode chamber (30) is fixed to the fuel anode chamber which is combined within the air electrode tube (31).    USE - Micro cylindrical solid oxide fuel cell stack for solid fuel oxide fuel cell generation system (claimed).    ADVANTAGE - The layout structure of the fuel anode chamber and air electrode chamber can be optimized. The damage of the fuel cells can be prevented. The heat loss of the fuel cells can be minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel oxide fuel cell generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of micro cylindrical solid oxide fuel cell stack.    Micro cylindrical solid oxide fuel cell (10)    Fuel anode chamber (20)    Air electrode chamber (30)    Air electrode tube (31)    Cylinder solid oxide fuel cell stack (100)
NOVELTY - Treatment of highly degradable solid organic waste such as food and plant material and waste, involves a heat treatment at 150-200 degrees C to cook and dry the waste, by the use of a mineral mix as a catalyst.    USE - For the treatment of highly degradable solid organic waste such as food and plant material and waste (claimed).    ADVANTAGE - The process for treating degradable organic matter, provides easily manageable, fast and complete process requiring a low environmental footprint. This process is more user friendly than other thermal processes and may be undertaken onsite (at the point of generation of waste) thus overcoming the issues of all treatment processes currently used in solid organic waste treatment. The process is preferably residue free (unlike other treatment processes which may require extensive processing to convert the residual final product to a useful product), meaning the final product is disposed into gardens for natural means of improving soil or used in composting facilities to improve the final compost quality. The finished product may serve in slowly improving the soil biota for a long term benefit thus eliminating pollution problems and putting carbon and nutrients from the original solid organic matter back into soil.
NOVELTY - Producing alcohols from cellulosic or lignocellulosic biomass, comprises: e.g. (a) thermochemically pretreating a cellulosic or lignocellulosic substrate; (b) optionally washing the pretreated substrate; (c) enzymatic hydrolyzing the pretreated substrate, optionally washing, implementing cellulolytic and/or hemicellulolytic enzyme, producing a hydrolyzate and insoluble residue in water; and (d) fermenting ethyl hexose content in the hydrolyzate.    USE - The method is useful for producing alcohols.    ADVANTAGE - The method provides alcohol with improved physical properties in an economical manner.    DETAILED DESCRIPTION - Producing alcohols from cellulosic or lignocellulosic biomass, comprises: (a) thermochemically pretreating a cellulosic or lignocellulosic substrate; (b) optionally washing the pretreated substrate and setting the pH; (c) enzymatic hydrolyzing the pretreated substrate, optionally washing, implementing cellulolytic and/or hemicellulolytic enzyme, producing a hydrolyzate and insoluble residue in water; (d) fermenting ethyl hexose content in the hydrolyzate from the step (c) in ethanol by an alcoholic microorganism and obtained ethyl hexose; (e) separating and purifying the alcohol from step (d) and separating a solid cake containing the insoluble residue and obtaining spent liquors; and (f) fermenting ethyl pentose content in at least one of the flows obtained in the previous steps by microorganism fermentation of pentoses and obtaining ethyl pentose, where at least one part of the ethyl pentose obtained in the step (f) is recycled upstream of at least one of enzymatic hydrolysis and/or alcoholic fermentation.
NOVELTY - Producing alcohols and/or solvents from cellulosic or lignocellulosic biomass, comprises: e.g. (a) thermochemically pretreating a cellulosic or lignocellulosic substrate; (b) optionally washing the pretreated substrate; (c) enzymatic hydrolyzing the pretreated substrate, optionally washing, implementing cellulolytic and/or hemicellulolytic enzyme producing a hydrolyzate and insoluble residue in water; and (d) fermenting ethyl hexose content in the hydrolyzate from the step (c) in ethanol by an alcoholic microorganism and obtaining ethyl hexose.    USE - The method is useful for producing alcohols.    ADVANTAGE - The method provides alcohol with improved physical properties in an economical manner.    DETAILED DESCRIPTION - Producing alcohols and/or solvents from cellulosic or lignocellulosic biomass, comprises: (a) thermochemically pretreating a cellulosic or lignocellulosic substrate; (b) optionally washing the pretreated substrate and setting the pH; (c) enzymatic hydrolyzing the pretreated substrate, optionally washing, implementing cellulolytic and/or hemicellulolytic enzyme, producing a hydrolyzate and insoluble residue in water; (d) fermenting ethyl hexose content in the hydrolyzate from the step (c) in ethanol by an alcoholic microorganism and obtaining ethyl hexose; (e) separating and purifying an ethanol and/or solvents from step (d) and separating a solid cake containing the insoluble residue and obtaining spent liquors; and (f) fermenting butyl pentose content in at least one of the flow obtained in the previous steps by solventogenic microorganism and obtaining butylic wine, where at least one part of the butylic pentose wine obtained in the step (f) is recycled upstream of at least one of enzymatic hydrolysis and/or ethanolic fermentation.
NOVELTY - Catalyst is formed by supporting platinum, iridium, and rhenium to titanium oxide support or tin oxide support.    USE - The catalyst is useful for carrying out oxidation removal of methane in to-be-processed gas containing methane and excess oxygen (claimed).    ADVANTAGE - The catalyst has excellent resistance to water vapor or sulfur compound, also in waste gas which contains water vapor in large quantities like combustion exhaust gas, and contains sulfur oxide, and exhibits high methane oxidation activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for carrying out the oxidation removal of methane in to-be-processed gas containing methane and excess oxygen, which involves contacting to-be-processed gas and the catalyst at the temperature of 300-450 degrees C.
NOVELTY - The method involves collecting the value of coefficient of variations at steady-state in chemical process. The average of value of coefficient of variations and standard deviation are stored. The value of coefficient of variations is normalized (8). The matrix pattern including confusion signal indicating the normalized value of coefficient of variations about the given time horizon in a graph is formed (9). The formed matrix pattern is compared (10) with matrix patterns stored in database.    USE - Control method of chemical process e.g. liquid natural gas (LNG) liquefaction process, power generation type fuel cell process, LNG evaporation and storage process (all claimed), for use in factory.    ADVANTAGE - The unusual condition of the matrix pattern is determined effectively and abnormal condition in the chemical process is reduced. The load of the factory can be saved and profit of the factory is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating control method of chemical process. (Drawing includes non-English language text)    Step for forming matrix pattern about unusual condition (7)    Step for normalizing value of coefficient of variations (8)    Step for forming matrix pattern including confusion signal indicating normalized value of coefficient of variations about the given time horizon in graph (9)    Step for comparing formed matrix pattern with matrix patterns stored in database (10)
NOVELTY - Anode electrode is obtained by electrodepositing chromium to titanium oxide electrode by carrying out cathodic polarization of titanium oxide electrode in aqueous solutions of chromium nitrate.    USE - The anode electrode is used in apparatus useful for visible light decomposition of water (all claimed).    ADVANTAGE - The anode electrode provides optical electric current by low bias of 0.6 V, and utilizes visible light of a long wavelength area of 590 nm or less.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for manufacturing anode electrode; and    (2) apparatus for visible light decomposition of water.
NOVELTY - Electrolyzer comprises a single cell or several single cells electrically connected in series or parallel manner. The single cell comprises cell components arranged to one another in concentric manner and comprises at least one inner electrode (1), an outer electrode (3) and at least one separation component (2). The inner electrode is electrically conductive and exhibits a defined form with openings, holes, perforations, a gas-permeable porous layer, or a surface structure. The outer electrode is constructed from an electrically conductive and the gas-permeable structure.    USE - The electrolyzer is useful for producing hydrogen and oxygen from electrochemical decomposition of water.    ADVANTAGE - The electrolyzer achieves the shortest paths for the current-carrying ions between the two electrodes, thus it allows a low inner resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the arrangement of a cell of the electrolyzer.    Inner electrode (1)    Separation component (2)    Outer electrode (3)    Rod-shaped electric conductor (6)    Outer electrical conductor (9)
NOVELTY - A polynucleotide encoding modified beta -glucosidase, is new. The beta -glucosidase is modified for enhancing its activity.    USE - The polynucleotide encoding modified beta -glucosidase for enhancing its activity, which is useful for producing bioethanol (claimed).    ADVANTAGE - The bioethanol can be produced at low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide comprising base sequence of SEQ ID NO: 9;    (2) expression vector comprising the polynucleotide;    (3) transformant transformed by the expression vector, which is introduced into host cell;    (4) method for producing the modified beta -glucosidase for its enhancing activity, involves cultivating transformant in culture medium and collecting the beta -glucosidase from culture substance; and    (5) method for producing bioethanol, involves cultivating transforman capable of producing bioethanol in culture medium, or cultivating host cell in substrate of beta -glucosidase.
NOVELTY - Treating organic materials to produce methane gas, comprises: (a) subjecting an organic feedstock comprising organic materials to a liquefaction process at subcritical conditions in at least one reaction stage, to obtain a mixture containing low molecular weight materials and optionally lignins; and (b) subjecting the obtained mixture containing low molecular weight materials and optionally lignins, to a methane fermentation process.    USE - The method is useful for treating organic materials to produce methane gas (claimed).    ADVANTAGE - The method efficiently increases the degradation of organic matter and achieves a high output of high value end products in a resource effective and thus economically favorable way.    DETAILED DESCRIPTION - Treating organic materials to produce methane gas, comprises: (a) subjecting an organic feedstock comprising organic materials to a liquefaction process at subcritical conditions in at least one reaction stage, to obtain a mixture containing low molecular weight materials and optionally lignins; and (b) subjecting the obtained mixture containing low molecular weight materials and optionally lignins, to a methane fermentation process; where the organic feedstock comprises liquid water and/or is combined with liquid water before and/or during the liquefaction, and the subcritical conditions for the at least one or more reaction stages in (a) is a temperature of 280-374 degrees C during a reaction time of less than 1 minute, and where if more than one reaction stage is used in step (a) the obtained mixture after each reaction stage is subjected to a separation of the produced low molecular weight materials from the remaining solid materials of the treated feedstock.
NOVELTY - A fuel cell includes fuel cell stack formed by stacking greater than or equal to 2 electric power generation cells which fuel and air are made to react and are generated; combustor which burns exhausted fuel and the air exhaust emitted from the fuel cell stack making it produce heat; and modifier which produces reformed fuel and supplies this reformed fuel to the fuel cell stack.    USE - A fuel cell.    ADVANTAGE - The fuel cell has improved reliability while avoiding enlargement of the whole fuel cell by providing the heating structure of heating the whole fuel cell stack uniformly.    DETAILED DESCRIPTION - Fuel cell comprises fuel cell stack formed by stacking greater than or equal to 2 electric power generation cells which fuel and air are made to react and are generated; combustor which burns exhausted fuel and the air exhaust emitted from the fuel cell stack making it produce heat; modifier which produces reformed fuel and supplies this reformed fuel to the fuel cell stack by carrying out steam reforming of the introduced fuel from the outside using the heat produced by the combustor; air preheater which heats the air introduced from the outside with the heat produced by the combustor, and supplies it to the fuel cell stack; and air temperature control mechanism which controls temperature of the air supplied to the fuel cell stack by adjusting a flow ratio with the flow volume of the air which reroutes the air preheater and is directly introduced into fuel cell stack. An INDEPENDENT CLAIM is included for operating the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of the fuel cell.
NOVELTY - A biogas treatment system comprises a deforming jar, an air voltage stabilizing cabinet, a biogas burner and a multi-section pipe. The deforming jar is connected with biogas voltage regulation cabinet. The air voltage stabilizing cabinet is connected with the biogas combustor, and leads to the biogas voltage regulation cabinet from the deforming jar of pipeline and is provided with a biogas flow meter.    USE - System for anaerobic treatment of biogas.    ADVANTAGE - The biogas flow meter is not only capable of detecting and monitoring the situation in the reactor, a reaction pot is also provided which helps control the characteristics of chemical oxygen demand load.
NOVELTY - An isolated nucleic acid comprising: (a) the nucleotide sequence of SEQ ID NO: 1, 2, or 3, a copy of the Sequence Listing is available in electronic form from the USPTO web site (http://seqdata.uspto.gov//pageRequest=docDetail DocIDUS20120258511A1); or (b) a nucleotide sequence which hybridizes under stringent conditions to SEQ ID NO: 1, 2, or 3, or to a fully complementary nucleotide sequence, where over-expression in yeast of the isolated nucleic acid provides increased xylose fermentation in the yeast relative to a control yeast lacking over-expression of the isolated nucleic acid, is new.    USE - The isolated nucleic acid, recombinant yeast, recombinant S. cerevisiae strain, and method are useful for producing ethanol by fermentation of xylose in yeast (all claimed).    ADVANTAGE - The isolated nucleic acid is highly improved and can be efficiently used in xylose fermentation, and for enhanced biofuel production, particularly ethanol production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a recombinant yeast comprising the isolated nucleic acid; (2) a method for producing ethanol by fermentation of xylose in yeast, comprising: (a) culturing under ethanol-producing conditions the recombinant yeast; and (b) isolating ethanol produced by the recombinant yeast; and (3) a recombinant Saccharomyces cerevisiae strain, comprising: (a) an isolated nucleic acid encoding an aldo/keto reductase (AKR) or a nucleotide sequence which hybridizes under stringent conditions to the isolated nucleic acid encoding AKR, or to a fully complementary nucleotide sequence, operably linked to a heterologous promoter; and (b) XYL1, XYL2 and XYL3 genes from Pichia stipitis.
NOVELTY - Soluble organic fertilizer comprises at least one soluble organic nutrient.    USE - The fertilizer is useful for: enhancing plant growth, nutrition or crop production (claimed); and controlling one or more pathogens in or on a seed, in the soil, or in or on a plant. No biological data given.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the soluble organic fertilizer, comprising liquefying a solid organic nutrient source, extracting at least one soluble organic nutrient from the liquefied solid organic nutrient source, and saturating the soluble organic nutrient onto a soluble absorbent carrier.
NOVELTY - A one or more isolated, purified, or substantially pure insecticidal lipids or lipid fractions from fungus of phylum Ascomycota, are new.    USE - The insecticidal lipids or lipid fractions are useful in composition for controlling one or more insects, and reversing, wholly or in part resistance of insect to insecticides using entomopathogenic agents (all claimed) and phytopathogenic insects, and in agricultural and horticultural applications. The composition is in the form of powder, dust, pellet, granule, spray, emulsion, colloid or solution.    ADVANTAGE - The insecticidal lipids or lipid fractions are environmentally-friendly and has less toxic.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition comprising one or more insecticidal lipids or one or more insecticidal lipid fractions from fungus of the phylum Ascomycota together with at least one carrier;    (2) method for producing biological control composition, involves providing a culture of one or more fungi of the phylum Ascomycota, maintaining the culture under conditions suitable for production of at least one lipid or lipid fraction, and (i) combining the at least one lipid or lipid fraction with carrier, entomopathogenic fungi or its culture, (ii) separating the at least one lipid or lipid fraction from the fungi, (iii) at least partially purifying or isolating the at least one lipid, or (iv) any combination of two or more of (i)-(iii); and    (3) method of preparing insecticidal lipid or lipid fraction.
NOVELTY - Repelling an insect or a hoofed animal, comprises applying a repelling composition to a surface, where the insect or the hoofed animal is repelled from the surface, and the repelling composition comprises: a base oil (78-88 wt.%) including white oil, polyalphaolefins, glycols, polyalkylene glycols, alkylated naphthalenes, alkylated benzenes and/or esters; a thickening agent (5-12 wt.%); a tackifying polymer (5-10 wt.%); a repellent agent (0.025-0.1 wt.%) including capsaicin, piperine, allyl isothiocyanate and/or allicin; and a solubility improving additive (1-2 wt.%).    USE - The method is useful for repelling an insect or a hoofed animal, where the insect (including cockroach) is exterminated, and the hoofed animal (including horse) is deterred from at least one undesirable behavior including cribbing, removing bandages (both preferred) or wood-chewing (all claimed). No biological data given.    ADVANTAGE - The method utilizes the repellent composition which: is odor free or low odor, thus enabling them to be employed in areas e.g. restaurants, stores, and homes where odors would otherwise be offensive or unacceptable; is non-toxic, water resistant, economic and environmentally friendly; is tacky, thus enabling them to remain in place when applied to non-horizontal surfaces, and to persist on insects' exoskeletons or hoofed animal when contacted; and is stable and maintains good viscosity/tackiness when exposed to hot or cold ambient conditions.
NOVELTY - A sludge pile-turning machine comprises rack (1); road wheel (2) located at bottom of rack; chained turning rake (3) equipped on rack, where the end of chained turning rake is swinging connected on rack and front end circles on lazy arm (5) by the inhaul cable, and the rack is respectively provided with a horizontal driving device (6) of pile-turning machine for driving the road wheel move front and back; a swinging driving device (7) for pulling the chained turning rake swing up and down; and conveying driving device for driving the chained turning rake convey sludge toward the back.    USE - As a sludge pile-turning machine (claimed), used in the fermentation tank.    ADVANTAGE - The sludge pile-turning machine has rational structure and high automaticity; and fully piles the sludge in the tank, which makes all the sludge fully fermented to reach the purpose of saving the occupied area as fermenting sludge.    DESCRIPTION OF DRAWING(S) - The figure shows a view of the sludge pile-turning machine.    Rack (1)    Road wheel (2)    Chained turning rake (3)    Lazy arm (5)    Horizontal driving device (6)    Swinging driving device (7)
NOVELTY - Soil conditioner prepared by taking soil (50 parts by weight (pbw)), original sawdust (25 pbw) and rice husk (25 pbw), uniformly mixing and stirring the mixture, roasting the mixture under high temperature at 105-125 degrees C for 8 hours after drying and cooling the mixture, is claimed.    USE - The soil conditioner is useful for treating biological waste including poultry, eggshell, cornstalk, foots fish goods, poultry excrement of animals and/or swill. (all claimed).    ADVANTAGE - The soil conditioner is eco-friendly, autonomously absorbs air and nutrients, slowly releases the air and nutrient during the growth of crop, and removes the foul smell of the waste of living beings.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method-I for preparing taking soil (50 parts by weight (pbw)), original sawdust (25 pbw) and rice husk (25 pbw), uniformly mixing and stirring the mixture, roasting the mixture under high temperature at 105-125 degrees C for 8 hours after drying and cooling the mixture; and    (2) a method-II for treating biological waste by soil conditioner, comprising taking soil conditioner and biological waste and mixing the mixture and letting the mixture natural state
NOVELTY - Self-healing artificial landscape of river and lake, comprises forming ice layer on a water surface, breaking an ice cave in different positions on an ice face, forming a half vent state below the ice face, adding microbe enzyme agent using an artificial landscape of lake and a half vent cavity below the ice face, and fermenting and self-restoring biological water by allowing the water to flow slowly for self-restoring the water and decomposing the sewage at the bottom of the water, where a water level is nearest to sewage at the bottom of the water in a dry season.    USE - The method is useful for self-healing artificial landscape of river and lake in winter and summer seasons.    ADVANTAGE - The method is carried out in an environmentally friendly manner with low cost.
NOVELTY - Method for manufacturing bio oil, involves mixing (in parts weight): biomass (50-80) and crude glycerin (20-50) in a reactor, heating and evaporating the mixture in furnace, subjecting the product to pyrolysis, decomposing the obtained product, heating the product, cooling the product in cooling device, carbonizing the carbide in the product, storing the obtained product in storage tank, cooling and condensing the product, distilling the product under reduced pressure, evaporating the product using vacuum evaporator, and condensing and cooling the product.    USE - The method is useful for manufacturing bio oil which is used in carbide (all claimed).    ADVANTAGE - The method is rapid and economical.
NOVELTY - Preparation of high purity of gefitinib comprises generating 4-chloro-7-methoxy-6-(3-morpholin-4-ylpropoxy)quinazoline hydrochloride by reacting with aniline to obtain gefitinib hydrochloride, neutralizing crude gefitinib and processing post-treatment.    USE - Method for preparing high purity of gefitinib (claimed).    ADVANTAGE - The method has shortened production period, reduces energy consumption, decreases amount of used solvent, has low production cost, and reduces the solvent to human body and environment; and produces gefitinib of high purity.
NOVELTY - The method involves redirecting gas flow from a dry filter (WFS) to a vertical plate heat exchanger (PPWC), where high boiling fractions of cooling gas are condensed and discharged to a drain of high-boiling liquid. The gas is directed to a liquid condensing unit to perform moisture condensation. Low-boiling organic compounds are discharged to drain a condensate tank. Stream of gas is directed to a liquid filter (FC) to obtain cool water-free gas. Solid particles deposited on surface of coke are collected in a reservoir by gravity and input to the heat exchanger to water-cool the particles.    USE - Method for purifying product gases obtained by gasification of yellow and gray straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for purifying product gases obtained by gasification of yellow and gray straw.    Liquid filter (FC)    Vertical plate heat exchanger (PPWC)    Dry filter (WFS)    Horizontal filter (WFSH-1)    Tank (ZGN)
NOVELTY - Making a catalyst, comprises (a) treating a zeolite socony mobil (ZSM)-5 zeolite with a phosphorus-containing compound to form a phosphorus-promoted ZSM-5 component, (b) preparing a slurry comprising the phosphorus-promoted ZSM-5 component and a silica-containing binder and (c) shaping the slurry into shaped bodies.    USE - The catalyst is useful for the conversion of particulate biomass to a fuel (all claimed), where the fuel is gasoline, jet fuel, diesel fuel and petrochemical, and the biomass includes any biological material, inedible materials such as grasses, saw dust, wood chips, wood bark, twigs, straw, corn stover, cotton linters and bagasse.    ADVANTAGE - The process provides the catalyst that is free of amorphous alumina. The catalyst has: higher bio-oil yield and lower coke than the conventional catalysts; and improved hydrothermal stability and/or deoxygenation activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process-I for the conversion of particulate biomass to a fuel, comprising: step (a), step (b) and step (c) as above per se; and (d) contacting the shaped bodies with a particulate biomass in a reactor under conditions for biomass conversion to a fuel.
NOVELTY - The system has a mass flow torrefaction reactor (25) including mass flow characteristics, containing particulate biomass and equipped with a heated gas input (19), a gas discharge output, a particulate solid inlet and particulate solid discharge. The reactor is configured as a vertical arranged cylindrical or rectangular vessel (5) having an upper straight walled section (20) and defining a reaction chamber and a lower tapered bottom section (22). The heated gas input is positioned at a top portion of the tapered bottom section or bottom portion of an upper straight-walled section.    USE - System for facilitating torrefaction of biomass e.g. forest waste, agricultural crop grown for energy production or by-product of agricultural activity and cellulosic biomass from urban origin, obtained from forest thinning operations as non-commercial slash from commercial logging operations and purposeful agricultural operations.    ADVANTAGE - The system enhances efficiency of use of a mass flow hopper as the reactor, which provides uniform treatment of biomass material so as to pretreat raw particulate biomass prior to charging to the reactor and to mitigate variance of natural feed material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a process for producing torrefied biomass by subjecting raw particulate biomass to elevated temperature sufficient to bring about torrefaction of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a torrefaction reactor.    Vertical arranged cylindrical or rectangular vessel (5)    Heated gas input (19)    Upper straight walled section (20)    Lower tapered bottom section (22)    Mass flow torrefaction reactor (25)
NOVELTY - The method involves rising temperature of preheater (2) by supplying hot-air to preheater, after stopping the circulation of organic substance raw material supply with respect to thermal decomposition device (4), and heat carrier. The material supply halt condition and hot-air supply state are continued, after the temperature in preheater reaches preset steady operation temperature. The rapid heating operation which circulates through heat carrier is performed until temperature in modifier (3) and temperature in thermal decomposition device reach preset temperature respectively.    USE - High-speed warm-up method for heat carrier circulating-type gasification system of organic substance e.g. woody biomass such as coppiced timber and pruned branch. Can also be used in plastic.    ADVANTAGE - The organic substance gasification system can be heated rapidly, thus the organic substance can be gasified reliably. The electric power can be generated using the gas generated by the gasification system effectively, thus the profit to the seller of electric power is increased. The number of labors required for operating the gasification system is reduced, thus the labor cost can be reduced. Since the gasification system is maintained with certain temperature by performing heat retention operation above constant temperature, the operation of the organic substance gasification system stopped temporarily can be restarted reliably and rapidly, while reducing energy consumption of the gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic substance gasification system. (Drawing includes non-English language text)    Hot-air generation apparatus (1)    Preheater (2)    Modifier (3)    Thermal decomposition device (4)    Transfer apparatus (6)
NOVELTY - A pressure gauge (4p) measures the internal pressure of the thermal decomposition device (4). The differential pressure elimination operation which stops supply of organic substance raw material is performed, and the hot-air supply to the pre-heater (2) is continued, when the measured result by pressure gauge exceeds predetermined steady operation permissible range. The supply of substance raw material is restarted and differential pressure elimination operation is completed, when the measured result by pressure gauge is returned to preset steady operation permissible range.    USE - Gasification system of organic substance such as woody biomass e.g. coppiced timber.    ADVANTAGE - The differential pressure with respect to the modifier generated in the thermal decomposition device of heat carrier circulating-type system can be eliminated, without requiring decomposition cleaning.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for thermal decomposition device differential pressure elimination method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification system of organic substance. (Drawing includes non-English language text)    Hot-air generation apparatus (1)    Pre-heater (2)    Modifier (3)    Thermal decomposition device (4)    Pressure gauge (4p)
NOVELTY - Methane tank has a sealed reservoir with a top and a bottom. Inside the reservoir, there is an inner and an outer fermentation chamber, pipes for feeding liquefied organic wastes, outlet of the fermented mass, and pipes for outlet of biogas. The inner chamber is insulated from the outer chamber and lies coaxially inside it on supports which are connected to the bottom of the reservoir. The inner chamber is linked to the outer chamber through a system of pipes connected to a separator. The system of pipes consists of a pipe for feeding into the inner chamber a mixture of volatile fatty acids from the separator and air from an air inlet, a pipe for feeding a substrate after the hydrolysis phase and acidogenesis from the inner chamber into the separator for separation of volatile fatty acids from the thick mass, and a pipe for feeding the thick mass, separated from the volatile fatty acids in the separator, into the outer chamber under gravity.    USE - Chemistry.    ADVANTAGE - Shorter duration of fermentation of organic wastes and high efficiency. 2 dwg
NOVELTY - The system has an outer shell provided with a gas inlet, a tail gas exhaust port, a reforming air inlet pipe and a gas outlet pipe. An inner part of the outer shell is provided with a combustion chamber that is arranged with an inner shell and in a porous medium body. A reforming chamber is made of metal honeycomb structure, arranged between the outer shell and the inner shell, and filled with foam. A gas mixing device is connected with the combustion chamber through the gas inlet. A fireproofing device is arranged between the combustion chamber and the gas mixing device.    USE - Coupled-type reforming reactor solid oxide fuel cell (SOFC) generating system.    ADVANTAGE - The system has improved integration degree.
NOVELTY - Sintered refractory product comprises chromium oxide (greater than 10 wt.%), hafnium oxide (greater than 2 wt.%) and zirconium oxide (greater than 1 wt.%), where the total content of chromium oxide, hafnium oxide and zirconium oxide is greater than 70 wt.%.    USE - The sintered refractory product is useful for a gasifier (claimed), which is useful for gasifying coal, petroleum coke, biomass, wood and heavy oils to be recycled and for producing synthesis gas.    ADVANTAGE - The sintered refractory product exhibits enhanced thermal shock resistance and corrosion resistance, and excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasifier comprising a reactor provided with an interior wall partially covered by a refractory coating including refractory product.
NOVELTY - Sintered refractory product comprises chromium oxide (greater than 10 wt.%), hafnium oxide (greater than 2 wt.%) and zirconium oxide (greater than 1 wt.%), where a structure of the product has an aggregate bound by a matrix and the total content of chromium oxide, hafnium oxide and zirconium oxide is greater than 70 wt.%.    USE - The sintered refractory product is useful for a gasifier (claimed), which is useful for gasifying coal, petroleum coke, biomass, wood and heavy oils to be recycled and for producing synthesis gas.    ADVANTAGE - The sintered refractory product exhibits enhanced thermal shock resistance and corrosion resistance, and excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasifier comprising a reactor provided with an interior wall partially covered by a refractory coating including refractory product.
NOVELTY - A catalyst has nonprecious metal alloy, consists of 2 types of nonprecious metal elements where 1st nonprecious metal element determines the crystal structure of the nonprecious metal alloy, and 2nd nonprecious metal element. The d band center (Epsilon d) of the 1st nonprecious metal element is -1.7 to -1.2 eV.    USE - Catalyst for steam reformation of methane (claimed) used in manufacture of hydrogen for fuel cells.    ADVANTAGE - Catalyst exhibits outstanding steam reforming performance equal to noble metals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modification catalyst body comprising catalyst for steam reforming supported on a porous base as the porous catalyst support layer made of alumina, zirconia, ceria and/or silicacarrier particles.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory diagram of the crystal structure of catalyst for steam reforming.    Catalyst for steam reforming (1)    1st nonprecious metal element (2)    2nd nonprecious metal element (3)
NOVELTY - A liquid hydrocarbon fuel comprising organosulfur compound(s) containing sulfur having concentration of more than 50 weight ppm to less than 400 weight ppm, is contacted with an oxidant and steam or water, in presence of catalyst bed comprising reforming catalyst deposited on ultra-short-channel-length metal substrate at peak catalyst temperature of more than 950 degrees C, and a reformate mixture comprising hydrogen and carbon monoxide is obtained. Thus, sulfur-containing liquid fuel is reformed.    USE - Reformation of sulfur-containing liquid fuel e.g. kerosene, diesel, biodiesel, Fisher-Tropsch fuel, JP-8, JP-5 and Jet A (all claimed) used for fuel cell used as power supply for portable and logistic applications.    ADVANTAGE - The method safely and economically reforms sulfur-containing liquid fuel with excellent reforming efficiency and catalyst efficiency, with suppressed generation of desulfuration.
NOVELTY - The hydrogen station system (1) comprises a proton exchange membrane electrolyzer (2) to generate hydrogen, a compression device (3) for hydrogen, a system (4) for refueling a vehicle (5) with the compressed hydrogen, and an infrastructure, by which additional components are connected. The electrolyzer is connected with the compression device, and the compression device is connected to the refueling system. An output pressure of the hydrogen produced in the electrolyzer is 30-50 bar. The compression device is designed for compression of hydrogen at 700 bar, and comprises a compressor tank.    USE - The hydrogen station system is useful for the production of hydrogen on demand.    ADVANTAGE - The compact and safe hydrogen station system exhibits high reliability.    DETAILED DESCRIPTION - The hydrogen station system (1) comprises a proton exchange membrane electrolyzer (2) to generate hydrogen, a compression device (3) for hydrogen, a system (4) for refueling a vehicle (5) with the compressed hydrogen, and an infrastructure, by which additional components are connected. The electrolyzer is connected with the compression device, and the compression device is connected to the refueling system. An output pressure of the hydrogen produced in the electrolyzer is 30-50 bar. The compression device is designed for compression of hydrogen at 700 bar, and comprises a compressor tank, which is directly connected with the refueling system. The electrolyzer comprises a maximum power of 4 MW. An INDEPENDENT CLAIM is included for a method of operating a hydrogen station system for the production of hydrogen.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a hydrogen station system.    Hydrogen station system (1)    Proton exchange membrane electrolyzer (2)    Compression device (3)    Refueling system (4)    Vehicle. (5)
NOVELTY - The boiler has a cylindrical furnace body connected with a safety valve and a hot water outlet, where lower part of the furnace body is connected with an ash inlet, a fire grate, a feeding port, an air inlet and an upper part of a water level controller.    USE - Biomass gasification direct-fired hot water boiler for use in a toilet and a greenhouse.    ADVANTAGE - The boiler is simple in structure, safe and reliable to use, convenient to install and inexpensive, and can obtain high heating efficiency, high energy saving effect, high environmental protection and has wide range application.
NOVELTY - The composter has an aerator (20) that is arranged within container accommodating material to be composted, and is provided with openings for allowing air to pass from the aerator into the container. The composting material is sat above a leachate tank located under floor (60) of base structure (30). An air flow path is formed in base structure for providing air from outside to the aerator and to openings located in floor above the leachate tank to facilitate aerobic decomposition of the composting material. The underside of the floor is supported by spaced pillars (40).    USE - Composter for disposing waste organic material.    ADVANTAGE - Since the air flow path is formed in the base structure for providing air from outside to the aerator and to openings located in the floor above the leachate tank, the ready transfer of air for the aerator and the top of the leachate tank is facilitated. Hence, the aerobic decomposition is performed on the compositing material in the container efficiently. The leachate that drains from the composting mass is collected by the leachate tank effectively during composting process of the material.    DETAILED DESCRIPTION - The spaced pillars of composter are extended upwardly from the base of the leachate tank. Each pillar is provided with cut out (61) in the wall surface to facilitate air flow into the leachate tank. The composting material is supported by a perforated floor panel. An air inlet is utilized to allow air to flow through air channels (66,67) beneath the floor and to enter the container through holes in the floor.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the composter.    Aerator (20)    Base structure (30)    Pillar (40)    Floor (60)    Cut out of pillar (61)    Air channels (66,67)
NOVELTY - Adapting microorganisms (22) to increases the microorganisms efficiency in producing ethanol, comprises: (a) providing a tallow base (18) comprising Chinese tallow tree (16) parts mixed with water; (b) inoculating the tallow base with yeast; and (c) adapting the yeast in the tallow base in a growth stage such that the yeast will ferment and produce ethanol from cellulosic material other than Chinese tallow tree.    USE - The method is useful for adapting microorganisms to increases the microorganisms efficiency in producing ethanol (claimed), which is useful as a rocket fuel in certain early bio-propellant rocket vehicles and for combustion in automobiles, as a food source, as an antiseptic, in medical wipes and antibacterial hand sanitizer gels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a method-I of producing ethanol, comprising preparing a mash, where the mash comprises water and an organic material (44), inoculating the mash with a starter culture (10), where the starter culture comprises yeast of the genus Saccharomyces and the fungus Pichia membranifaciens, fermenting the mash, and recovering ethanol from the mash; and (2) a culture for fermenting cellulosic materials comprising yeast of the genus Saccharomyces and the fungus Pichia membranifaciens which have been adapted in a mixture comprising Chinese tallow tree and water such that the culture will ferment cellulosic materials other than Chinese tallow tree.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an ethanol production system.    Starter culture (10)    Chinese tallow tree (16)    Tallow base (18)    Microorganisms (22)    Organic materials. (44)
NOVELTY - Fuel composition comprises: (A) a normally liquid fuel; and (B) a cold flow improving amount of (i) a metathesized natural oil and/or (ii) a metathesized natural oil derivative.    USE - Used as fuel composition.    ADVANTAGE - The cold flow additives modify the low temperature flow behavior of normally liquid fuels and lowers the cloud point, pour point and/or cold filter plugging point of the fuels. The metathesized natural oils is derived from renewable sources (e.g. vegetable oils, animal fats or oils) and are made using environmentally friendly production techniques with less energy than processes for making fuel additives derived from petrochemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising the reaction product of (a) the metathesized natural oil with (b) a nucleophile, oxidizer, aromatic compound and/or enophilic acid reagent.
NOVELTY - The apparatus (100) has electrode portions (20,30) which are arranged on sides of inflow cell (10). The electrolyte solution is flowed into the inflow cell. The electrolyte solution passes the electrode portions are supplied to outflow cells (40,50). The pressure of electrolyte solution in inflow cell is higher than the pressure of electrolyte solution in outflow cells. The outflow cells are provided with introducing portion. The electrode portions are equipped with electrode substrates.    USE - Apparatus for decomposition of electrolyte solution e.g. water for generating hydrogen and oxygen used in medical field, chemical industry, gas welding application, and steel manufacturing process.    ADVANTAGE - The electrolyte solution is separated by setting the pressure of electrolyte solution in inflow cell higher than the pressure of electrolyte solution in outflow cells, so that the gas generated by electrolysis or photolysis of electrolyte solution can be recovered easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolyte solution decomposition method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolyte solution decomposition apparatus. (Drawing includes non-English language text)    Inflow cell (10)    Electrode portions (20,30)    Outflow cells (40,50)    Photocatalyst film (91)    Electrolyte solution decomposition apparatus (100)
NOVELTY - The apparatus (100) has flow-path formation cell (10) which forms flow path through which water flows into apparatus main portion. The electrodes (20,30) are respectively arranged by facing the flow-path formation cell. The water passing through the electrodes is discharged by respective outflow cells (40,50). The electrodes are spaced apart and are arranged downstream to each other. A reference electrode is provided in the flow-path formation cell.    USE - Apparatus for decomposition of electrolyte solution e.g. water, for generating hydrogen and oxygen used in medical field, gas welding application, manufacturing process of steel and chemical industry.    ADVANTAGE - The electrodes are respectively arranged by facing flow-path formation cell, and water in electrodes is discharged by respective outflow cells, so that electrolyte solution decomposition apparatus can easily separate and collect oxygen and hydrogen gas generated by electrolysis or photolysis of water. The working efficiency of the electrolyte solution decomposition apparatus can be improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for decomposition of electrolyte solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolyte solution decomposition apparatus.    Flow-path formation cell (10)    Electrodes (20,30)    Outflow cells (40,50)    Electrolyte solution decomposition apparatus (100)    Separator (400)
NOVELTY - A processing apparatus of nitrogen-containing organic substance wastewater has a methane fermentation tank (1) for carrying out methane fermentation treatment of wastewater under anaerobic condition, a microfiltration or ultrafiltration membrane separator (2) for separating processed liquid into solid and liquid, a reverse osmosis membrane separator (5) for desalinating filtrate of separator, an evaporation concentration apparatus (6) for concentrating concentrated water of separator, and a unit for adding acid to concentrated water of separator introduced into concentration apparatus.    USE - Apparatus used for processing nitrogen-containing organic substance wastewater discharged from manufacture of semiconductor and liquid crystal, and manufacturing pure water.    ADVANTAGE - The method reduces generation amount of wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of processing apparatus of nitrogen-containing organic substance wastewater. (Drawing includes non-English language text)    Methane fermentation tank (1)    Microfiltration or ultrafiltration membrane separator (2)    Filtrate tank (3)    Reverse osmosis membrane separator (5)    Evaporation concentration apparatus (6)
NOVELTY - Producing butanol, comprises filtering a butanol-containing solution through a nanofiltration membrane, and collecting butanol containing solution from the permeate flow of the nanofiltration membrane.    USE - The method is useful for producing butanol, which is useful as raw material of chemicals and pharmaceutical agents, solvent, and fuel material.    ADVANTAGE - The process is cost-effective for producing butanol with high purity.
NOVELTY - For producing fatty ester composition comprising a beta-hydroxy ester, engineered recombinant microorganism, comprising heterologous polynucleotide sequence encoding a polypeptide having ester synthase activity (EC 2.3.1.75), where in the presence of a carbon source the recombinant microorganism produces an ester composition comprising beta-hydroxy esters.    USE - For producing fatty ester composition comprising a beta-hydroxy ester (claimed); useful in biofuel (e.g. biodiesel), industrial chemical, or component of, or feedstock for, biofuel or industrial chemical.    ADVANTAGE - The recombinant microorganism engineered to produce fatty acid precursor molecules and fatty acid derivatives having desired properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production (M1) of fatty ester composition comprising beta-hydroxy esters involving: culturing the recombinant microorganism in the presence of a carbon source under conditions to produce a fatty ester composition comprising beta-hydroxy esters; and    (2) a composition produced by the method (M1).
NOVELTY - Composite gasoline is obtained by homogeneously mixing (in wt.%): methanol (45-65), gasoline (35-45), ethanol (1.5-2.5) and xylene (1-1.5).    USE - As composite gasoline.    ADVANTAGE - The composite gasoline has excellent antiknock property and stability, and can be manufactured cost-effectively.
NOVELTY - Recombinant cyanobacterium comprising an exogenous nucleic acid molecule encoding a transcription factor domain protein, is new, where the cyanobacterium produces a greater amount of at least one free fatty acid or its derivative than does a cyanobacterium that does not contain an exogenous nucleic acid molecule encoding the transcription factor domain protein.    USE - The recombinant cyanobacterium is useful for producing a free fatty acid or its derivative (claimed), and/or lipids derivatives in photosynthetic microorganisms, which are used for biofuels.    ADVANTAGE - The recombinant cyanobacterium increases the amount of fatty acids production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing a free fatty acid or its derivative, comprising culturing the recombinant cyanobacterium under conditions in which the nucleic acid molecule is expressed to produce the free fatty acid or fatty acid derivative; and    (2) an isolated or recombinant nucleic acid molecule, comprising a nucleic acid sequence encoding a polypeptide comprising an amino acid sequence having at least 85% or at least 95 % sequence identity to SEQ ID NOs: 2, 4, 6, 8, 10 or 12 (each comprising fully defined sequence of 148, 546, 391, 696, 105 or 109 amino acids, respectively as given in the specification).
NOVELTY - Solidification of wastewater involves solidifying (S40) wastewater by mixing with polymer material.    USE - Solidification of wastewater used for solid material for industrial material, solid fuel (all claimed), and construction material.    ADVANTAGE - The method is economically carried out with reduced generation of carbon dioxide by environmentally-friendly process.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of solidification of wastewater.    Providing wastewater (S10)    Reducing heavy metal (S20)    Dehydrating wastewater (S30)    Solidification (S40)
NOVELTY - A continuous trans-esterification reaction method for trans-esterifying triglyceride involves: continuously providing triglycerides; continuously providing monohydric alcohol; continuously mixing triglycerides and monohydric alcohol in presence of nanostructured trans-esterification catalyst where the catalyst is present with largest cross-sectional dimension of 50-200 nm and where the monohydric alcohol is present as supercritical fluid; continuously trans-esterifying the triglycerides with the monohydric alcohol and generating mono-ester derivatives of triglycerides.    USE - In trans-esterifying triglyceride (claimed) for preparing biodiesel.    ADVANTAGE - The method continuously trans-esterifies triglyceride.
NOVELTY - A polyimide-type asymmetrical hollow fiber membrane consists of a polymer blend of a linear polyimide and multibranched polyimide.    USE - Polyimide-type asymmetrical hollow fiber membrane for separation of carbon dioxide and methane.    ADVANTAGE - The polyimide asymmetrical hollow fiber membrane has excellent gas permeability, particularly carbon dioxide and methane separation properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of polyimide-type asymmetrical hollow fiber membrane, which involves preparing mixed solution of linear polyamic acid which is a precursor of linear polyimide, and multibranch polyamic acid which is precursor of multibranched polyimide, forming hollow fiber-like structure consisting of a mixture of linear polyamic acid and multibranch polyamic acid using a hollow fiber-formation apparatus, and heat-processing hollow fiber-like structure.
NOVELTY - A composite hollow fiber membrane (10) has a compact layer (14) formed in the inner surface or outer surface of a porous layer (12) containing porous materials. The compact layer is formed with multibranched polyimide-type material.    USE - Composite hollow fiber membrane is used for separating methane and carbon dioxide.    ADVANTAGE - The composite hollow fiber membrane has excellent gas separation property.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of composite hollow fiber membrane.    Composite hollow fiber membrane (10)    Porous layer (12)    Compact layer (14)
NOVELTY - Recombinant microorganism comprising a recombinant pathway including a heterologous beta -ketothiolase and one or more enzymes comprising an acetyl-coenzyme A acetyltransferase, a 3-hydroxybutyryl-coenzyme A dehydrogenase, a crotonase, a trans-2-enoyl-coenzyme A reductase and a bifunctional aldehyde/alcohol dehydrogenase, is new.    USE - The recombinant microorganism is useful for producing 6-8C alcohol, which are n-hexanol and/or octanol (claimed). The microorganism is useful for synthesizing biofuels from a carbon dioxide.    ADVANTAGE - The microorganism exhibits improved yield of alcohol production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) making the recombinant microorganism; and    (2) making n-hexanol and/or octanol, comprising culturing the recombinant microorganism with a substrate and under conditions to produce n-hexanol and/or octanol.
NOVELTY - An oleaginous composition (C1) comprises oil extracted from biomass comprising a microorganism.    USE - As oleaginous composition (claimed) useful for making jet fuel, aviation fuel (avgas), diesel fuel, gasoline, fuel oil and lubricating oil.    ADVANTAGE - The composition (C1) has a percent mass fraction with a boiling point of 260-630 degrees F (preferably 490-630 degrees F) of 5-55% (preferably 20-35% or 30-45%) as determined by ASTM protocol D7169-11. The composition is substantially identical to geologic petroleum in that it is compatible with existing petroleum infrastructure and can be refined into the same classes of compounds as those obtained from the refining of fossil fuels. The oleaginous composition contains fewer amounts of phosphorus content, sodium content, calcium content, magnesium content, manganese content, strontium content, and potassium content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an oleaginous composition (C2) comprising a phosphorus content of less than 20 parts per million (ppm) and a sodium content of less than 50 ppm, where the composition is obtained from aquatic biomass.
NOVELTY - A hydrogen ion-conductive copolymer (I) including diphenyl fluorene group in which sulfonic acid group is introduced, is new.    USE - New hydrogen ion-conductive copolymer is used for forming polymer electrolyte membrane for membrane/electrolyte assembly used in polymer electrolyte membrane fuel cell (all claimed).    ADVANTAGE - The film formed using the hydrogen ion-conductive copolymer has excellent flexibility, mechanical properties, dimensional stability and hydrogen ion conductivity.    DETAILED DESCRIPTION - A hydrogen ion-conductive copolymer of formula (I) including diphenyl fluorene group in which sulfonic acid group is introduced, is new.    A=H or -SO3H;    L1,L2=-O- or -SO2;    m,n=2-500;and    m/(n+m)=0.05-5.    An INDEPENDENT CLAIM is included for manufacture of hydrogen ion-conductive copolymer (I).
NOVELTY - A synthesis gas conversion catalyst comprises nickel; two or more metals selected from ruthenium, palladium, gold, chromium, aluminum and tin; a promoter comprising at least one of an alkali metal or alkaline earth metal; and a catalyst support selected from silica, alumina, and magnesium oxide, or its mixture.    USE - The synthesis gas conversion catalyst or process is useful for producing one or more 2-4C alcohols (claimed). It can also be used for converting synthesis gas where the primary product is a mixture of ethanol, propanol, and butanol, optionally in conjunction with higher alcohols.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process for producing one or more 2-4C alcohols comprising placing synthesis gas in contact with the catalyst under conditions sufficient to convert at least a portion of the synthesis gas to at least one of ethanol, propanol and butanol.
NOVELTY - A synthesis gas conversion catalyst (C1) comprising nickel, molybdenum, at least one metal selected from palladium, ruthenium, chromium, gold, zirconium or aluminum, a promoter comprising at least one of alkali metal or alkaline earth metal and a catalyst support selected from silica, alumina and/or magnesium oxide, is new.    USE - As a catalyst for producing 2-4C alcohol, particularly methanol, ethanol, propanol or butanol and acetaldehyde from synthesis gas (Claimed).    ADVANTAGE - The catalyst enables conversion of syngas to alcohols even at relatively low pressures such as less than or equal to 500 psig (3.4 MPa). Thus use of this pressure is economically attractive as it avoids cost of high pressure vessels, compressors, and energy costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process (P1) for producing at least one 2-4C alcohol involving placing synthesis gas in contact with the catalyst (C1) under conditions to convert at least a portion of the synthesis gas to at least one of ethanol, propanol and butanol.
NOVELTY - Method (10) for processing organic substance waste liquid, involves using calcium silicate.    USE - The method is useful for processing organic substance waste liquid, preferably Shochu liquor lees waste liquid (claimed), where the processed liquid is used as feed and fertilizer.    ADVANTAGE - The method is cost-effective and environmentally-friendly. The organic waste liquid can be recycled repeatedly. The processed organic waste liquid is free from phosphorus, and hence suitable as replenishment source of livestock or crops when used as feed or fertilizer. The fertilizer is natural and does not contain any chemical components. The calcium silicate has excellent bulk density, permeability, oil absorption amount, porosity, Brunauer Emmett Teller specific surface area of 20-300 m2/g, pore volume of 0.05-2 ml/g, and average pore diameter of 3-20 nm.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram illustrating processing method of organic substance waste liquid.    Hydrothermal synthesis process (1)    Methane fermentation process (3)    Solid-liquid separation process (4)    Drying process (5)    Processing method of organic substance waste liquid (10)
NOVELTY - Catalyst comprises metal microparticle chosen from nickel, cobalt, iron, copper, magnesium, chromium and aluminum which is coated on surface of particle of complex oxide sintered component containing vanadium component.    USE - The catalyst is useful for manufacturing gasified hydrocarbon fuel and alcoholic fuel (claimed) which are used for preparing carbon nanofiber useful as reinforcement and electrically conductive material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing catalyst, which involves mixing metal microparticle chosen from nickel, cobalt, iron, copper, aluminum, magnesium, and chromium with compound containing vanadium, subjecting the product to thermal reaction process, and depositing the metal oxide on the surface of complex oxide sintered component.
NOVELTY - Hydrogen storage material is obtained by mixing and reacting (in mol.%): at least one type of metal borohydride (30-85) chosen from sodium borohydride, lithium borohydride, potassium borohydride, and magnesium borohydride, metal chloride (10-50) chosen from magnesium chloride, aluminum chloride, nickel chloride, zinc chloride, iron chloride, cobalt chloride, tin chloride, and palladium chloride, and metal hydroxide (1-50) chosen from sodium hydroxide, lithium hydroxide, potassium hydroxide, magnesium hydroxide, calcium hydroxide, and aluminum hydroxide.    USE - The material is used in tank for storing hydrogen (claimed) which is used as energy source, preferably fuel cell.    ADVANTAGE - The material has excellent deterioration tolerance with respect to repeated hydrogen desorption and occlusion, and low hydrogen desorption temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen storage tank (1), which is filled with the hydrogen storage material (3).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the hydrogen storage tank.    Hydrogen storage tank (1)    Container (2)    Hydrogen storage material (3)    Unit (4)    Filling unit (5)
NOVELTY - Hydrogen generated in water electrolysis unit (3) which works by reproducible energy and carbon dioxide contained in waste gas emitted in a combustion installation (1) are supplied in a row from the water electrolysis unit and the combustion (3a), and reacted in presence of catalyst using the exhaust heat of the waste gas, to obtain reaction material of dimethyl ether, methanol and ethanol as exhaust heat and renewable energy utilization reaction material.    USE - Manufacture of exhaust heat and renewable energy utilization reaction material e.g. reaction material of dimethyl ether, methanol and ethanol used as fuel.    ADVANTAGE - The method efficiently and economically provides exhaust heat and renewable energy utilization reaction material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for exhaust heat and renewable energy utilization reaction material-manufacturing system, which comprises a water electrolysis unit, a hydrogen-transfer line which transfers hydrogen produced with the water electrolysis facility, a waste gas transfer line which transfers the waste gas containing the carbon dioxide generated in a combustion installation, and a reactor which makes the hydrogen supplied from hydrogen-transfer line and the waste gas transferred from the said waste gas transfer line react in catalyst presence. The hydrogen transfer line and the waste gas transfer line are connected.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of exhaust heat and renewable energy utilization reaction material-manufacturing system. (Drawing includes non-English language text)    Combustion installation (1)    Fuel gas supply line (1a)    Waste gas transfer line (1b)    Water electrolysis unit (3)    Transfer line (3a)    Windmill (4)
NOVELTY - A waste-derived solid fuel storing facility has fermenter (52) which carries out anaerobic fermentation of waste-derived solid fuel, a biogas storage tank which stores biogas generated during anaerobic fermentation of waste-derived solid fuel, a flow path (p1) which sends biogas to biogas storage tank from fermenter, and a supply path which supplies the biogas to fuel installation from biogas storage tank. The storage facility stores the waste-derived solid fuel which ferments easily, before burning by a combustion installation.    USE - Facility is used for storing waste-derived solid fuel (claimed) e.g. refuse-derived fuel and biomass-type waste-derived solid fuel.    ADVANTAGE - The facility efficiently stores the waste-derived solid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for storage method of waste-derived solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the conceptual diagram of fuel storage portion of facility. (Drawing includes non-English language text)    Fuel storage portion (5)    Fuel injection tank (11)    Fermenter (52)    Primary storage tank (53)    Oxygen concentration detector (78)    Methane concentration detector (79)
NOVELTY - A biological organic fertilizer comprises (wt.%) activated biological bacterial liquid (4), fulvic acid (19.2), oil residue (24), sediment (14.4), medical stone (9.6), urea (9.888), diammonium hydrogen phosphate (4.224), and potassium chloride (14.688).    USE - Biological organic fertilizer used for promoting growth of sunflower (claimed).    ADVANTAGE - The fertilizer is environment-friendly and rich in nutrients, has residue degradation property to protect the soil, and can fully satisfy growth requirement of sunflower.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biological organic fertilizer, comprising:    (A) drying and grinding organic raw material and chemical fertilizer, and sieving through 100-120 meshes for later use;    (B) preparing activated bacterial liquid by preparing original bacterial liquid, brown granulated sugar and water at ratio of 1:1:18; dissolving brown granulated sugar in 100 degrees C boiling water, adding into a fermenting tank, adding original bacterial liquid when water temperature is 36 degrees C, stirring for 15-30 minutes and stirring for once every 6 hours for 84 hours;    (C) mixing the organic raw material and chemical fertilizer, uniformly stirring, adding the activated bacterial liquid, completely mixing and stirring, and entering to a tank by conveying system; and    (D) fermenting for 20-30 days at normal temperature to obtain the product.
NOVELTY - High temperature fermenter comprises thermal storage raw material that is arranged in outer wall, inner wall and wall of the fermenter.    USE - The high temperature fermenter is useful in fermentation plant for carrying out high temperature fermentation of organic waste, grass and tree, and producing biogas, manure or methane gas (claimed). The organic wastes are livestock excrement, fishery waste and household waste.    ADVANTAGE - The high temperature fermenter saves energy and cost-effectively produces manure with good quality.
NOVELTY - Degrading biomass or pretreated biomass to sugars using enzyme, is claimed.    USE - The process is useful for degrading biomass or pretreated biomass to sugars (claimed). The polypeptide is useful: in the preparation of a food product, a detergent, and an animal feed; and for prebleaching kraft pulp, processing lignin, producing ethanol, treating textiles or dyed textiles.    ADVANTAGE - The enzyme is cost effective, and has cellulase enhancing activity, high specific activity, stability, or resistance to inhibitors.    DETAILED DESCRIPTION - Degrading biomass or pretreated biomass to sugars using enzyme, is claimed, where the enzyme comprises a polypeptide having: (a) a polypeptide sequence of SEQ ID Nos: 3, 6, 9, 12, 15, 18, 21, 24, 27 and 30; (b) a polypeptide that is at least 60%, preferably 99% homologous to the sequence of SEQ ID Nos: 3, 6, 9, 12, 15, 18, 21, 24, 27 and 30; (c) a polypeptide sequence encoded by nucleic acids sequence of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 23, 25, 26, 28 and 29, or nucleic acids that are at least 60%, preferably 99% homologous to sequence of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 23, 25, 26, 28 and 29; (d) a polypeptide sequence encoded by a nucleic acids sequence hybridizing under stringent conditions to the polynucleotide sequence of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 23, 25, 26, 28 and 29; or (e) a polypeptide sequence encoded by a nucleic acids sequence hybridizing under stringent conditions to the reverse complement of a polynucleotide sequence of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 23, 25, 26, 28 and 29, where sequences not defined here may be found at ftp://ftp.wipo.int/pub/published-pct-sequences/publication.
NOVELTY - Methane generator stirring system comprises a first loop in the middle of a methane generator. A suction head connected with a lumen of the first loop. An upper part of the first loop is connected with a junction station. A second loop is located at the bottom of the methane generator. A sprayer is connected with a lumen of the second loop. The sprayer forms a certain angle at the upper wall of second loop and distributed along the tangential direction of the second loop in clockwise or counterclockwise direction. A slurry pump is located outside the methane generator.    USE - Used as a methane generator stirring system.    ADVANTAGE - The system improves the gas generating efficiency.
NOVELTY - A reusable deodorizing particulate conditioner comprises uniform wood particles with size of 0.5-10 cm, and organic acid including lactic acid, malic acid and tartaric acid.    USE - Deodorizing particulate conditioner used in sludge composting.    ADVANTAGE - The conditioner is easy to screen, reusable, biodegradable, and convenient for microbial attachment; has uniform size and shape, light weight, good fluidity, good hygroscopicity, adjustable water content, high deodorization nitrogen efficiency, and no adsorption saturation; and enables circulating inoculation and deodorization. The residue does not reduce product quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of conditioner by crushing dry wood into particles of 0.5-10 cm, soaking in 10-60% organic acid solution for 5-20 hours, and air-drying or drying until anhydrous; and    (2) application of conditioner in sludge composting including mixing sludge and conditioner at weight ratio of 1:0.35-1.35 (preferably 1:0.7) to obtain a mixture with water content of 55-65%, in which the sludge has water content of 75-85 (preferably 80%) and organic content of 40-85 (preferably 60%); aerobically fermenting the mixture at high temperature and ventilation rate of 0.05-6 (preferably 0.2) m3/minute-m3, and maintaining the temperature of mixture at more than 55 degrees C for greater than or equal to 5 days and adjusting ventilation rate to 1.5 m3/minute-m3 when the temperature of mixture is more than 60 degrees C; and fermenting for 9-20 days, discharging the material after fermenting for 16 days, screening the conditioner with screening rate of more than 98%, and directly drying or air-drying the screened conditioner for 0.5-2 days and recycling to quickly neutralize and fix ammonia and to inoculate microorganism in sludge composting process, in which reduction in nitrogen loss of sludge is more than 65% and nutrient content of product is increased to more than 25%.
NOVELTY - The campfire structure has wooden blocks that are devoid of charcoal and additive. The wooden blocks are immersed in hot paraffin wax. The wooden blocks are dried for removing moisture content. The diseased or dead trees are used as wooden blocks.    USE - Campfire structure used in harsh weather conditions such as winter, snow, rain and wind.    ADVANTAGE - The wooden blocks can burn for 15 minutes. The fire can be provided for longer time by adding wooden blocks when fire burns down. The warming effect is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the campfire structure.
NOVELTY - The method involves feeding biomass slurry into a continuous flow reactor. The biomass in the continuous flow reactor is liquefied. Water and water soluble components from biomass slurry are discharged from the flow reactor. Solid material in the biomass slurry is passed into another continuous flow reactor. Residual biomass from the biomass slurry is liquefied. Water and water soluble components from the biomass slurry are discharged from the latter continuous flow reactor. The biomass slurry is discharged from the reactors at specific temperature.    USE - Method for performing iterative liquefaction of biomass slurry.    ADVANTAGE - The method allows performing fractionation, separation and collection of valuable components from the biomass in a simple, quick and effective manner, thus improving recovery rate of valuable product components of the biomass. The method enables avoiding generation of strain on a processing equipment during liquefaction process of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for performing iterative liquefaction of biomass slurry.
(SE201150465-A1)   NOVELTY - The method involves cooling torrefied reacted products obtained from an exothermic torrefying station to temperature of a partially counteracted product. A heat exchanger is utilized to heat the partially counteracted product within temperature range of 5 to 50 degrees Celsius. A eucalyptus lignocellulose biomass is dried and heated in the exothermic torrefaction station that is connected to a cooling source. A rotatable drum is coupled to another rotatable drum. Compartments are connected together by a connection part.    USE - Method for torrefying of dried and heated biomass products.    ADVANTAGE - The method enables allowing precise control of the exothermic torrefying station so as to facilitate accurate control of the quality and properties of the torrefied reacted products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a torrefaction arrangement comprising at least one torrefaction zone where the torrefaction zone comprises means for cooling and optionally also means for heating and the means for cooling is connected to a vessel or arrangement containing a cooling media, which is water.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an exothermic torrefying station.
NOVELTY - The system has a fermenter chamber (1) arranged near a tank (7) that is located next to a separator (10). A hopper (4) and a pumping unit (5) are arranged in the fermenter chamber. A liquid reactants reservoir (6) is placed next to a biogas tank (2). A motor, a transformer (8), a torch (9) and a reservoir (11) are arranged with each other.    USE - System for production of electricity and heat using biogas produced by anaerobic digestion of organic substrates.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a system for production of electricity and heat using biogas produced by anaerobic digestion of organic substrates.    Fermenter chamber (1)    Biogas tank (2)    Hopper (4)    Pumping unit (5)    Liquid reactants reservoir (6)    Tank (7)    Transformer (8)    Torch (9)    Separator (10)    Reservoir (11)
NOVELTY - The device has a vegetation water tank arranged with a substrate fermentation reactor (1) and equipped with anchors (2). A mixer (7) is placed in the substrate fermentation reactor and connected to floats (8).    USE - Device for obtaining biogas from aquatic plants.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a device for obtaining biogas from aquatic plants.    Substrate fermentation reactor (1)    Anchors (2)    Mixer (7)    Floats (8)
NOVELTY - The method involves compressing a dried material (4) before thermal treatment for raising density of a raw material (6). A feedstock is made of a lignocellulose biomass biological material. Firewood and grasses are broken into units with maximum volume of 200 cubic-centimeters. Air content of the firewood and grasses are reduced by compressing density of dried crude products (5) to 30 percent. The compressed dried crude products are subjected to thermal treatment at temperatures between 200-1800 degrees Celsius.    USE - Method for manufacturing carbon content products.    ADVANTAGE - The method enables increasing volume of the wood and bark so as to increase the volume of biomass obtained by efficient heat transfer. The method enables reducing the supply of nitrogen at pyrolysis of dry distilled product, so that the obtained powder is easy to evaporate. The method enables utilizing gases for conversion of synthetic products, thus improving the commercial value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a carbon content products manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for manufacturing carbon content products.    Dried material (4)    Dried crude products (5)    Raw material (6)
NOVELTY - Use of Gonostegia hirta is claimed for treating biogas residues generated from livestock and poultry industry. The G.hirta is planted in polluted environment containing the biogas residues.    USE - The G.hirta is useful for treating biogas residues generated from livestock and poultry industry (claimed), and in medicine for invigorating spleen to promote digestion, clearing heat and promoting diuresis, removing toxin and dispersing swelling.    ADVANTAGE - The G.hirta is simple, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for automatic oxygen-supply artificial wetland system, which comprises internal portion comprising filing substance and hollow shale bricks, and aperture gaps of the hollow shale bricks for supplying oxygen into the wetland system.
NOVELTY - An organoselenium-enriched rice is cultivated by preparing rice seedling matrix having thickness of 0.5-1 cm for sowing 0.8-0.9 kg bud seed/m2; before transplanting rice, applying selenium-enriched organic-inorganic fertilizer as base fertilizer at 20-35 kg/acre, and then spraying selenium-enriched organic-inorganic fertilizer as foliar fertilizer at 10-25 kg/acre; and applying selenium-enriched organic-inorganic fertilizer as topdressing fertilizer at 30-60 kg/acre prior to rice tillering stage, and harvesting mature rice to obtain organoselenium-enriched rice.    USE - Method of cultivating organoselenium-enriched rice (claimed).    ADVANTAGE - The method is safe and has no pollution.
NOVELTY - Tryptanthrin derivatives or their salts, solvates, polycrystalline matters, enantiomers or racemic mixtures are new.    USE - For preparing indoleamine-2,3-dioxygenase (IDO) inhibitor drugs; for preparing drugs for preventing and treating diseases related to tryptophan metabolism disorder mediated by indoleamine-2,3-dioxygenase (IDO), where the diseases related to the tryptophan metabolism disorder mediated by the indoleamine-2,3-dioxygenase (IDO) comprise tumor, cancer, Alzheimer's disease, autoimmune disease, cataract, psychological disorder, depression and anxiety disorder (all claimed).    ADVANTAGE - In comparison with an acknowledged indoleamine-2,3-dioxygenase (IDO) inhibitor, the tryptanthrin derivative (I) has a stronger IDO inhibition function and is applicable to treating diseases of IOD-mediated tryptophan metabolism-pathway pathological features such as tumor, cancer, Alzheimer's disease, autoimmune disease, cataract, psychological disorder, depression and anxiety disorder. The preparation method of the compound (I) provides convenient operation and gentle reaction conditions; saves the solvent; decreases pollution; and is suitable for industrial production.    DETAILED DESCRIPTION - Tryptanthrin derivatives of formula (I) or their salts, solvates, polycrystalline matters, enantiomers or racemic mixtures are new.    R1 or R2=H, 1-5C alkyl, halo or a substituent group of formula (II) (preferably F or H);    R3=aryl (preferably phenyl);    n=0-3 (preferably 1).    Provided that one of R1 and R2 is the substituent group of formula (II). An INDEPENDENT CLAIM is included for preparation of the compound (I) involving reacting substituted 1H-benzo(d)(1,3)oxazine-2,4-dione compound of formula (XIII) with substituted 1H-indole-2,3-dione compound of formula (XIV) in the presence of alkali to obtain the compound (I).
NOVELTY - Continuous system includes using a separator for continuous recovery of meal in pig manure, where soluble substances (urine and dirt) are washed and removed to obtain impurities free product. The product is sterilized by removing fecal coliform and Bacilli bacteria. Fertilizer is obtained from pig manure, where coagulation, flocculation and pressing processes are carried out for pig slurry.    USE - Continuous system used for recovery of bran and obtaining fertilizer from manure of pigs (claimed).    ADVANTAGE - The continuous system is economic and eco-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous system.    Waste pipe (1.1)    Pump (2)    Solution preparation box (3)    Drinking water pipe (4)    Continuous dryer (7)    Hood (8)
NOVELTY - The device has a vacuum contactor which is connected with a storage battery, a switch, and a load. The storage battery is connected to an AC/DC circuit and a DC/DC circuit through a diode. The DC/DC circuit is connected with the AC/DC circuit. The AC/DC circuit and the DC/DC circuit are connected with a polymer hydrogen fuel battery.    USE - Hydrogen energy generating device.    ADVANTAGE - The stability of the hydrogen energy generating device can be improved.
NOVELTY - The device has a sealing cover that is provided with several electric power generating units. The generating units are provided with a positive electrode plate, a cathode plate and a conductive medium outlet. The positive electrode plate is provided in a shell portion. The positive electrode plate is fixed to the sealing cover. The positive electrode plate and negative electrode plate are arranged in conducting medium.    USE - Fuel generating device.    ADVANTAGE - The structure of the fuel generating device is simple. The pollution and noise are not generated, by using the device.
NOVELTY - The device has a furnace unit that is provided with a feeding port at the top. A microwave generator is installed on the furnace unit whose inner wall is provided with a heat insulating material. The feeding port is set with a gas sealing valve, whose upper portion is provided with an exhaust pipe. The bottom of the gasification furnace is provided with a slag outlet. The air inlet pipe is set with an air inlet adjusting valve. The exhaust pipe of device is connected with the inlet of the gas cooling device.    USE - Biomass microwave cracking and gasifying device.    ADVANTAGE - The energy consumed by the device can be reduced. The device is safe and reliable to use.
NOVELTY - The system (10) has gas-liquid separating apparatus (22) that is located upstream of water electrolysis apparatus (12) in gravitational direction to separate moisture contained in high-pressure hydrogen. A hydrogen supply line (20) is provided to supply high-pressure hydrogen discharged from water electrolysis apparatus to the gas-liquid separating apparatus. A current regulator is provided to regulate a current to be applied to the water electrolysis apparatus based on the water level detected by the water level detector (90) in the gas-liquid separating apparatus.    USE - Water electrolysis system for decomposing water to generate oxygen and hydrogen.    ADVANTAGE - The current regulator is provided to regulate a current to be applied to the water electrolysis apparatus based on the water level detected by the water level detector in the gas-liquid separating apparatus, thus the water level in the gas-liquid separating apparatus can be controlled by regulating the electrolysis current. The need for providing a special water discharge structure in the gas-liquid separating apparatus can be eliminated. Hence efficient water electrolysis with a simple configuration and simple process can be obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system.    Water electrolysis system (10)    Water electrolysis apparatus (12)    Water circulating apparatus (16)    Hydrogen supply line (20)    Gas-liquid separating apparatus (22)    Controller (28)    Water level detector (90)
NOVELTY - Production of fuel involves flowing bio-oil vapor into a reaction zone of the reactor, heating bio-oil vapor and hydrocarbon oil and/or melt in a reaction zone, cracking, and then extracting cracked reaction products.    USE - Production of fuel e.g. diesel fuel.    ADVANTAGE - The method efficiently and economically provides fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel-producing apparatus, which comprises a reaction zone for heating bio-oil vapor, hydrocarbon oil and/or melt, and a bio-oil inlet port arranged to flow bio-oil vapor into the reaction zone.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of fuel-producing apparatus.    Reaction chamber (1)    Oil (2)    Feed port (3)    Settling unit (4)    Mixing unit (5)
NOVELTY - Performing a hydrothermal carbonation reaction, comprises supplying a biomass to a reaction space and creating pressure and temperature with respect to the reaction conditions required for the course of a hydrothermal carbonation reaction by injecting steam. The vapor is introduced under swirling of the biomass within the reaction space in jet form.    USE - The method is useful for performing a hydrothermal carbonation reaction.    ADVANTAGE - The even distribution and enhanced mixing of the biomass in the reaction space by energetic potentials including temperature and pressure, help the complete carbonation of the biomass and improve the yield and quality of the product with less process time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reaction tank (1) of a device for performing hydrothermal carbonation of biomass, comprising the reaction space with a supply tool (3) for supplying of biomass and a supply tool (5) for supplying of vapor, where the supply tool for supplying of vapor comprises at least one injector arranged in a near surface swirling area, for the swirling of the biomass with the help of the inflowing vapor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic, perspective view angle from above of a device for carrying out a hydrothermal carbonation reaction.    Reaction tank (1)    Preheating tank (2)    Biomass supply (3)    Biomass pump (4)    Steam supply (5)
NOVELTY - The method involves supplying biomass feedstock dry granular material and active charcoal powder for deodorizing to upper surface of circular vibration board (2). A separation unit is provided to separate the excessive active charcoal powder which did not adhere to the biomass feedstock dry granular material surface. An active charcoal-powder coated on surface of biomass feedstock dry granular material is continuously discharged from the discharge port (6) of a movement terminal unit along circumferential direction.    USE - Method for manufacturing deodorizing type bio-solid fuel.    ADVANTAGE - The active charcoal powder can be coated easily and reliably on the surface of biomass feedstock dry granular material. The productivity of the deodorizing type bio-solid fuel can be improved. The space utilization of the deodorizing type bio-solid fuel manufacturing apparatus is reduced, so that the cost of the deodorizing type bio-solid fuel manufacturing apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the deodorizing type bio-solid fuel manufacturing apparatus. (Drawing includes non-English language text)    Coating apparatus (1)    Circular vibration board (2)    Material supply unit (3)    Discharge port (6)    Separation unit (8,8a,8b)
NOVELTY - Domestic garbage and waste tire pyrolysis waste spiral feeding pump comprises vertically arranged primary spiral feeder provided with hopper. The hopper is provided with first screw rod driven by first motor. The first screw rod is provided with first spiral blade. The feeding hopper has feeding port with upper end connected with secondary spiral feeder, and bottom having discharging opening. It has inner air chamber which is connected with negative pressure generator.    USE - Domestic garbage and waste tire pyrolysis waste spiral feeding pump.    ADVANTAGE - The feeding pump has rational structure, provides safe and controlled feeding process, and environment friendly.    DETAILED DESCRIPTION - Domestic garbage and waste tire pyrolysis waste spiral feeding pump comprises vertically arranged primary spiral feeder provided with hopper. The hopper is provided with first screw rod driven by first motor. The first screw rod is provided with first spiral blade. The feeding hopper has feeding port with upper end connected with secondary spiral feeder, and bottom having discharging opening. It has inner air chamber which is connected with negative pressure generator. It has feeding inlet arranged with cutter-shaped valve for opening and closing feeding port; and discharge hole provided with cutter-shaped outlet valve. The second screw secondary spiral feeder has cylinder body provided with second screw rod driven by second motor and provided with second screw blade. The secondary spiral feeder cylinder end is set with drop type cover board. The air chamber has vacuum degree of 5-10 kPa. The domestic garbage and waste tire pyrolysis waste spiral feeding pump has first motor power of 2.2-3 kW and speed reducer ratio of 1:87; and second motor power of 5.5-7.5 kW and speed reducer ratio of 1:87.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of domestic garbage and waste tire pyrolysis waste spiral feeding pump.
NOVELTY - The furnace has an outer wrapped heat water bag (4) provided with an inner drum and an outer drum. A furnace bottom part (11) is provided with a blower (10). A fire combustion chamber (7) is equipped between the inner drum and the outer drum and connected with a chimney (16). A side part of a dry distillation chamber is provided with an auxiliary combustion-supporting burner (8). A combustion-supporting air hole is formed on an inner cylinder wall of a furnace body (1). A front cavity opening of a combustion chamber is connected to the dry distillation furnace.    USE - Multifunctional biomass straw raw material gasification furnace.    ADVANTAGE - The furnace can produce combustible gas at high temperature and anoxic condition under dry distillation of straw raw material so as to reduce generation of tar pollution and peculiar smell and improve heat energy conversion rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a multifunctional biomass straw raw material gasification furnace.    Furnace body (1)    Outer wrapped heat water bag (4)    Fire combustion chamber (7)    Auxiliary combustion-supporting burner (8)    Blower (10)    Furnace bottom part (11)    Chimney (16)
NOVELTY - The complex (10) has an expander (15) for expanding and cooling compressed c. A heat exchanger (16) removes water and carbon dioxide from the exhaust gas passing through a waste heat recovery cycle i.e. organic rankine cycle (ORC) (13), by phase change. The exchanger generates a stream of fuel that is returned to an inlet of an anode (11) of a fuel cell i.e. solid-oxide fuel cell (SOFC), with a higher molar concentration of carbon monoxide and hydrogen fuel than the concentration initially present in fuel cell anode exhaust gas before entering the waste heat recovery cycle.    USE - SOFC recirculation complex for use in a large-scale power system of a turbine to provide electricity for industrial and municipal applications and smaller portable application such as car. Can also be used for a phosphoric acid fuel cell (PAFC), molten carbonate fuel cell (MCFC), and proton exchange membrane fuel cell (PEMFC).    ADVANTAGE - The complex can boost overall performance of the SOFC while simultaneously separating a nearly pure stream of carbon dioxide for sequestration or generating electrical power to increase overall efficiency and economics of operations of the SOFC to about 60 percentage with simultaneous carbon capture and reduce pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a SOFC recirculation complex.    SOFC recirculation complex (10)    Anode of SOFC (11)    ORC (13)    Expander (15)    Heat exchanger (16)
NOVELTY - Copolymer comprising (in mole%) substituted butane repeating units (I) (10-90) and (II) (90-10), where the sum of (I) and (II) is 100 mole%, is new.    USE - The copolymer is useful: for improving cold flow properties of the middle distillate fuels; as additives for fuels comprising biofuel oils based on fatty acid esters, or mixtures of (A) at least one biofuel oil based on fatty acid esters (30-less than 100 wt.%) and (B) middle distillates of fossil-, plant- and/or animal origin (greater than 0-70 wt.%) that are free of fatty acid esters, comprising hydrocarbon mixtures; and for lowering the pour point value of middle distillate fuels (all claimed).    ADVANTAGE - The copolymer exhibits improved low-temperature behavior in middle distillate fuels, and effectively reduces the pour point of the middle distillate fuels.    DETAILED DESCRIPTION - Copolymer comprising (in mole%) substituted butane repeating units of formula (CH3-C(R1)(R2)-C(R3)(R4)-CH3) (I) (10-90) and (CH3-C(R5)(R6)-C(R7)(R8)-CH3) (II) (90-10), where the sum of (I) and (II) is 100 mole%, is new.    R1, R2 = H, 1-4C alkyl or -COOR9;    R9 = 6-30C hydrocarbyl;    R3, R4 = H, 1-4C alkyl, -COOR9 or -C=O, which may also be present in the form of its alkali metal-, alkaline earth metal- or ammonium salts;    R5 = -A-CO-O-R10;    A = 1-20C alkylene;    R10 = 1-30C hydrocarbyl; and    R6-R8 = H or 1-8C alkyl.    INDEPENDENT CLAIMS are also included for:    (1) preparing the copolymer; and    (2) middle distillate fuels comprising the above copolymer (10-5000 ppm by weight).
NOVELTY - The apparatus (1) has a heat resistor (34) exposed to an atmosphere, and a control circuit (5) controlling the heat resistor to exhibit two different temperatures. The control circuit detects output voltages from the heat resistor corresponding to two different temperatures. The control circuit obtains potential differences by subtracting respective offset voltages from the corresponding detected output voltages and amplifies the potential differences. The control circuit detects a state of gas in the atmosphere using the amplified potential differences.    USE - Combustible gas detecting apparatus for detecting a state such as concentration of combustible gas i.e. hydrogen, in an atmosphere, or leakage of the combustible gas in the atmosphere, or moisture in the atmosphere of a fuel-cell vehicle. Can also be used for detecting a state of helium and methane.    ADVANTAGE - The apparatus enables detecting the state of the gas with high accuracy by setting a large amplification factor even in case of using a low-cost electronic controller such as a microcomputer, thus minimizing the circuit size, and reducing cost of the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for detecting a state of gas in an atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a combustible gas detecting apparatus. '(Drawing includes non-English language text)'    Combustible gas detecting apparatus (1)    Control circuit (5)    Microcomputer (7)    Heat resistor (34)    Amplifying circuits (101, 102)
NOVELTY - A catalyst consists of carrier containing silica and 0.5-14 %mass of zirconium oxide and 10-40 %mass of cobalt metal and cobalt oxide by tricobalt tetraoxide conversion, with respect to mass of the carrier. The reduction degree of cobalt atom in the catalyst is 75-93%. The catalyst has hydrogen gas adsorption amount of 0.40-1.0 ml/g per unit mass of the catalyst at 100 degrees C.    USE - Catalyst for manufacture of hydrocarbon by Fischer-Tropsch synthesis reaction (claimed) used for fuel oil.    ADVANTAGE - The catalyst having high activity is manufactured without using expensive metal seed such as rhenium. The hydrocarbon is manufactured efficiently using the catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrocarbon, which involves carrying out Fischer-Tropsch synthesis reaction of raw material containing carbon monoxide gas and hydrogen gas in the presence of catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the Fischer-Tropsch synthesis reaction system. (Drawing includes non-English language text)    Bubbling-tower type fluid bed reaction apparatus (1)    Reactor (2)    Cooling pipe (3)    Gas-liquid separators (4,6)    Splitter (5)
NOVELTY - The method involves fixing an oxidation blower in a high temperature thermolysis gasification blast furnace. High temperature synthesis gas is supplied to the gasification blast furnace through a high temperature water cooling flue (1). Qualified synthesis gas is stored in a wet gas holder storage unit. Temperature of the high temperature thermolysis gasification blast furnace is 1000-1100 degrees Celsius. Waste heat is produced by a medium pressure steam supply unit. The high temperature water cooling flue is made of a film-type water cooling pipe structure.    USE - Positive pressure biomass synthesis gas and oil purification processing method.    ADVANTAGE - The method enables improving cooling process of synthesis gas, removing dust from the high temperature synthesis gas, reducing energy consumption, improving efficiency of the high temperature synthesis gas and stability and performance of the high temperature thermolysis gasification blast furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a positive pressure biomass synthesis gas and oil purification processing method.'(Drawing includes non-English language text)'    High temperature water cooling flue (1)    Water cooling-type quench tower (2)    Water pipe-type waste heat furnace (3)    Heat pipe waste heat furnace (4)    Venturi washing tower (5)
NOVELTY - Preparing mechanically stabilized polyazole polymers, comprises: producing a film comprising polyazoles with at least one amino group in repeat unit; treating the film with a solution comprising at least one strong acid and at least one stabilizing reagent; performing the stabilization reaction in the membrane obtained in step directly or in a subsequent membrane processing step by heating to a temperature greater than 60 degrees C; and optionally additionally doping the membrane obtained with a strong acid or concentrating the strong acid present by removing water present.    USE - The process is useful for preparing mechanically stabilized polyazole polymers, which is useful for obtaining membrane, where the membrane is useful for producing membrane electrode assembly, which is useful for production of a fuel cell (all claimed).    DETAILED DESCRIPTION - Preparing mechanically stabilized polyazole polymers, comprises: (a) producing a film comprising polyazoles with at least one amino group in repeat unit; (b) treating the film from step (a) with a solution comprising at least one strong acid and at least one stabilizing reagent, where the total content of stabilizing reagents in the solution is 0.01-30 wt.%; (c) performing the stabilization reaction in the membrane obtained in step directly or in a subsequent membrane processing step by heating to a temperature greater than 60 degrees C; and (d) optionally additionally doping the membrane obtained in step (c) with a strong acid or concentrating the strong acid present by removing water present, where the stabilizing reagent comprises at least one compound which has at least one aldehyde group and at least one hydroxyl group or at least one hemiacetal group or at least one acetal group. An INDEPENDENT CLAIM is included for a membrane obtainable by the process.
NOVELTY - The device has a central rotating shaft connected with a main shaft of a variable-frequency motor that is arranged on a lower part of the central rotating shaft. The central rotating shaft rotates by the variable-frequency motor. Blades are arranged on the central rotating shaft. An upper part of the central rotating shaft is divided into an upper part and a lower part. Diameter of an upper part of the blades is larger than diameter of a lower part of the blades.    USE - Spiral material stirring conveying device for a biomass destructive distillation cracking device.    ADVANTAGE - The device ensures effectively controlling raw material conveying and cracking reaction time and pyrolysis dry distillation and cracking reaction process, and improves heat efficiency.
NOVELTY - The system has a stacking sub-system (A) composed of a washing unit, a de-nitration unit, a decarbonising unit and an acidic substance recycling unit. The de-nitration unit has a flue gas compressor (P2) compressing flue gas at given pressure, where the compressed flue gas is passed to a de-nitration tower. A solid recovery and recycling system (H) is composed of a water filled solid collecting groove and multiple depth resources processing terminals. A solid collecting tank collects cooling solid from alkaline water that is passed to a gas processing system as washing water.    USE - Municipal solid waste processing and using system.    ADVANTAGE - The system eliminates the classification process of waste, and prevents poisonous and harmful greenhouse gas from being released to atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a municipal solid waste processing and using system. '(Drawing includes non-English language text)'    Stacking sub-system (A)    Electron system (E)    Gas treatment and recycling system (G)    Solid recovery and recycling system (H)    Flue gas compressor (P2)
NOVELTY - Method for increasing production of methane during methane fermentation of excrement, involves adding sodium acetate to excrement contained in a fermenter and fermenting the excrement.    USE - The method is useful for increasing production of methane during methane fermentation of excrement, preferably pig excrement (claimed).
NOVELTY - The method involves connecting a high temperature water-cooling flue (1) with a condensate slag water tube waste heat furnace (3). A water pipe-type waste heat furnace is provided with a heat pipe waste heat furnace section. Low steam is supplied to an outer side of a heat pipe waste heat furnace by the heat pipe waste heat furnace section. Dust is extracted by a gas fan (7) and sent to a wet gas holder (8) or downstream section.    USE - Biomass synthesis gas positive pressure oil purification method.    ADVANTAGE - The method enables providing better dust removing and recycling effect and better stability and economic performance and reducing energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass synthesis gas positive pressure oil purification method.'(Drawing includes non-English language text)'    High temperature water-cooling flue (1)    Condensate slag water tube waste heat furnace (3)    Wet electric dust collector (6)    Gas fan (7)    Wet gas holder (8)