NOVELTY - Method for culturing edible fungus, involves inoculating edible fungus strain into a solid culture medium at 20-26 degrees C for 25-40 days to obtain solid strain, adding stabilizing agent in water or potato dextrose agar liquid culture medium, mixing the mixture uniformly to obtain liquefacient, adding the solid strain into the liquefacient, stirring the mixture, filtering the mixture to obtain liquid strain, inoculating the liquid strain into the culture medium, and culturing the strain.    USE - The method is useful for culturing edible fungus chosen from mushroom, needle mushroom, and Pleurotus eryngii (claimed).    ADVANTAGE - The method is simple, feasible, stable, environmentally-friendly, less labor intensive, and suitable for industrial production, reduces waste of raw materials, and produces edible fungus with high quality.
NOVELTY - Preparing roflumilast comprises: (a) mixing 4-difluoromethoxy-3-hydroxy benzaldehyde with cyclopropylmethyl bromide, and reacting to obtain 3-(cyclopropylmethoxy)-4-(difluoromethoxy)benzaldehyde; (b) mixing 3-(cyclopropylmethoxy)-4-(difluoromethoxy)benzaldehyde with the potassium permanganate, and reacting to obtain 4-(difluoromethoxy)-3-(cyclopropylmethoxy)benzoic acid; and (c) mixing 4-(difluoromethoxy)-3-(cyclopropylmethoxy)benzoic acid with 4-amino-3,5-dichloropyridine, and reacting to obtain roflumilast crude product and post treating.    USE - The method is useful for preparing roflumilast.    ADVANTAGE - The method is simple, and economical; has high product yield; and does not produce harmful gases.    DETAILED DESCRIPTION - Preparing roflumilast comprises: (a) mixing 4-difluoromethoxy-3-hydroxy benzaldehyde with cyclopropylmethyl bromide in a weight ratio of 1:0.8-5, reacting for 1-8 hours at -30 to 80 degrees C in a solvent under the influence of a catalyst, extracting and recycling to obtain 3-(cyclopropylmethoxy)-4-(difluoromethoxy)benzaldehyde; (b) mixing 3-(cyclopropylmethoxy)-4-(difluoromethoxy)benzaldehyde with the potassium permanganate in a weight ratio of 1:0.2-8, reacting for 1-6 hours in a solvent at -38 to 80 degrees C, evaporating the solvent to dryness, acidifying and filtering to obtain 4-(difluoromethoxy)-3-(cyclopropylmethoxy)benzoic acid; and (c) mixing 4-(difluoromethoxy)-3-(cyclopropylmethoxy)benzoic acid with 4-amino-3,5-dichloropyridine in a weight ratio of 1:0.2-4, reacting in the presence of thionyl chloride in a solvent at -20-50 degrees C for 1-3 hours to obtain roflumilast crude product and post treating the crude-product.
NOVELTY - Device comprises: receiving container; acid-genetic reactor and alkaline reactor; vibration-vortex mixer reactor, which is connected to the bioreactor; staggered thermo-furnace; and line of vibration aerodrying which is connected to aerocyclone for cooling of dry fertilizer.    USE - The device is useful for processing of the waste of cattle raising into dry fertilizer and biogas (claimed).
NOVELTY - Composition and method for manufacturing biodiesel based on gun cleaner and lubricant, by using major portion of biodiesel with a minor portion of synergistically blended chemicals. The method involves adding major proportion of biodiesel into the mixing vessel blended with minor proportion of synergistically blended chemicals, adding minor portion of sulfur or zinc salts of dithio-organophosphate as anti-wear additives, antioxidant, lubricity agent, ether solvent and corrosion inhibitor into mixing vessel containing biodiesel to enhance the properties of biodiesel.    USE - The composition and method is useful for manufacturing biodiesel (claimed) which is used as alternative to petroleum based oils.    ADVANTAGE - The method is simple, rapid and reliable. The produced biodiesel is environmentally-friendly, nontoxic and cost-effective, and has excellent solubility, compatibility, anti-wear, antioxidant, lubricity, and anti-corrosion properties.
NOVELTY - Ethyl salicylate glycoside compounds, and their isomers, and fully-acetylated derivatives, are new.    USE - For preparation of pharmaceutical composition, useful as antipyretic, antiinflammatory, analgesic, or anticoagulant agent (claimed).    ADVANTAGE - The ethyl salicylate glycoside compounds have prolonged effecting time as antipyretic, antiinflammatory, analgesic, or anticoagulant agent i.e. maintain good activity; whereas untoward side effect of gastrointestinal irritation associated with salicylic acid medicine is improved. The ethyl salicylate glycoside compounds can be prepared by simple synthesis method, have low synthesis cost, and small environmental pollution.    DETAILED DESCRIPTION - Ethyl salicylate glycoside compound of formula (I) and its isomers, and fully-acetylated derivatives, are new.    R'=monosaccharide or disaccharide.    An INDEPENDENT CLAIM is included for preparing the compound (I) involving: reacting monosaccharide or disaccharide and acetic oxide to synthesize fully acetylated monosaccharide or disaccharide; converting fully acetylated monosaccharide or disaccharide into sugar ligand; reacting sugar ligand with ethyl salicylate to synthesize fully-acetylated ethyl salicylate glycoside; and deacetylating fully-acetylated ethyl salicylate glycoside to form ethyl salicylate glycoside compound (I).
NOVELTY - A waste is fragmented with synthetic resin water-proof film on lower side of pulp, the fragmented waste fragments are transported to a screw conveyor, caking supplementary agent is sprayed, and mixed and dried. The caking supplementary agent is waste cooking oil. The waste cooking oil is sprayed, and caking supplementary agent is sprayed through caking supplementary agent nozzles which are installed at cylinder entrance portion of a conveyor at a specific interval along transporting direction of the conveyor or installed at a place dividing circumference of the cylinder.    USE - Production of solid fuel.    ADVANTAGE - The solid fuel is efficiently produced without polluting the environment.    DETAILED DESCRIPTION - A waste such as disposable diapers or disposable sanitary pad adhered is fragmented with synthetic resin water-proof film on lower side of pulp, the fragmented waste fragments are transported to a screw conveyor, caking supplementary agent is sprayed, and mixed and the mixed up waste is pressed out to an extruder and dried. The caking supplementary agent is waste cooking oil. The waste cooking oil (5-10 wt.%) is sprayed, and caking supplementary agent is sprayed through caking supplementary agent nozzles which are installed at cylinder entrance portion of a conveyor at a specific interval along transporting direction of the conveyor or installed at a place dividing circumference of the cylinder equally in a uniformly distributed along spiral direction.
NOVELTY - Liquefying agricultural wastes by using ionic liquid catalysts comprises preparing acidic ionic liquid, drying agricultural wastes and grinding to small particles with diameters of 20-60 meshes, washing with de-ionized water and acetone to remove surface oily substances and not completely extracted sugars and water and acetone soluble components, mixing ionic liquid and agricultural wastes in an aqueous solution, heating to 200-350 degrees C in inert gas environment, reacting for 5-75 minutes with stirring to obtain a biological micro-molecular substance and a biological oil with low boiling point.    USE - The method is useful for liquefying agricultural wastes by using ionic liquid catalysts.    ADVANTAGE - The method uses less amount of ionic liquid, the ionic liquid can be recycled; has high utilization rate of agricultural wastes and high selectivity towards micro-molecular substances; and produces biological oil with high calorific value.    DETAILED DESCRIPTION - Liquefying agricultural wastes by using ionic liquid catalysts comprises: (i) preparing acidic ionic liquid; (ii) completely drying agricultural wastes and grinding to small particles with diameters of 20-60 meshes, washing with de-ionized water and acetone to remove the surface oily substances and not completely extracted sugars and water and acetone soluble components; and (iii) completely mixing ionic liquid (0.01-2 mol) and agricultural wastes (1-200 g) in an aqueous solution (10-300 ml), heating to 200-350 degrees C in inert gas environment, reacting for 5-75 minutes with stirring to obtain a biological micro-molecular substance and a biological oil with low boiling point.
NOVELTY - Organic wastewater (AA) is biologically treated under anaerobic conditions. Liquid and solid content are separated from organic wastewater, and anaerobic treatment of separated liquid is carried out to obtain treated water passing through a filter mechanism (3) from sludge in the anaerobic treatment. Anaerobic treatment of the separated solid content is carried out and the processed sludge is supplied to liquid anaerobic treatment.    USE - Treatment of wastewater e.g. domestic wastewater, and sewage generated from industries, sewage works, and foodstuffs factories.    ADVANTAGE - The method uses a filter mechanism which functions stably without increasing the size of anaerobic treatment tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater-treatment system (1).    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the wastewater-treatment system.(Drawing includes non-English language text)    Wastewater-treatment system (1)    Solid-liquid separator (2)    Filter mechanism (3)    Anaerobic treatment tanks (4,5)    Organic wastewater (AA)
NOVELTY - A raw-coal composition comprises striped agglomerate obtained by delayed coking method such that the ratio of generation rate (%mass) of gas comprising 1-4C gases and hydrogen gas generated by coking processing of heavy oils, and formation rate of coking coal composition (%mass) is 0.3-0.8. The ratio of average height of stripes and average length of base side of stripes is 0.15-0.4. The ratio of average length of stripes along the vertical direction and average length of base side of stripes is 5 or more.    USE - Raw-coal composition is used for manufacturing carbon material for negative electrode of lithium-ion secondary battery (claimed) for plug-in hybrid motor vehicle.    ADVANTAGE - The lithium-ion secondary battery containing the raw-coal composition has excellent charging and discharging characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of raw-coal composition; and    (2) manufacture of carbon material.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the battery.    Battery (10)    Negative electrode (11)    Positive electrode (13)    Separator (15)    Aluminum laminated exterior (16)
NOVELTY - Producing biogas with a methane content of at least 80 vol.%, comprises converting a percolate by methanogenic microorganisms into biogas, where the reaction is carried out in a reactor operating under excess pressure, and the excess pressure is at least partially produced by the gas production of the methanogenic microorganisms.    USE - The method is useful for producing biogas.    ADVANTAGE - The method enables the production of biogas with high content of methane, and prevents implementation of a natural gas system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reactor for carrying out a pressure methanogenesis of a percolate, where the reactor is arranged such that it is operated at a pressure of 2-100 bars.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a two-stage system for producing biogas (Drawing includes non-English language text).
NOVELTY - Method for recovering lipids from lipid-producing microorganism, involves providing biomass of lipid-producing microorganism, rupturing cell wall and/or cell membrane of microorganism by algal cytotoxin and thus releasing lipids from the microorganism cell, and recovering lipids.    USE - The method is useful for recovering lipids from lipid-producing microorganism, preferably lipid-producing algae chosen from Chlorophyceae (green algae), Cryptophyceae (recoiling algae), Chrysophyceae (golden brown algae), Diatomophyceae (diatoms), Dinophyceae (dinoflagellates), Euglenophyceae, Eustigmatophyceae, Pavlovophyceae, Pedinophyceae, Prasinophyceae, Prymnesiophyceae (haptophyte algae) and Raphidophyceae (all claimed). The recovered lipids are used in production of biodiesel, renewable diesel, jet fuel, gasoline and base oil.    ADVANTAGE - The method is cost-effective related to energy consumption and suitable for industrial production, maximize value chain of algae, decreases price of raw biooil, and reduces regenerating large amount of solvents.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for integrated system, which comprises first growth vessel for lipid-producing algae, and second growth vessel for cytotoxin producing algae, where the lipid-producing algae is cultivated under conditions suitable for lipid production and cytotoxin producing algae is cultivated under conditions suitable for cytotoxin production, cytotoxins is added from second growth vessel comprising cytotoxin producing algae to first growth vessel comprising lipid-producing algae in sufficient amount to rupture cell walls and/or cell membranes of the lipid-producing algae thus releasing the lipid component from the cell, and recovering lipids from the other cell components.
NOVELTY - Preparing bio-potassium fertilizer, comprises mixing 45-60% of low and medium grade stone powder containing potassium, 40-55% of organic matter, 10-30% of compound bacteria preparation and molasses liquid or water and super fine crushing, fermenting, pelleting, and drying at low temperature.    USE - The method is useful for preparing bio-potassium fertilizer.    ADVANTAGE - The method ensures simple, economic and rapid preparation of the bio-potassium fertilizer in an environmentally friendly manner with improved conversion rate of low and medium grade stone containing potassium and high efficiency.
NOVELTY - Slow-release urea, is claimed, where a coating slow-release liquid is used to cover urea after drying and solidifying urea. The coating slow-release liquid comprises 1-5 mass% of gamma -polyglutamic acid, 1-5% of nitrification inhibitor, 0.5-5% of adhesive, 0.05-2% of surfactant, and rest of water, where pH is 5.5-6.5.    USE - The slow-release urea is useful as a fertilizer.    ADVANTAGE - The environment-friendly, slow-release urea can be economically, simply and easily prepared with high efficiency, saves work time in agricultural production, and effectively improves crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing efficient slow-release urea comprising adding water in a reactor, heating to 50-60 degrees C, adding nitrification inhibitor and stirring for 5-15 minutes, adding adhesive and surfactant and stirring for 5-10 minutes, adding gamma -polyglutamic acid to fully dissolve, adjusting the pH to 5.5-6.5, cooling and coating the urea with fluidized bed spray coating, and drying and solidifying.
NOVELTY - Producing hydrocarbons from biomass involves: providing a feed stream containing biomass having fatty acids, mono-, di-, and/or triglycerides, and a phosphorus content of 10-1000 weight parts per million (wppm); providing a heated hydrocarbon solvent; providing a hydrogen-rich gas; combining the feed stream, heated hydrocarbon solvent, and hydrogen-rich gas in the presence of a low activity hydrogenation catalyst; and recovering a spent low activity hydrogenation catalyst at the end of run. The spent low activity hydrogenation catalyst contains phosphorus (at least 3 wt.%).    USE - For producing hydrocarbons (selected from renewable diesel, chemical intermediates, fluids, and solvents) from biomass (claimed).    ADVANTAGE - The present method can trap phosphorus during conversion of fats and oils to biofuels and bio-based chemicals, such that the trapped phosphorus can economically be recovered for reuse (e.g. as fertilizer).
NOVELTY - Producing biogas from an organic fermentation substrate in an anaerobic process, with low hydrogen sulfide content, comprises converting hydrogen sulfide using iron(III) hydroxide, which is obtained from aqueous sludge as a by-product during the treatment of drinking water or groundwater, into iron sulfide. The sludge is first subjected to mechanical drying and then to thermal drying to obtain a dry grain mixture, from which powdered iron(III) hydroxide is obtained, which is mixed with the fermentation substrate with homogeneous distribution, before carrying out anaerobic process.    USE - The method is useful for producing biogas.    ADVANTAGE - The method produces the biogas with minimum hydrogen sulfide content and thus it avoids the impairment and instability in the biogas production process.    DETAILED DESCRIPTION - Producing biogas formed from an organic fermentation substrate in an anaerobic process, with low hydrogen sulfide content, comprises converting hydrogen sulfide using iron(III) hydroxide, which is obtained from aqueous sludge as a by-product during the treatment of drinking water or groundwater, into iron sulfide. The sludge is first subjected to mechanical drying until the dry matter content of the sludge is 18-35% and then to thermal drying to obtain a dry grain mixture with a grain size of up to 10 mm, from which powdered iron(III) hydroxide with a particle size of 0-0.5 mm is obtained by classifying and/or grinding, and the powdered iron(III) hydroxide is mixed with the fermentation substrate with homogeneous distribution, before the anaerobic process.
NOVELTY - A blueberry fertilizer comprises animal excrement, pine needle powder, saw milled wood ash, and peat powder at mass ratio of 1:0.9-1.1:1.2-1.4:3.2-3.5.    USE - Blueberry fertilizer used for modulating growth and development of blueberry or improving soil quality.    ADVANTAGE - The fertilizer utilizes acidic organic matter as raw materials, meets nutritional growth requirements of blueberry, improves yield and quality of blueberry, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of blueberry fertilizer, comprising:    (A) removing impurities of animal excrement, adding effective microorganisms (EM) bacteria liquid, mixing and uniformly stirring, and fermenting for 5-10 days in a sealed environment of 25-35 degrees C;    (B) crushing saw milled wood ash, peat powder, and pine needle powder into 30-60 meshes; and    (C) uniformly mixing the materials after drying to obtain the fertilizer.
NOVELTY - An agricultural straw is burnt to generate electricity, and supply heat power to generating device. A mixing device is arranged in a granulating device. A marking device and product drying device are connected with generating device. A light generating device is provided with a biomass boiler and steam turbine. The steam turbine generator is arranged to generate electricity to the biomass boiler. A dust remover is connected with the mixing device, granulating device and drying device.    USE - Comprehensive system for processing agricultural waste.    ADVANTAGE - The quality, design, efficiency, operability, reliability and usability of the comprehensive system for processing agricultural waste can be improved. The environmental-pollution effect and energy consumption of the comprehensive system for processing agricultural waste can be reduced.
NOVELTY - A cavity-type gas positive and negative pressure protecting device comprises a tank body provided with a biogas inlet hole, where a gas inlet hole is arranged on the tank body; an inner cavity plate, an inner tower spring and an inner baffle that are arranged at the inner side of the gas inlet hole; an outer cavity plate and a bracket that are arranged in the middle of the gas inlet hole; an outer tower spring and an outer baffle are arranged at the outer side of the gas inlet hole; and a screw rod that sequentially runs through the inner baffle.    USE - The device is useful in biogas engineering.    ADVANTAGE - The device is simple in structure, novel in design, and low in manufacturing cost, where the problems of large area, freezing at low temperature condition, high investment and management cost of the current water seal type positive and negative pressure protector are solved. In this way, the device of can replace the water seal type positive and negative pressure protector in the large and middle biogas engineering.    DETAILED DESCRIPTION - A cavity-type gas positive and negative pressure protecting device comprises a tank body provided with a biogas inlet hole, where a gas inlet hole is arranged on the tank body; an inner cavity plate, an inner tower spring and an inner baffle that are arranged at the inner side of the gas inlet hole; an outer cavity plate and a bracket that are arranged in the middle of the gas inlet hole; an outer tower spring and an outer baffle are arranged at the outer side of the gas inlet hole; and a screw rod that sequentially runs through the inner baffle, the inner tower spring, the inner cavity plate, the outer cavity plate, the bracket, the outer tower spring and the outer baffle; and both ends of the screw rod are screwed down by nuts.
NOVELTY - A quinoline-type compound (I) or (II),is new.    USE - New quinoline-type compound used for preparing antiacetyl cholinesterase medicine.    ADVANTAGE - The quinoline-type compound is efficiently and economically prepared without polluting the environment, by simple method.    DETAILED DESCRIPTION - A quinoline-type compound of formula (I) or (II), is new.    R1,R2=-CH3, -CH2CH3 -CH=CH2, -CH2-CH=CH2, cyclohexyl, phenyl or halophenyl;and    X=groups chosen from group of formulae (i)-(vii).    An INDEPENDENT CLAIM is included for preparation of quinoline-type compound.
NOVELTY - A copper catalyst, an organic solvent, and alkynes are taken in a reactor at 90 degrees C and placed in an oil bath. Hydroxylamine hydrochloride and a base are added at 100 degrees C and reacted. The reaction mixture is solid-liquid separated to obtain an isoxazole compound (I). The molar ratio of alkyne, hydroxylamine hydrochloride, base, and catalyst is 100:100-300:100-300:1-50.    USE - Preparation of isoxazole compound for use in medical field.    ADVANTAGE - The method enables environmentally-friendly one-pot preparation of isoxazole compound under mild reaction conditions, with good compatibility and wide substrate range.    DETAILED DESCRIPTION - A copper catalyst, an organic solvent, and alkynes of formulae: R1-CC-H and R2-CC-H are taken in a reactor at 90 degrees C and placed in an oil bath. Hydroxylamine hydrochloride and a base are added at 100 degrees C and reacted. The reaction mixture is solid-liquid separated to obtain an isoxazole compound of formula (I). The molar ratio of alkyne, hydroxylamine hydrochloride, base, and catalyst is 100:100-300:100-300:1-50.    R1,R2=3-8C alkyl, 3-10C alkoxy, optionally substituted 6-10C aryl, or 3-8C heteroaryl.
NOVELTY - Preparing levetiracetam (Q) comprises: (a) alkylating (S)-2-aminobutyric acid with 4-chlorobutyryl chloride to obtain (S)-2-(4-chlorobutyryl chloride) butyric acid (I); (b) acylating (I) with ethyl chloroformate or methylchloroformate in the presence of acid-binding agent to obtain a reaction solution of mixed anhydride compounds; (c) adding ammoniation reagent into the reaction solution of mixed anhydride to obtain N-((S)-1-carbamoyl-propyl)-4-chloro-butyramide (II); and (d) adding (II) into an organic solvent in the presence of a phase transfer catalyst and alkali.    USE - (Q) is useful for treating epilepsy.    ADVANTAGE - The simple process produces (Q) in high yield, high purity and in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing levetiracetam (Q) comprises: (a) alkylating (S)-2-aminobutyric acid with 4-chlorobutyryl chloride to obtain (S)-2-(4-chlorobutyryl chloride) butyric acid (I); (b) acylating (I) with ethyl chloroformate or methylchloroformate in the presence of acid-binding agent to obtain a reaction solution of mixed anhydride compounds comprising (S)-2-(4-chlorobutanamido)butanoic (methyl carbonic) anhydride and (S)-2-(4-chlorobutanamido)butanoic (ethyl carbonic) anhydride; (c) adding ammoniation reagent into the reaction solution of mixed anhydride to carry out ammonolysis reaction to obtain N-((S)-1-carbamoyl-propyl)-4-chloro-butyramide (II); and (d) adding (II) into an organic solvent to perform cyclization reaction in the presence of a phase transfer catalyst and alkali.
NOVELTY - Harmless fermentation liquid reflux spraying system comprises upper portion set with a spray pipe, spray pipe, spray pipeline is provided with biogas storage tank and inlet port.    USE - The system is useful for disposing biochemical waste (claimed).
NOVELTY - Preparation of 6-methyl pyridine-3-formaldehyde intermediate (I) comprises taking 5-ethyl-2-methyl pyridine (II) as raw material; adding potassium permanganate for oxidation to obtain 5-ethyl-pyridine-2 carboxylic acid (III); adding with chloro sulfoxide compound for methyl esterification to obtain 5-ethyl-2-carboxyl pyridine (IV); adding with sodium borohydride for reduction and alcohol oxidation to obtain 5-ethyl-pyridine-2-ethanol (V); and adding with manganese dioxide to obtain compound (I).    USE - Preparation of 6-methyl pyridine-3-formaldehyde intermediate used for preparing medicine for treating rheumatoid arthritis (claimed).    ADVANTAGE - The method has easy operation, excellent technology performance, low catalyst raw material cost, and is environment friendly.    DETAILED DESCRIPTION - Preparation of 6-methyl pyridine-3-formaldehyde intermediate of formula (I) comprises taking 5-ethyl-2-methyl pyridine (II) as raw material; adding with potassium permanganate for oxidation to obtain 5-ethyl-pyridine-2 carboxylic acid (III); adding compound (III) with chloro sulfoxide compound of formula (RCHSOCl2) for methyl esterification to obtain 5-ethyl-2-carboxyl pyridine of formula (IV); adding compound (IV) with sodium borohydride for reduction and alcohol oxidation to obtain 5-ethyl-pyridine-2-ethanol (V); and adding compound (V) with manganese dioxide to obtain compound (I).    R=1-4C alkyl.
NOVELTY - Synthesizing olanzapine, involves heating reaction mixture of 2-methyl-4-amino-10H-thiene (2,3-b)(1,5) benzodiazepine hydrochloride and N-methyl piperazine to 80-100 degrees C under solvent-free condition for 16 to 24 hours.    USE - For synthesizing olanzapine (claimed), for treating mild anxiety disorder.    ADVANTAGE - The method is simple, convenient to operate, provides high product purity, the yield is more than 90%. The post-processing process in reaction process, does not use any organic solvent, thus reduces the environment pollution and saves the production cost; the reaction temperature is low, avoids the unnecessary impurities, yield of product is high; after the reaction, N-methyl piperazine can be recycled so as to save resource and reduce environment pollution. The method simplifies the processing steps, and used raw materials are easy to obtain, low in cost. The method has no obvious toxicity and has good application value; and is suitable for large scale industrial production.    DETAILED DESCRIPTION - Synthesizing olanzapine, involves heating reaction mixture of 2-methyl-4-amino-10H-thiene (2,3-b)(1,5) benzodiazepine hydrochloride and N-methyl piperazine to 80-100 degrees C under solvent-free condition, and maintaining for 16 to 24 hours under this temperature to synthesize the olanzapine. The mole ratio of the 2-methyl-4-amino-10H-thiene (2,3-b)(1,5) benzodiazepine hydrochloride to the N-methyl piperazine is 1:3-1:12 (preferably 1: 10). The reaction of the 2-methyl-4-amino-10H-thiene (2,3-b) (1,5)benzodiazepine hydrochloride and N methyl piperazine is performed under inert gas protection. The inert gas is nitrogen.
NOVELTY - Synthesis of chlorpyrifos comprises dissolving 1/2-1/3 catalyst of the total catalyst in water as solvent, adding 3,5,6-trichloropyridine-2-sodium alkoxide in solvent, replenishing remaining catalyst, and adding ethyl chloride to obtain chlorpyrifos.    USE - Method for synthesizing chlorpyrifos (claimed).    ADVANTAGE - The solvent of the method can be reused after precipitating and cooling; and the method is energy saving, environment-friendly and easy, has low cost and is suitable for industrial production.
NOVELTY - Cis-1-halo-2-chloro olefin compounds (I) are new.    USE - (I) are useful in the preparation of polysubstituted aromatic hydrocarbon, trisubstituted olefin or a compound containing a trisubstituted olefin structural unit, where the polysubstituted aromatic hydrocarbon is 1,2-ethyl dicarboxylate-4-chloro-5,6,7,8-tetrahydronaphthalene, the trisubstituted olefin is (Z)-4-phenyl-p-tolyl-1-phenyl-3-alkenyl-1-yne, and the compound containing a trisubstituted olefin structural unit is vitamin A (all claimed).    ADVANTAGE - (I) can be produced in a simple, economical and environmentally friendly manner.    DETAILED DESCRIPTION - Cis-1-halo-2-chloro olefin compounds of formula (Cl-C(R)=C(X)-H) (I) are new.    R = phenyl (optionally mono, di or tri-substituted by alkyl, alkoxy, F, Cl or Br), 1-naphthyl, 2-naphthyl, thienyl, furyl, alkenyl, styryl, benzyloxy methylene or alkyl (optionally substituted with heteroatom); and    X = Cl or Br.    INDEPENDENT CLAIMS are included for:    (1) for the preparation of (I); and    (2) the preparation of vitamin A comprising reacting tert-butyl-((2E,4E)-5-iodo-3-methyl-penta-2,4-dienyloxy)-dimethyl-silane (XIII) with tert-butyl lithium in an organic solvent for half an hour at -78 degrees C, reacting the obtained reaction mixture with anhydrous zinc chloride for half an hour at 0 degrees C, reacting the obtained mixture with tetrakis(triphenylphosphine)palladium catalyst and 2-((1E,3Z)-3-chloro-4-bromo-1,3-butadienyl)-1,3,3-trimethyl cyclohexene (XII) for 8-12 hours at 20-60 degrees C, adding dimethyl zinc into the reaction mixture and reacting for 3-5 hours at 40-60 degrees C, adding and stirring tetrabutyl amine fluoride into reaction mixture for 1.5-3 hours at 15-38 degrees C and performing post-treatment for preparing the vitamin A.
NOVELTY - The composite pig feed additive comprises 9 parts by weight (pbw) of Paeonia alba, 10 pbw of rhizoma anemarrhenae, 5 pbw of Cassia twig, 15 pbw of Astragalus mongholicus, 9 pbw of Angelica sinensis, 9 pbw of radix angelicae pubescentis, 6 pbw of radix clematidis, 8 pbw of Tripterygium wilfordii, 5 pbw of Polygonum multiflorum, 13 pbw of Saccharomyces, 1.5 pbw of cellulose, 8 pbw of nicotinic acid, 3 pbw of D-calcium pantothenate, 1.5 pbw of riboflavin, and 1 pbw of vitamin A acetic ester.    USE - The composite pig feed additive is useful for treating edema in pig, and improving immunity of the pig.    ADVANTAGE - The composite pig feed additive can be economically and safely prepared with high quality and efficiency in an environmentally friendly manner, and improves the stress resistance and breeding effect of the swine.    DETAILED DESCRIPTION - The composite pig feed additive comprises 9 parts by weight (pbw) of Paeonia alba, 10 pbw of rhizoma anemarrhenae, 5 pbw of Cassia twig, 15 pbw of Astragalus mongholicus, 9 pbw of Angelica sinensis, 9 pbw of radix angelicae pubescentis, 6 pbw of radix clematidis, 8 pbw of Tripterygium wilfordii, 5 pbw of Polygonum multiflorum, 13 pbw of Saccharomyces, 1.5 pbw of cellulose, 8 pbw of nicotinic acid, 3 pbw of D-calcium pantothenate, 1.5 pbw of riboflavin, 1 pbw of vitamin A acetic ester, 0.6 pbw of vitamin D3 microparticles, 2 pbw of L-ascorbic acid, 3.5 pbw of L-lysine hydrochloride, 1 pbw of L-tryptophan, 13 pbw of threonine, 40 pbw of adhesive, and 876 pbw of carriers. The carriers are mixture of corncob powder and bran in a mass ratio of 4:6. The adhesive is guar gum.
NOVELTY - Disclosed is an environmentally-friendly and improved process for the preparation of imatinib and its pharmaceutically acceptable acid addition salts. Image 0/0
NOVELTY - Thiazole organic copper compound (I), is new.    USE - (I) is useful for preventing the bacterial disease such as Xanthomonas oryzae and Phomopsis hulianthi, and fungal disease such as rust disease, Rhizoctonia solani, leaf spot disease, withered disease, Sclerotinia sclerotiorum and stem blight of agricultural plant, where the agricultural plant comprises crop, fruit tree or vegetable, the crop comprises rice, wheat, corn, soybean, cotton, peanut, watermelon, rapeseed or sesame, the vegetable comprises tomato or cucumber and the fruit tree comprises apple tree, pear tree or peach tree (all claimed). No biological data given.    ADVANTAGE - (I) can be prepared with less time and energy consumption in a simple, economical and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Preventing scab of nitrophosphate fertilizer calcium nitrate crystallizer freezing coil, involves: defluorinating phosphoric acid cleaning liquid by separating acid insoluble substance of phosphoric acid cleaning liquid; adding defluorination agent to the calcium nitrate crystal feed tank with stirring at normal pressure; arranging depositing room between the calcium nitrate crystal feed tank and calcium nitrate crystallizer for separating deposit formed in the defluorination reaction; and sending the defluorinated phosphoric acid cleaning liquid to calcium nitrate crystallizer.    USE - For preventing scab of nitrophosphate fertilizer calcium nitrate crystallizer freezing coil (claimed).    ADVANTAGE - The method has simple operation and is easy to carry out, the treatment effectively avoids the scar of crystallizer calcium nitrate refrigerating coil, so, it saves the energy and improves the operating rate, and introduction of defluorination agent will not bring secondary pollution to system.    DETAILED DESCRIPTION - Preventing scab of nitrophosphate fertilizer calcium nitrate crystallizer freezing coil, involves: carrying out defluorination treatment of phosphoric acid cleaning liquid by separating the acid insoluble substance of phosphoric acid cleaning liquid; adding defluorination agent to the calcium nitrate crystal feed tank with stirring at the normal pressure; arranging a depositing room between the calcium nitrate crystal feed tank and the calcium nitrate crystallizer for separating the deposit formed in the defluorination reaction; and sending the defluorinated phosphoric acid cleaning liquid to the calcium nitrate crystallizer; where the defluorination agent is mixture of phosphate and sodium hexamethane phosphate or sodium nitrate and sodium hexamethane phosphate, in weight ratio of 1:1.
NOVELTY - A penam diphenylmethyl ester sulfoxide is prepared by adding 420 kg 6- alpha -bromo penicillanic acid, 2000 kg tetrahydrofuran and 800 kg water in a reaction kettle; adding 120 kg peracetic acid at 0-10 degrees C while stirring, after reacting for 1 hour, and adding 42 kg composite metal oxide solid alkaline catalyst; and adding 110 kg zinc powder in three batches to react for 1-5 hours, and filtering the catalyst and zinc powder solid matters.    USE - Method for the preparation of penam diphenylmethyl ester sulfoxide (claimed).    ADVANTAGE - The method has simple operation, good technique property and free from environment pollution.    DETAILED DESCRIPTION - Preparation of penam diphenylmethyl ester sulfoxide of structure (I) comprises:    (A) adding 420 kg 6-~-bromo penicillanic acid, 2000 kg tetrahydrofuran and 800 kg water in a reaction kettle;    (B) adding 120 kg peracetic acid at 0-10 degrees C while stirring, after reacting for 1 hour, and adding 42 kg composite metal oxide solid alkaline catalyst;    (C) adding 110 kg zinc powder in three batches to react for 1-5 hours, and filtering the catalyst and zinc powder solid matters;    (D) utilizing 100 kg of tetrahydrofuran to wash the solid matters;    (E) mixing tetrahydrofuran phase;    (F) utilizing saturated salt water to wash, heating, removing the aqueous layer, drying tetrahydrofuran solution by anhydrous sodium sulfate, decompressing and condensing; and    (G) utilizing ethyl acetate to recrystallize to obtain a solid target product.
NOVELTY - Method for modifying humic acid, involves (a) adding humic acid to alkaline solution, adjusting pH to 9-11, and adding alkylating agent to solution, performing alkylation reaction at 65-85 degrees C to obtain alkylated humic acid, where the alkylating agent is halogenated alkane, and (b) adding sulfomethylated agent to obtained solution, performing sulfomethylation reaction at 60-100 degrees C, and performing post-treatment process to obtain modified humic acid.    USE - The method is useful for modifying humic acid which is useful for remediating contaminated soils (all claimed).    ADVANTAGE - The method is simple, and easy to operate. The modified material has higher surface tension, and hydrophilic-lipophilic balance, and is environmentally-friendly.
NOVELTY - Compost rod comprises (in %): fermented sawdust (45), adhesive (10) and gunny bags, where peripheral portion of compost rods are adhered to gunny bags.    USE - The compost rod is useful for planting trees (claimed), and arboriculture.    ADVANTAGE - The compost rod facilitate moisture absorption in trees, and has excellent intensity and permeability, and is simple and cost-effective.
NOVELTY - Carbon dioxide determination involves processing material with ammonia in a reactor in order to produce ammonium bicarbonate fertilizer, which is utilized to determine carbon dioxide amount in soil.    USE - Method for determining carbon dioxide.    ADVANTAGE - The carbon dioxide determining method enables to provide eco-friendly and cost-effective process.
NOVELTY - Method involves mixing of sugar beet pulp and a defecate by their distribution on the surface of the soil at a ratio of (1-2):(1-1.5), providing pH of the resulting mixture of 6.8-7.0, in an amount of 12-20 t/ha, then the processing of the mixture by the culture Trichoderma viride, strain 98 or 838, with the norm of the introduction of 5 l/ha and uniform embedding in the soil to a depth of 7-10 cm.    USE - Agriculture.    ADVANTAGE - Creation of a favorable phytosanitary condition and increase of soil fertility in beet-seed crop rotation. 2 cl, 5 tbl
NOVELTY - Clay-based xanthogenate (I) is new. The crystal structure of (I) comprises clay-based dithiocarbonate functional groups (II) and clay-based hydroxides (III). The dithiocarbonate groups are grafted on the mineral clay crystal structures form clay-based xanthogenate, clay-based bis(xanthogenate) and/or clay-based multi-xanthogenate.    USE - (I) is useful as heavy metal ion flocculating agent in the fields of waste water treatment, soil remediation, wet process metallurgy, environment protection and ecological construction (claimed).    ADVANTAGE - (I) has simple, easy, fast and convenient operation, has high metal ion removal rate and easy solid-liquid separation; is environmental friendly. The method is simple, feasible, economical and suitable for industrial production.    DETAILED DESCRIPTION - Clay-based xanthogenate of formula ((HO)m-n-A-(O-C(=S)-S-)(n/i)M(i+)) (I) is new. The crystal structure of (I) comprises clay-based dithiocarbonate functional groups of formula (A-O-S(=O)-S-) (II) and clay-based hydroxides of formula (A-(OH)n) (III). The dithiocarbonate groups are grafted on silicate mineral clay crystal structures form clay-based xanthogenate, clay-based bis(xanthogenate) and/or clay-based multi-xanthogenate.    A = clay;    m, n, i = nonzero integers;    m = greater than or equal to n; and    M(i+) = Na+ or K+.    An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - Preparation of 3-(2(dimethylamino) ethyl)-N-methyl indole-5-methane sulfonamide succinate (I) comprises carrying out condensation reaction of 3-(2-ethyl)-N-methyl-IH-indole-5-methane sulfonamide (II) with aqueous formaldehyde solution in ammonium carbonate and methanol; without separating intermediate product, directly carrying out catalytic hydrogenation reduction using palladium/carbon catalyst; recovering the solvent, reacting with succinic acid; and when the reaction liquid is clear, adding activated carbon, and decoloring.    USE - Method for the preparation of 3-(2(dimethylamino) ethyl)-N-methyl indole-5-methane sulfonamide succinate (I) (claimed) used in pharmaceutical preparation.    ADVANTAGE - The method is stable, is environment-friendly, and is inexpensive.    DETAILED DESCRIPTION - Preparation of 3-(2(dimethylamino) ethyl)-N-methyl indole-5-methane sulfonamide succinate (I) comprises:    (A) carrying out condensation reaction of 3-(2-ethyl)-N-methyl-IH-indole-5-methane sulfonamide (II) with aqueous formaldehyde solution in ammonium carbonate and methanol;    (B) without separating intermediate product, directly carrying out catalytic hydrogenation reduction to obtain 3-(2(dimethylamino) ethyl)-N-methyl indole-5-methane sulfonamide (III) using palladium/carbon catalyst;    (C) recovering the solvent by post-processing, reacting with succinic acid for salt-forming reaction in deionized water; and    (D) when the reaction liquid is clear, adding activated carbon, and decoloring.
NOVELTY - Extracting and purifying of jackfruit xanthene ketone comprises taking tree bark as raw material, crushing and adding in extraction kettle, using supercritical carbon dioxide (CO2) extraction, acetone or ethanol as entrainer, extracting for 2-4 hours, and analyzing extraction liquid recycling reagent to obtain extract; adding extract and ethanol-water phase system, heating and uniformly mixing; and putting concentrated extract into glucose gel column, n-hexane-acetone eluting, decompressing and recycling reagent to obtain concentrated solution.    USE - Method for extracting and purifying of jackfruit xanthene ketone (claimed).    ADVANTAGE - The method has high extraction rate, low cost, and small environment pollution.    DETAILED DESCRIPTION - Extracting and purifying of jackfruit xanthene ketone comprises:    (A) taking tree bark as raw material, crushing and adding in extraction kettle, using supercritical carbon dioxide (CO2) extraction, acetone or ethanol as entrainer, extracting for 2-4 hours, and analyzing extraction liquid recycling reagent to obtain extract;    (B) adding extract and ethanol-water phase system, heating and uniformly mixing (and is divided into upper and lower end), where lower phase, crystal and ammonium sulfate crystal, adding ethyl acetate, adding water and sodium chloride, and uniformly mixing;    (C) putting concentrated extract into glucose gel column, n-hexane-acetone eluting, decompressing and recycling reagent to obtain concentrated solution; and    (D) mixing concentrated solution with petroleum ether-acetone and repeatedly recrystallizing jackfruit amlexanoxton.
NOVELTY - The method involves gasifying methanol to prepare dimethyl ether on which dehydration and condensation reaction are performed to obtain hydrocarbon component. The hydrocarbon product is passed to oil-water separator. The separated product is entered into ammonia cooler before passing another oil-water separator. The product is entered into absorption tower of drying apparatus for obtaining liquid product with oxygen content of more than 2.0%. The rest absorbed gaseous hydrocarbon product is entered into gas circulating machine. The reaction product is moved to alkylation reactor.    USE - Method of manufacturing hydrocarbon fuel from methanol.    ADVANTAGE - The hydrocarbon fuel can be manufactured from the methanol thorough simple technique at low cost. The number of processes required for manufacturing the hydrocarbon fuel is reduced. The hydrocarbon fuel can be manufactured safely, without causing pollution to the environment. The production efficiency of the hydrocarbon fuel is improved. The need of performing hydrogenation, isomerization and fractionation on the obtained product is eliminated, thus the applicability of the hydrocarbon fuel manufacturing technique in industry is improved.    DETAILED DESCRIPTION - gasifying methanol after pre-heating to prepare dimethyl ether. The dehydration and condensation reaction are performed on dimethyl ether to obtain hydrocarbon component.
NOVELTY - Method of processing hydrocarbon material via high-temperature fractionation involves feeding hydrocarbon material (hydrocarbon fractions) into a fractionation column with bottom heater and outlet of commercial-grade high-boiling fraction(s) from the bottom, units for outlet of fractionation gases from the top part and obtaining reflux liquid for reflux of the top of the column, a unit for outlet of calculated commercial-grade excess low-boiling fraction(s). Said method is characterised by that the reflux unit is fitted with a cooler (recuperator, recuperator-evaporator) for further cooling of the reflux liquid with control of its temperature from 12 degrees C to minus 1 degrees C from the initial temperature of reflux liquid before the cooler (recuperator, recuperator-evaporator) to the further cooling process, directly before feeding said reflux liquid for reflux.    USE - Chemistry.    ADVANTAGE - Invention increases propane extraction ratio, as well as the feed rate of de-ethaniser columns and other high-temperature columns. 5 cl, 6 tbl, 6 dwg
NOVELTY - A single acyl ferrocene Schiff base iron amino ring phosphorus nitrile compound (I) is new.    USE - Single acyl ferrocene Schiff base iron amino ring phosphorus nitrile compound for use in electrochemical, medical, catalyst and lubricating field.    ADVANTAGE - The nitrile compound has wide application value, and can be prepared in simple, safe and cost-effective manner.    DETAILED DESCRIPTION - A single acyl ferrocene Schiff base iron amino ring phosphorus nitrile compound of formula (I) is new.    R1=-(NH)-R8-N-C(R)(C5H4FeC5H4);    R2-R6=-(NH)-R8-N=C(R)(C5H4FeC5H4) or Cl;and    R8=CH2CH2, phenylene, biphenylene, C6H4-CH2-C6H4, C6H4-O-C6H4 or C6H4-SO2-C6H4; and    R = H, 1-3C alkyl or phenyl.
NOVELTY - A plant to carry out the semi-continuous type fermentation process of molasses and non-molasses materials, is disclosed. Molasses is a by-product in sugar processing industry. In most of the cases, molasses is used for producing ethyl alcohol by fermenting the sugar contents in the molasses. To accomplish this fermentation, the molasses is subjected to bio-chemical reaction in tanks or vessels known as fermentors using micro-organisms such as yeast as the fermenting medium. The quantity of molasses handled is pretty large, hence it is necessary to provide multiple units to fermentors. Image 0/0
NOVELTY - Organic-type industrial waste is processed by performing continuous fermentation of fermented material (2) which contains organic-type industrial waste having heavy metal as main material, wherein gas generated during fermentation process is discharged from fermenter (1), injecting new fermented material multiple times with respect to fermenter in the middle of fermentation process, stirring fermented material, extracting fermented or decomposed material from fermenter after evaporation of water contained in fermented material, and concentrating heavy metal in fermented or decomposed material.    USE - Processing method of organic-type industrial waste e.g. fish waste, agricultural waste, livestock farming waste, or food processing waste (all claimed).    ADVANTAGE - The processing method of organic-type industrial waste is simple, effectively performs fermentation process without the need for a special microbe or fuel, and reduces processing costs and energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a processing system which applies the processing method of organic waste.    Fermenter (1)    Fermented material (2)    Input apparatus (3)    Stirring apparatus (4)    Deodorizing apparatus (5)
NOVELTY - A bamboo pellet fuel is manufactured by crushing process which obtains mixed powder of bamboo base (7) from crushed and ground withering bamboo (4) with moisture content of less than or equal to 55% with respect to 100 wt.% of green bamboo (2) with removed branches-and-leaves part, drying process which dries mixed powder of bamboo base, and granulation process which granulates dried mixed powder of bamboo base using granulator and obtaining bamboo pellet.    USE - Manufacture of bamboo pellet fuel.    ADVANTAGE - High heat generation is favorable. Acceleration of fermentation and production of fungi are eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the manufacture procedure of the bamboo pellet fuel. (Drawing includes non-English language text).    Green bamboo (2)    Withering bamboo (4)    Crusher and grinder (6)    Mixed powder of bamboo base (7)    Sieve (8)
NOVELTY - Formaldehyde content of wood vinegar, which is a water-soluble distillate obtained when woody biomass is thermally decomposed, is reduced by alkali addition process performed by adding alkali to wood vinegar.    USE - Reduction method of formaldehyde content of wood vinegar for manufacture of wood vinegar (claimed) used in soil improvement, disease and insect damage extermination, growth promotion, bathwater additive, deodorizer, and minimum-risk pesticide.    ADVANTAGE - Formaldehyde in wood vinegar is simply and efficiently reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of wood vinegar.    DESCRIPTION OF DRAWING(S) - The drawing shows a reaction mechanism of the formaldehyde reduction process. (Drawing includes non-English language text).
NOVELTY - The method involves performing biomass pretreatment in biomass gasification furnace. The biomass in the gasification furnace is heated using external heat source at the reaction temperature of 1300 degrees C and 1750 degrees C. The liquid slag is cooled by quench tower and heat recovery boiler. The fresh gas is obtained in the gas storage cabinet by de-dusting. The negative pressure or positive pressure to 50KPa is maintained. The gasifying medium adopts single air, oxygen-enriched air, and pure oxygen.    USE - Method for performing gasification of biomass or raw coal.    ADVANTAGE - The quality of the crude gas is improved. The structure of gasification furnace is simple, and easy to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass gasification device.    Raw material pre-processing and storage unit (1)    Biomass feeding unit (2)    External heat source unit (3)    Gasification furnace unit (4)    Thick gas cooling unit (5)
NOVELTY - Regenerated hydrocracking catalyst is obtained by regenerating used hydrocracking catalyst comprising carrier containing zeolite and amorphous composite metal oxide having solid acidity, and at least one type of active metal chosen from noble metals of group 8-10 of periodic table and supported on carrier with respect to total mass of catalyst, where the hydrocracking catalyst comprises 0.05-1 %mass of carbonaceous material with respect to carbon atoms.    USE - The regenerated hydrocracking catalyst is useful for manufacturing hydrocarbon oil (all claimed).    ADVANTAGE - The produced oil is cost-effective and has high yield for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing hydrocarbon oil, which involves contacting raw material oil containing 70 %mass or more of linear aliphatic hydrocarbons having boiling point of greater than 360 degrees C with hydrocracking catalyst under coexistence of molecular hydrogen.
NOVELTY - The apparatus comprises a reactor (102) for receiving waste material, a mixer for mixing the material with a liquid such as water, a skimmer (3) for removing a portion of the waste material having similar or lighter density than the liquid, a settler (1) for removing a portion of the waste material having higher density than the liquid, and a diffuser (7) for blowing gas micro-bubbles into the reactor. A portion of the waste material comprises organic and non-bio organic waste materials and an inorganic waste material. The gas is methane. The reactor comprises anaerobic bacteria.    USE - The apparatus is useful for separating a waste into organic and inorganic material for producing biogas, where the waste is generated on a daily basis by organizations and households.    ADVANTAGE - The apparatus efficiently removes non bioorganic matter from the waste.    DETAILED DESCRIPTION - The apparatus comprises a reactor (102) for receiving waste material, a mixer for mixing the material with a liquid such as water, a skimmer (3) for removing a portion of the waste material having similar or lighter density than the liquid, a settler (1) for removing a portion of the waste material having higher density than the liquid, and a diffuser (7) for blowing gas micro-bubbles into the reactor. A portion of the waste material comprises organic and non-bio organic waste materials and an inorganic waste material. The gas is methane. The reactor comprises anaerobic bacteria. The waste material comprises less than 2-8wt.% of solids. An INDEPENDENT CLAIM is included for a process for separating waste material.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of an apparatus for separation of waste.    Settler (1)    Skimmer (3)    Diffuser (7)    Biogas blower (8)    Reactor. (102)
NOVELTY - Capturing carbon from the atmosphere, comprises cultivating green plants, harvesting the plants, processing the harvested plants into food for shell-bearing gastropods and green waste, feeding the food to gastropods until maturity, harvesting the mature gastropods and separating the shells from the bodies, processing the bodies to obtain protein or fuel and processing the shells for use as a construction material.    USE - The method is useful for capturing carbon from the atmosphere, producing protein for animal or fish feed, and producing a liquid or gaseous fuel (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an installation for cultivating shell-bearing gastropods, comprising food-processing apparatus for receiving green plant material and for separating the material into food for the gastropods and plant waste, containment means for containing the gastropods, feeding means for supplying the food to the gastropods at a controlled rate conducive to growth of the gastropods, means for harvesting gastropods from the containment means and processing means for processing the harvested gastropods to obtain protein or fuel and shells for use as a construction material.
NOVELTY - A starch manufacture waste water is stored in a tank by adding lactic acid bacteria to starch manufacturing waste water.    USE - Storage process of starch manufacture waste water in a tank.    ADVANTAGE - The pH of starch manufacture waste water is reduced without adding acids. Magnesium ammonium phosphate production is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the experimental result. (Drawing includes non-English language text).
NOVELTY - The system (1) has a fuel tank (2) storing fuel i.e. liquid hydrocarbon mixture, and a reactor (3) for reforming the mixture from the fuel tank into gas containing hydrogen. A heating device (4) heats the mixture supplied to the reactor. A fuel supply line (6) feeds the mixture to the reactor. A discharge line supplies the gas containing hydrogen from the reactor to a fuel cell (5), and the reactor is designed to process a synthetic fuel, which is manufactured from biomass or bio-oil. The reactor is designed to implement partial dehydrogenation.    USE - Fuel cell system for use in an aircraft (claimed) i.e. airplane, for generating electrical power.    ADVANTAGE - The system uses the liquid hydrocarbon mixture produced from bio-oil as the fuel instead of kerosene, thus preventing accumulation of coke on a catalyst surface of the reactor, and hence improving the service life of the reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system for an aircraft.    Fuel cell system (1)    Fuel tank (2)    Reactor (3)    Heating device (4)    Fuel cell (5)    Fuel supply line (6)
NOVELTY - A photoelectrochemical cell (20) comprises a p-type sensitized photocathode (24) including sensitizer (22), and an electrolyte.    USE - Photoelectrochemical cell e.g. photoelectrochemical water-splitting device and device for chemical transformation of feedstock.    ADVANTAGE - The photoelectrochemical cell has high efficiency, increased overall spectral response, and is economical and does not pollute the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of photoelectrochemical cell.    Photoelectrochemical cell (20)    Sensitizer (22)    Sensitized photocathode (24)    Light (26)    Water (28)    External circuit (30)
NOVELTY - The emission control method involves producing a methane conversion temperature that corresponds predetermined methane conversion efficiency. The power is selectively applied to a substrate of an electrically heated catalyst based on a temperature of the electrically heated catalyst and the methane conversion temperature. The electrically heated catalyst has a catalyst which reacts with methane in the exhaust gas that circulated by an engine (102). The catalyst has platinum, rhodium and palladium.    USE - Emission control method.    ADVANTAGE - The emission control method involves producing a methane conversion temperature that corresponds predetermined methane conversion efficiency, where the power is selectively applied to a substrate of an electrically heated catalyst based on a temperature of the electrically heated catalyst and the methane conversion temperature, and thus ensures improved efficiency of the emission control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an engine system.    Vehicle system (100)    Engine (102)    Intake manifold (110)    Throttle valve (112)    Engine control module (114)
NOVELTY - Bamboo charcoal-photosynthetic bacteria integrated municipal wastewater treating agent is prepared by concentrating 3-5 times of the photosynthetic bacteria nutrient solution, adjusting pH value to 4.0-5.0, adding activated bamboo charcoal crushed into 5-10 meshes, adsorbing for 4-5 hours at 80-100 revolutions/minute (rpm) at 30-40 degrees C, filtering to obtain the product. Adding amount of activated bamboo charcoal is 15-25 g/100 ml of photosynthetic bacteria nutrient solution.    USE - A bamboo charcoal-photosynthetic bacteria integrated municipal wastewater treating agent useful for dislodging and disposal of organics and ammonia nitrogen in municipal wastewater.    ADVANTAGE - The treating agent has low cost in municipal wastewater disposal, less covering, and little sludge production; and has obvious economic benefits, environmental benefits, and social benefits. Chemical oxygen demand (COD) value and ammonia nitrogen content of the municipal wastewater are effectively reduced.
NOVELTY - Use of Stenotrophomonas maltophilia (DS4) in degrading organic contaminants of saponin wastewater, is claimed.    USE - The Stenotrophomonas maltophilia DS4 is useful for degrading organic contaminants of saponin wastewater (claimed).    ADVANTAGE - The Stenotrophomonas maltophilia DS4 has stronger growing ability, has high removal rate of organic contaminants in saponin wastewater (62.34%), and removes chemical oxygen demand (2930 mg/l) in saponin wastewater within 72 hours.
NOVELTY - The method involves concentrating sludge (5) to predetermined moisture content by using concentration device (4). The sludge is circulated for predetermined amount of time between hydrothermal reactor (11) and gas-liquid separator (12) to reduce molecular weight of sludge, while heating to hydrothermal temperature at 160-200 degrees C to maximize amount of methane gas recovered per unit amount of sludge resulting from methane fermentation process. The low molecular weight sludge is retained for 3-5 days in methane fermentation tank (20), and methane gas (G) is recovered.    USE - Method for processing methane fermentation in sludge, used in waste water treatment field.    ADVANTAGE - The methane fermentation processing is efficiently performed to increase the amount of methane gas recovered from sludge which is previously processed by hydrothermal reactions. The energy efficiency of the whole system combining hydrothermal reactor and methane fermentation tank can be improved, while reducing the size and weight of the system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for processing methane fermentation in sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for processing methane fermentation in sludge.    Concentration device (4)    Concentrating sludge (5)    Hydrothermal reactor (11)    Gas-liquid separator (12)    Methane fermentation tank (20)    Methane gas (G)
NOVELTY - The fuel cell module has a heat transmission unit (50) that is configured so that an interfacial boundary is formed between regions in a heat-insulating section (122). The heat generated in a fuel cell (12) is transmitted to a fuel accommodation section (60), when the fuel cell is below a predetermined temperature. The heat generated in fuel cell and fuel accommodation section is released outside of the fuel cell and fuel accommodation section from thermal-radiating section (120), when the fuel cell is at or above a predetermined temperature.    USE - Fuel cell module for portable apparatus. Uses include but are not limited to mobile telephone, notebook-type personal computer, personal digital assistant (PDA), MPEG audio layer-3 player, digital camera, electronic dictionary and electronic book.    ADVANTAGE - The temperature of the fuel cell and the fuel accommodating section can be appropriately controlled. The temperature of the membrane electrode assembly and the fuel accommodating section can be adjusted in a simply appropriate range.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.(Drawing includes non-English language text)    Fuel cell (12)    Heat transmitting unit (50)    Fuel accommodation section (60)    Thermal-radiating section (120)    Heat-insulating section (122)
NOVELTY - The apparatus has reformer temperature detector (25) which detects temperature of reformer (6). A transformer (7) is arranged downstream of reformer and is configured so as to be heated using combustion gas that results from heating reformer. A transformer temperature detector (26) is provided to detect temperature of transformer. A controller (33) is provided to control air supplier (14) so as to increase flow rate of air for combustion when temperature of transformer detected by transformer temperature detector falls below predetermined threshold temperature.    USE - Hydrogen generating apparatus for fuel cell system.    ADVANTAGE - Since the controller is provided to control air supplier so as to increase flow rate of air for combustion when temperature of transformer falls below predetermined threshold temperature, the decrease in energy efficiency, electric power consumption and fuel consumption can be effectively reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus.    Reformer (6)    Transformer (7)    Air supplier (14)    Reformer temperature detector (25)    Transformer temperature detector (26)    Controller (33)
NOVELTY - Preparation of a microbial organic fertilizer comprises using (kg) rice straw (650), animal waste (200), a pond sludge (150), effective microorganism (EM) strain (2), sugar (3), and water (1000-1200).    USE - Method for the preparation of a microbial organic fertilizer (claimed).    ADVANTAGE - The raw materials have wide range of resources with low cost. The method is simple. The fertilizer has high content of beneficial bacteria, increases soil organic matter, improves soil structure, accelerates the soil microbial activities, and enhances nutrient-keeping and the nutrient-supply of soil. It increases the crop yield, and reduces the use of chemical fertilizer.
NOVELTY - Fertilizer is produced using industrial and municipal sludge by concentrating sludge discharged from industrial and municipal sludge plant with 80-85% water content to concentration of 2000-50000 mg/l muddy water; collecting stored muddy water and separating mud from water; concentrating and dehydrating sludge; drying the sludge; sterilizing the sludge at 80-90 degrees C; adding additives according to different conditions of soil and different requirement of crops, stirring and mixing; preparing the mixed materials into particles; and drying the particles to 20% water content.    USE - Method of producing fertilizer using industrial and municipal sludge (claimed).    ADVANTAGE - The method is simple and can recycle heat energy in the drying process.    DETAILED DESCRIPTION - Production of fertilizer using industrial and municipal sludge comprises:    (A) concentrating sludge discharged from industrial and municipal sludge plant with 80-85% water content to concentration of 2000-50000 mg/l muddy water;    (B) collecting stored muddy water, and lifting by a screw sludge pump to a rotational flow reactor to separate mud from water;    (C) concentrating and dehydrating sludge;    (D) drying the concentrated and dehydrated sludge to 40% water content, and using steam, hot water and conduction oil as a heating medium, heating and drying the sludge in a conductive heating way;    (E) sterilizing the sludge at 80-90 degrees C;    (F) adding additives according to different conditions of soil and different requirement of crops, stirring and mixing the dried sludge having 20% water content with the additives;    (G) stirring and preparing the mixed materials into particles; and    (H) drying the particles to 20% water content.
NOVELTY - A bio-organic fertilizer is prepared by using municipal sludge by inoculating the traditional Chinese medicine microbial inoculants in the following raw materials with the mixing ratio by weight and fermenting: municipal sludge (30-70 parts), Eupatorium adenophorum preng (10-40 parts), turf (10-30 parts), waste flue-cured tobacco (3-10 parts), bacterium residue (3-10 parts), and coal ash (0-10 parts).    USE - As bio-organic fertilizer (claimed).    ADVANTAGE - The bio-organic fertilizer can use the organic matter, and nitrogen, phosphorus and potassium in the raw materials fully, and lets the heavy metal in the sludge perform passivation to meet the farm-oriented standard, and the product has the functions of developing land, improving fertility, and developing plant roots microbiology environment and improving the quality of crops and increasing production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the bioorganic fertilizer involving mixing uniformly municipal sludge (30-70 parts), Eupatorium adenophorum preng (10-40 parts), turf (10-30 parts), waste flue-cured tobacco (3-10 parts), bacterium residue (3-10 parts), and coal ash (0-10 parts), adjusting the water content of the mixture to 55-65%, and obtaining the compost; inoculating the traditional Chinese medicine microbial inoculants in the compost, mixing culture and the compost fully; the inoculation amount of the traditional Chinese medicine microbial inoculants is 0.3-1% of the total weight of ingredients; and letting the compost after inoculating ferment until the water content of the compost is 18-30%, the content of the active microorganism in the compost is more than 20 million/g.
NOVELTY - The system (150) has multistage refrigerant compressor that compresses refrigerant from flue gas chiller and CO2 condenser (164,170). The refrigerant condenser condenses compressed refrigerant. A refrigerant chiller (180) chills portion of condensed refrigerant using liquid CO2 separated in CO2 condenser. A flue gas chiller (160) chills flue gas stream using portion of chilled condensed refrigerant at expansion pressure. The CO2 condenser condenses and separates portion of CO2 from the chilled flue gas stream using portion of chilled condensed refrigerant.    USE - Refrigeration system for condensation of carbon dioxide (CO2) in flue gas stream.    ADVANTAGE - The auto-refrigeration systems is provided to require extensive efforts to remove harmful components in the flue gas upstream of the CO2 condensation. The pressure of the condensed CO2 is used for chilling of the condensed external refrigerant is kept sufficient so as to prevent evaporation of the condensed CO2 during the chilling.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) flue gas treatment system for removing CO2 from flue gas stream; and    (2) method for condensation of carbon dioxide (CO2) in flue gas stream using circulating stream of external refrigerant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schemtaic view of the refrigeration system.    Co2 separation system (140)    Refrigeration system (150)    Flue gas chiller (160)    Co2 condenser (164,170)    Refrigerant chiller (180)
NOVELTY - Production of biodiesel, involves (a) providing lamb fat in a supercritical carbon dioxide carrier, and (b) reacting the lamb fat in the supercritical carbon dioxide carrier with 1-5C alcohol or 1-5C ester in the presence of a lipase catalyst.    USE - The method is useful for production of biodiesel (claimed).    ADVANTAGE - The biodiesel is available from renewable resources and has a less negative environmental impact than fossil fuels. The method using 1-5C alcohols and 1-5C esters, has faster reaction rate than existing catalyzed methods, easy product purification and possibility of using inexpensive, unrefined feedstock material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) integrated reactor system; and    (2) biodiesel obtained by the above-cited method.
NOVELTY - The system comprises three continuous working units of feeding unit, pyrolytic reaction unit and discharging unit, and a pyrolytic reaction controlling system. The pyrolytic reaction unit comprises pyrolytic reaction body having screw propulsion unit and air blowing device. The discharging unit comprises a screw discharging device and air transporting system. The pyrolytic reaction body is rectangle cavity with metal shell. The cavity of pyrolytic reaction body is divided into up and down two separable parts.    USE - System for preparing biomass gas and biomass charcoal.    ADVANTAGE - The system effectively separates the metal shell and the high temperature reaction medium; decreases the heat resistance of the cavity material of pyrolytic reaction body; lowers the cost for using the ordinary steel material; effectively relieves the temperature distortion of the metal shell; and reduces the heat loss. It is easy to take down the easily damaged part in the bottom of the reaction body for dividing the pyrolytic reaction body into upper and lower parts. The system is convenient for maintaining and changing.
NOVELTY - Microorganisms transduced with gene encoding enzyme for xylose metabolism and not comprising genes encoding glycine synthesis system protein, and/or methionine synthesis system protein, are new.    USE - The microorganisms, preferably yeast, more preferably Saccharomyces cerevisiae are useful for manufacturing ethanol (all claimed) which is used as fuel.    ADVANTAGE - The microorganisms have outstanding xylose fermentation ability, produce ethanol rapidly and efficiently from biomass having low amino acid content compared to wild type strains, and produce low amounts of by-products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing ethanol, which involves contacting the above-mentioned microorganisms with xylose containing raw material.
NOVELTY - Composition (I) comprises: a lithium cocrystal composition or its solvate or hydrate, where the lithium cocrystal composition comprises a lithium salt and a neutral organic molecule in a stoichiometric ratio.    USE - (I) is useful for: treating suicidality and other disorders that require lithium to penetrate the blood brain barrier and exert therapeutic effects in the CNS; and preparation of pharmaceuticals, or for commercial/industrial uses such as green chemistry (synthesis of polymers and specialty chemicals), pesticides/herbicides, explosives/propellants and/or electronic materials. No biological data given.    ADVANTAGE - The cocrystal forms of (I) lower the oral dose required to achieve therapeutic concentrations of lithium in the brain, thus reducing the peripheral toxicity and potentially broadening the therapeutic index in comparison to conventional lithium forms.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of preparing (I) comprising dissolving a stoichiometric ratio of a lithium salt and a complementary neutral organic molecule in a solvent, evaporating or cooling the solvent to form the lithium cocrystal composition or its solvate or hydrate, and combining the lithium cocrystal composition with a carrier or diluent; and    (2) a cocrystal having structure of formula (LiX.aM) or (LiX.aM.bS), or its solvate or hydrate.    X = halide or oxyanion, preferably fluoride, chloride, bromide, nitrate, sulfate, sulfonate, or carbonate;    M = a neutral organic molecule, preferably neutral zwitterionic compound, a xanthine, a polyphenol, nicotinic acid, amino acid such as alanine, arginine, asparagine, aspartic acid, cysteine, isoleucine, glutamic acid, glutamine, glycine, histidine, leucine, lysine, methionine, phenylalanine, proline, selenocysteine, serine, taurine, threonine, tryptophan, tyrosine, or valine, or a flavonoid;    a = 1 or 2;    b = 0-3; and    S = solvent or water.
NOVELTY - The apparatus (100) has a carbonization furnace (110) which is equipped with a burner (118). The organic raw source injected in the carbonization furnace is heated and carbonized. A water-cooling rotation exhaustion assembly (130) is provided for cooling the charcoal dropped from the carbonization furnace. The water-cooling rotation exhaustion assembly is prepared in lower portion of carbonization furnace. The water-cooling rotation exhaustion assembly is rotated in drop direction of charcoal.    USE - Continuous carbonizing apparatus for carbonizing organic raw source such as coconut husk and palm shell during manufacture of charcoal.    ADVANTAGE - The quality of the charcoal can be improved. The fuel consumption can be reduced. The organic raw source can be carbonized efficiently. The organic raw source can be recycled efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the continuous carbonizing apparatus.    Continuous carbonizing apparatus (100)    Carbonizing furnace (110)    Burner (118)    Water-cooling rotation exhaustion assembly (130)    Rotation exhausting portion (140)
NOVELTY - Production of organic-inorganic compound fertilizer using glycine wastewater and abamectin dregs comprises drying or airing abamectin waste dregs to make the water content be less than or equal to 30%; crushing; mixing abamectin dregs with phosphate fertilizer raw material (e.g. monoammonium phosphate), potash fertilizer raw material (e.g. potassium chloride), ammonium chloride, humic acid, animal excrement treated after fermentation, and/or diatomite; mixing the preprocessed abamectin dregs and other materials; mixing with glycine wastewater; granulating; and drying.    USE - Production of organic-inorganic compound fertilizer (claimed).    DETAILED DESCRIPTION - Production of organic-inorganic compound fertilizer using glycine wastewater and abamectin dregs comprises:    (A) drying or airing abamectin waste dregs to make the water content be less than or equal to 30%; and crushing;    (B) mixing abamectin dregs with phosphate fertilizer raw material (e.g. monoammonium phosphate, diammonium phosphate, or phosphate fertilizer), potash fertilizer raw material (e.g. potassium chloride and potassium sulfate), ammonium chloride, humic acid, animal excrement treated after fermentation, and/or diatomite; and    (C) mixing the preprocessed abamectin dregs and other materials; mixing with glycine wastewater; granulating; and drying to obtain the organic-inorganic compound fertilizer product.
NOVELTY - The furnace has a motor speed reducer driving a rotary kick-out device at a top part of a furnace body. A rotary kicking unit and a hydraulic drawing lifter are connected with a gasification reaction chamber. The gasification reaction chamber is provided with a pre-heating drying chamber. Two air inlet pipes are arranged at the furnace body. A heat preservation layer is arranged at a cavity outer wall of the furnace body. A gas pump is connected to a dust remover by a pipe. Bottom of the furnace body is fixed with a carbon discharging device.    USE - Agriculture and forestry raw material biomass gasification furnace.    ADVANTAGE - The furnace realizes continuous carbon discharging to the furnace body at regular time period by rotating the furnace body in a uniform manner and improves an atomic force microscopy (AFM) image contrast rate of the furnace body.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an agriculture and forestry raw material biomass gasification furnace.
NOVELTY - Ceramic coating of a metal substrate (110) is carried out by providing a metal substrate, forming an underlayer (120) on the side(s) of metal substrate by aerosol deposition, and forming a ceramic layer (130) on the underlayer.    USE - Ceramic coating of metal substrate used in catalyst-layer-coated substrates of catalyst structures used for purifying exhaust gas and reforming hydrocarbon into hydrogen (all claimed).    ADVANTAGE - The method forms an underlayer which improves adhesiveness and oxidation resistance of metal substrate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) ceramic-coated metal substrate (100);    (2) manufacture of catalyst-layer-coated substrate, which involves forming underlayer on metal substrate, and forming a catalyst layer consisting of a ceramic material by immersing the underlayer in a catalytic substance;    (3) catalyst-layer-coated substrate; and    (4) catalyst structure using the catalyst-layer-coated substrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the ceramic-coated metal substrate.    Ceramic-coated metal substrate (100)    Metal substrate (110)    Underlayer (120)    Ceramic layer (130)
NOVELTY - A synergistic device comprises solar battery, supporting column, conductive wire, controller, inverter, electric water pump, low temperature water pipe, low temperature water conveying pipe, low temperature water tank, vacuum heat collecting pipe, hot water output pipe, heat insulating layer, water discharge pipe, low temperature water, water-spraying head, methane storage room, methane tank, solar water heater.    USE - Synergistic device for solar water heater used for conveying hot water to pipe of methane tank wall.    ADVANTAGE - The solar light illuminates solar battery to generate current through the controller. The temperature and humidity environment is created in methane gas tank for decomposing organic methane bacteria to produce methane gas. The insulating layer at the top of the methane tank releases the cooling of methane tank.
NOVELTY - The recovery device has a microwave generating device set on a metal shell. An opening is formed on the metal shell to realize microwave radiation. A filter bed is set on the metal shell. A fan is arranged outside of the metal shell. A fan outlet pipe is connected to an outer surface of the metal shell by a small valve. A connecting position of the filter bed and an air inlet pipe is connected to a lower surface of a condenser shell. A condenser is located in a side of the metal shell and connected with a purified gas outlet pipe. An inlet pipe large valve is located at the metal shell.    USE - Microwave regenerative dry filter biomass gasification tar recovery device.
NOVELTY - Water/Oil type (W/O) emulsified fuel comprises vegetable oil and fat or ester obtained from fatty acid and 3C or less alcohol and vegetable oil and fat (A), water (B), condensed ricinoleic acid polyglycerol (C), and polyoxyethylene alkyl ether (D), where the alkyl is 12-18C alkyl, and average added mole number of ethylene oxide is 5-20. The mass ratio of ricinoleic acid polyglycerol and polyoxyethylene alkyl ether is 1-10.    USE - As W/O emulsified fuel useful for motor vehicles, boats, ships, agricultural machine, electric power generator, and heater.    ADVANTAGE - The W/O emulsified fuel is environmentally-friendly as emission of nitric oxide, sulfur oxide and particulate matter in exhaust gas is suppressed, and has excellent stability, rust prevention property, combustibility and fluidity.
NOVELTY - Selenium-enriched corn straw has selenium content of 10-200 mu g/kg, where organic selenium content is greater than or equal to 70%.    USE - Selenium-enriched corn straw used as selenium-enriched animal feed and edible fungi cultivation base material for livestock.    ADVANTAGE - The method solves the environmental pollution problem of directly supplementing inorganic sodium selenite in the prior art; achieves stability of selenium content; and provides products, which are safe for human consumption to improve people selenium level to prevent and treat diseases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of selenium-enriched corn straw comprising when corn seedling produces 5-6 pieces of visible leaves, applying selenium-enriched biological agent diluted with 500 times water at 100 ml/mu by spraying to corn leaves; before the corn tassel grows out and 3-4 pieces of leaves become visible, applying selenium-enriched biological agent diluted with 500 times water at 300 ml/mu by spraying the corn leaves; and harvesting to obtain selenium-enriched corn straw.
NOVELTY - A biomass pyrolysis gasification system comprises a biomass pyrolysis and gasification device, and a biomass drying device. A biomass pyrolysis gas outlet of gasification device is connected with dust removing device. A gas outlet of dust removing device is connected with focus follower. A gas outlet of the coke remover and a gas storage cabinet through the exhaust fan are connected.    USE - Biomass pyrolysis gasification system.    ADVANTAGE - When the system works, the biomass pyrolysis gasification generates biomass gas and biomass charcoal, after biomass gas dust removal and tar schizolysis finally forms the calorific value and cleans the biomass fuel gas. The pyrolysis side product biomass carbon produced by burning gas is used as gas tar schizolysis and biomass pyrolysis gasification and biomass raw material drying heat source in series, thus realizing the utilization of energy.
NOVELTY - The device has a toilet that is set with pedestal and excrement discharging pipe connected with marsh gas tank and organic garbage discharging pipe. The lower portion of marsh gas pool is provided with slag outlet. Methane tank is installed on top of marsh gas bacteria feeding pipe and biogas conveying pipe. The biogas storage tank is connected with marsh gas generator through marsh gas conveying pipe. The power distribution room is connected with the LED lamps through the conductive wire.    USE - Cogeneration device for disposing garbage and feces biogas in multi-story residential building.    ADVANTAGE - The biological sludge and organic garbage can be discharged effectively.
NOVELTY - Unpowered beam oxygen increasing device comprises upper flow biogas tank with water outlet pipe provided with a water seal U-shaped bent pipe which is 360 degrees elbow pipe placed vertically downward. The top of the 360 degrees elbow is provided with a discharge of upper clear liquid oxygen increasing the vertical short tube.    USE - Unpowered beam oxygen increasing device.    ADVANTAGE - The device has simple structure, and the dissolved oxygen concentration increases to more than 2%.
NOVELTY - The device has an active carbon purification tower provided with a gas inlet. A top part of the active carbon purification tower is provided with a spray atomizer. The active carbon purification tower is connected with a gas outlet of a spraying washing device. The spraying washing device is connected with a discharging device and an exhaust device. The spraying washing device is provided with another spray atomizer and an outlet.    USE - Biochemical active carbon waste gas purifying device.    ADVANTAGE - The device has better exhaust gas purifying effect and better applicability, and is inexpensive.
NOVELTY - The system has a gas collecting system provided with a spraying cooling tower. A bio-trickling tower is connected with a circulating water pump. A fan is fixed with a chimney that is provided with a circulating water tank. The gas collecting system is arranged on an organic waste gas outlet via an air pipe. The air pipe is connected with an end of the fan and the spraying cooling tower. The spraying cooling tower is connected with the bio-trickling tower via the chimney.    USE - Efficient organic waste gas deodorization system.    ADVANTAGE - The system removes organic waste gas so as to ensure better removal effect without requirement of adding nutrient solution, so that pollution is avoided. The system is convenient to operate, and ensures safety performance.
NOVELTY - Producing silage by compound microbial fermentation of straws comprises selecting good straws, corn stalks and/or leguminous stalk raw materials, and cutting; pouring a compound microbial leavening agent into wort of 1-2 degrees Brix, mixing uniformly, treating for 2-3 hours at 25-35 degrees C; controlling the moisture content to be 70-80%; inoculating and charging; placing in the air for 5-30 days; and sealing for 20-90 days. The compound microbial leavening agent comprises Aspergillus niger-spores, Lactobacillus rhamnosus (CGMCC4430) and Lactobacillus plantarum.    USE - A method for producing silage for domestic animals.    ADVANTAGE - The method generates free amino acid, and simultaneously generates a large amount of metabolin lactic acid. The pH value of the treated silage is reduced. No impure bacteria are grown. The produced silage is high in nutritive value and easy to digest.    DETAILED DESCRIPTION - Producing silage by compound microbial fermentation of straws comprises: (A) selecting good straws, corn stalks and/or leguminous stalk raw materials, cutting until the raw materials are 2-5 cm long; (B) pouring a compound microbial leavening agent into wort of 1-2 degrees Brix, mixing uniformly, treating for 2-3 hours at 25-35 degrees C; controlling the moisture content of the raw material to be 70-80%; (C) layering the raw materials for piling, when the thickness of the piled raw material reaches 20-30 cm, spraying bacterial liquid; (D) placing in the air for 5-30 days; (E) sealing for 20-90 days by a plastic film, where the compound microbial leavening agent comprises Aspergillus niger-spores, Lactobacillus rhamnosus (CGMCC4430) and Lactobacillus plantarum, and is used at 0.1-5% of the raw materials.
NOVELTY - Carbonizing rural household waste, comprises: (i) sorting the household waste, and removing inorganic waste and organic waste, which produces poisonous and harmful matters after combustion; (ii) drying naturally the sorted waste by air, and then roughly breaking to make the particle diameter to less than or equal to 5 cm; and (iii) carbonizing the roughly broken household waste under an anoxic condition, controlling the carbonization temperature at 350-500 degrees C, and controlling the carbonization time at 20 minutes-5 hours, and cooling naturally to obtain the carbonized product.    USE - The method is useful for carbonizing rural household waste. The carbonized product is useful as a fertilizer for improving the soil, and increasing the output of crops.    ADVANTAGE - The method integrates the rural household waste, recycles waste, and facilitates carbon fixation, is economical and environmental-friendly, and has simple operation procedures. The carbonized product prepared by the method does not cause secondary pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a carbonized product obtained by the above mentioned method for carbonizing rural household waste; and    (2) use method of the carbonized product comprising dispersing the product into the soil, and controlling the application depth in the soil to 0-20 cm, where the carbonized product is used independently or used together with fertilizers.
NOVELTY - Straw coal comprises 3-5 parts by weight (pbw) of coal, 95-97 pbw of straw and 0.1-0.5 pbw of combustion improver.    USE - The straw coal is useful in a biomass power plant and a home for cooking, warming and bathing purposes.    ADVANTAGE - The straw coal is convenient to preserve, and can be simply and economically prepared with high burning quality and less labor intensive in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the straw coal, comprising: (a) crushing straw, coal and combustion improver; (b) putting the crushed straw powder into a dryer to dry, insuring water content of the straw to be 20%; (c) taking the dried straw, adding coal and combustion improver powder, and uniformly stirring and obtaining mixed powder; (d) putting the powder into a compacting shape machine to conduct compacting shape, and preparing to fuel granular, where the fuel granular has a diameter of 6-15 mm and length of 20-50mm; and (e) cooling, sizing and packing treatment to the obtained fuel granular, conducting melt down treatment to the unqualified fuel granular, and repeating all steps.
NOVELTY - The system comprises a gasification chamber (6), a liquefying chamber and a liquid heat exchange tank. The gasification chamber and the liquefying chamber are sealed in a vacuum insulating layer (5) to perform circulated heat exchange. The gasification chamber is provided with a heat storage body (8), a heater and a temperature control probe (9). The liquefying chamber is equipped with a heat exchanger (7), a forced circulation inlet, a forced circulation outlet, and a liquid surface controller. A large urban sewage treatment is provided with a biogas tank.    USE - The system is useful for preparing pure water from sewage.    ADVANTAGE - The system is capable of effectively and economically preparing pure water from sewage.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a system for preparing pure water from sewage.    vacuum insulating layer (5)    gasification chamber (6)    heat exchanger (7)    heat storage body (8)    temperature control probe. (9)
NOVELTY - Use of Ficus tikoua, is claimed in purification of livestock and poultry biogas slurry, where the F.tikoua is planted in pollution environment of livestock and poultry biogas slurry.    USE - The F.tikoua is useful for purification of livestock and poultry biogas slurry.    ADVANTAGE - The F.tikoua enables purification of livestock and poultry biogas slurry at low cost, and simply and is environmentally-friendly. The F.tikoua has medicinal effect for chronic bronchitis, rheumatism, arthralgia and myalgia, diarrhea, dysentery, mastitis, edema, irregular menstruation, puerperal abdominalgia with blood stasis and snakebite.
NOVELTY - An organic fertilizer comprises aquatic plant, rice bran, bean pulp, straw, cotton seeds, bone meal, lactic acid bacteria and water. Weight ratio of lactic acid bacteria to rice bran to bean pulp to straw to cotton seeds to bone mean to water to aquatic plant is 1:30-150:15-20:40-60:45-65:4-6:60-150:600-1000.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has wide raw material sources, low cost and simple manufacturing technology, and does not cause environment pollution and does not destroy the soil structure of agricultural land.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the organic fertilizer, comprising respectively crushing bean pulp and straw to 40-60 meshes, mixing the rice bran, bean pulp, straw, cotton seeds, bone meal and lactic acid bacteria, fermenting for 3-5 days, adding the aquatic plant, and composting for 35-45 days to obtain the organic fertilizer.
NOVELTY - Preparation of organic-inorganic compound fertilizer involves mixing (pts. wt.) potassium ore (1-50), desulfurization ash (1-45), limestone (0-32) and sodium salt (1-5, preferably 1-4), grinding to 200-250 meshes, calcining at 1000-1050 degrees C for 2-3 hours, cooling, and ball milling to obtain potassium-calcium-silicon compound fertilizer; and mixing with bioorganic fertilizer (1-90 pts. wt.). The sodium salt is sodium sulfate, sodium fluoride, or sodium chloride.    USE - Method for preparing organic-inorganic compound fertilizer (claimed) used for rice, sugarcane, cassava, and sweet corn.    ADVANTAGE - The method recycles industrial solid waste and produces new potassium fertilizer, is environment friendly, and avoids solid and liquid waste discharge. The fertilizer increases crop yield, improves product quality, and regulates acidity and alkalinity of soil.
NOVELTY - Preparation of organic-inorganic compound fertilizer involves uniformly mixing (pts. wt.) potassium ore (1-45), caustic soda slurry (1-45), fluoride (0-5), sulfur compound (1-5) and calcium salt (1-5), grinding, calcining, cooling, and ball milling to obtain potassium-calcium-silicon compound fertilizer; and mixing with bioorganic fertilizer (1-90 pts. wt.).    USE - Method for preparing organic-inorganic compound fertilizer (claimed) used for rice, sugarcane, cassava, and sweet corn.    ADVANTAGE - The method recycles industrial solid waste and produces new potash fertilizer, is environment-friendly, and avoids solid or liquid waste discharge. The fertilizer increases crop yield, improves product quality, and regulates soil pH.    DETAILED DESCRIPTION - Preparation of organic-inorganic compound fertilizer involves uniformly mixing (pts. wt.) potassium ore (1-45), caustic soda slurry (1-45), fluoride (0-5), sulfur compound (1-5) and calcium salt (1-5), grinding to 200 meshes, calcining at 850-1050 degrees C for 1-3 hours, cooling, and ball milling to obtain potassium-calcium-silicon compound fertilizer; and mixing with bioorganic fertilizer (1-90 pts. wt.). The fluoride is sodium fluoride, calcium fluoride, potassium fluoride, magnesium fluoride, or ammonium fluoride. The calcium salt is calcium oxide and/or calcium carbonate. The sulfur compound is potassium sulfide, sodium sulfite, sodium sulfate, calcium sulfate, or calcium sulfite.
NOVELTY - Preparation of low acid value biodiesel comprises reacting oil and monohydric alcohol in first level reactor at 100-330 degrees C and 3-12 MPa; introducing material with aliphatic ester from first level reactor into second level reactor at 100-330 degrees C and 0.1-3 MPa; and gathering biodiesel with reduced acid value.    USE - Preparation of low acid value biodiesel.    ADVANTAGE - The method effectively reduces acid value of biodiesel, enables continuous reaction, reduces acid value of oil material to less than 3 mg KOH/g, and reduces energy consumption of device.
NOVELTY - Inhibition of heat exchanger scaling during biodiesel production comprises contacting inner wall of thermal medium tube pass of heat exchanger with methanol.    USE - Inhibition of heat exchanger scaling during biodiesel production (claimed).    ADVANTAGE - The method increases operational cycle of heat exchangers, is convenient, effective, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel by contacting oil and methanol to obtain coarse products of biodiesel under transesterification; distilling coarse products of biodiesel using distilled methanol to obtain distilled coarse products of biodiesel and methanol; loading distilled coarse products into flash column to distill; washing and taking off light components; discharging component steam from upside of flash column and introducing into gathering tank after cooling via heat exchanger in flash column; recovering heavy components of higher boiling point than biodiesel from bottom of flash column; and performing inhibition of heat exchanger scaling when heat exchange efficiency of heat exchanger reduces to 50-70%.
NOVELTY - An aromatic primary amine is synthesized by using aryl halide and ammonia as raw materials, water as solvent and alkali metal or alkaline-earth metal as alkali; reacting at 50-130 degrees C using copper source as catalyst, saccharide compound as ligand and polyethylene glycol as surfactant; and catalyzing aromatic halide and aqueous ammonia to form primary amine.    USE - Method for synthesis of aromatic primary amine (claimed) useful in high-throughput fabrication of natural products, drugs and pesticides.    ADVANTAGE - The method has simple operation, easy separation of product and green environmental protection. It uses green solvent reagents in accordance with the requirements of the development of green chemistry to solve pollution problem from the source.
NOVELTY - Preparing cassava processing residues biomass fuel, comprises dewatering a cassava processing residue using a dewatering device till water content is 50-70%, and drying the cassava processing residue using an aerobic fermentation process till the water content is less than 45% to prepare biomass fuel.    USE - The method is useful for preparing cassava processing residues biomass fuel, which is useful as a raw material for preparing biomass oil, biomass gas and coke, or biomass/non-biomass mixture fuel (claimed).    ADVANTAGE - The biomass fuel is environment-friendly, and has great economic and social benefits.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for preparing cassava processing residues biomass fuel.
NOVELTY - Bacteria Pandoraea sp. yellow-2CGMCC No.5284, is new.    USE - The bacteria Pandoraea sp. yellow-2CGMCC No.5284 is useful for eliminating ammonia nitrogen in the sewage at low temperature (8-12 degrees C) (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of Bacteria Pandoraea sp. yellow-2CGMCC No.5284.
NOVELTY - Method for preparing anesthesia composition, involves collecting snowbell berries, mixing snowbell berries (0.5-2 kg) with water (1 l), and heating the mixture at 112-116 degrees C and 60-80 kPa for 1-3 hours.    USE - The method is useful for preparing anesthesia composition for fish (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly.
NOVELTY - The eszopiclone sustained-release tablet comprises 1-5 mg of eszopiclone, 5-30% of release retardant, and an excipient, where the eszopiclone is dispersed in the release retardant. The release retardant is high molecular material sodium alginate for swelling in water.    USE - The sustained-release tablet is useful for treating chronic insomnia.    ADVANTAGE - The sustained-release tablet reduces fluctuation of the active component in blood concentration, improves patient compliance, reduces adverse drug reaction, and can be simply and economically prepared without toxicity.
NOVELTY - The method comprises taking concentrated sludge and dewatered sludge to mix, processing the sludge (88-98%) with alkaline anaerobic fermentation acid, pre-heating the processed sludge at 90-120 degrees C for 10-60 minutes to perform alkaline anaerobic fermentation for 3-8 days, recycling the product to react, where the reaction temperature is 20-55 degrees C, stirring the mixture at a speed of 30-250 revolutions per minute, adding alkaline reagent into the mixture and then adjusting pH value of 9-11, and collecting the product to obtained the final product. A reflux ratio of the return sludge is 5-20%.    USE - The method is useful for anaerobic fermentation of sludge, which is useful for producing volatile fatty acid.    ADVANTAGE - The method allows easy and economical fermentation of the sludge with high efficiency thus improving stability and quality of the volatile fatty acid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a method for anaerobic fermentation of sludge (Drawing includes non-English language text).
NOVELTY - Microwave cycle sludge anaerobic fermentation method for production of volatile fatty acids, involves mixing concentrated sludge and dewatered sludge to prepare mixed sludge, taking the mixed sludge as feed for alkaline anaerobic fermentation of acid, returning sludge by microwave pretreatment, circulating alkaline anaerobic fermentation again, and discharging collected product with high content.    USE - The microwave cycle sludge anaerobic fermentation method is useful for production of volatile fatty acids.    ADVANTAGE - The method improves utilization of organic substrate as it combines the alkaline adjusting, microwave strengthening wall, and circulating reflux technology for realizing the physical chemical strengthening treatment technology and microbial processing, and operation stability of the whole system.
NOVELTY - NOVELTY -The multi-enzyme body functional composite bacterial fertilizer comprises 40% of organic humic acid, 28% of rare-earth micronutrient fertilizer, 10% of grass carbon, 8-12% of jam, 5% of plant activating enzymes, 2% of Trichoderma, 10% of fruit, 2% of dried early tooth holding, 1-3% Bacillus subtilis, 2% of Bacillus licheniformis and 1% of amino acid.    USE - The bacterial fertilizer is useful for improving growth of wheat crops.    ADVANTAGE - The bacterial fertilizer is safe and non-toxic, and improves crop disease resistance and stress resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of manufacturing a multi-enzyme body functional composite bacterial fertilizer.
NOVELTY - Facultative anaerobic microbial composite microbial inoculum comprises Cellulomonas, Phanerochaete chrysosporium, white rot fungus and Bacillus subtilis. The Cellulomonas is obtained from bovine rumen fluid by screening separation.    USE - The facultative anaerobic microbial inoculum is useful for degrading straw (claimed).    ADVANTAGE - The microbial inoculum improves the production of marsh gas yield from crop straw fermentation by degrading the crop straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the facultative anaerobic microbial inoculum, comprising: culturing the Cellulomonas, Phanerochaete chrysosporium, white rot fungus and Bacillus subtilis respectively to enlarge; inoculating into a mixed fermentation culture medium according to the mentioned ratio; and culturing at pH of 7, an aeration rate of 0.5 vol./vol.x minute and a rotating speed of 200 rotations/minute at 37 degrees C for 24-48 hours to ensure that the viable bacteria count of the broth reaches to 25 hundred million/ml.
NOVELTY - Rhodococcus species RHA-MLDS gene (I), preserved at China microorganism bacterial strain preservation committee common microbe centre on November 30th, 2010, under preservation number of CGMCC No. 4379 and NCBI log number of 4218150, is new.    USE - (I) is useful for: preventing or treating lipid metabolism disorder and metabolic storage disorder, such as obesity, fatty liver or atherosclerosis; and producing oil, such as bio-diesel (all claimed).    ADVANTAGE - (I) is capable of producing oil with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an inhibitor of (I) and/or MLDS protein.
NOVELTY - Reducing lignocellulose fermentation inhibitor, involves (a) carrying out first section of steam explosion treatment to straw raw material, (b) combing steamed material to obtain thin wall tissue and fibrous tissues, (c) carrying out second section of steam explosion treatment to fibrous tissues, (d) carrying out enzymolysis and fermentation process, and combing product, and (e) measuring straw raw material, thin wall tissue and fiber tissue after combing, and water content of second section steamed explosion material, washing the product, and fermenting product.    USE - The method is useful for reducing lignocellulose fermentation inhibitor.    ADVANTAGE - The method is simple, ensures better pre-processing effect, avoids thin wall tissue degradation, controls occurrence of side reaction, causes no toxic reaction, reduces inhibitor content, steaming condition and sludge content, and improves utilization rate of raw material.    DETAILED DESCRIPTION - Method for reducing lignocellulose fermentation inhibitor, involves (a) carrying out first section of steam explosion treatment to straw raw material, (b) combing the steamed material to obtain thin wall tissue and fibrous tissues, (c) carrying out second section of steam explosion treatment to fibrous tissues, (d) respectively carrying out enzymolysis and fermentation process, and combing the obtained product, and (e) respectively measuring straw raw material used in the first section of steam explosion process, thin wall tissue and fiber tissue after combing, and water content of the second section steamed explosion material, washing the obtained product using water, and fermenting the obtained product.
NOVELTY - A synthetic ammonia circulating water replenishing device has ammonia circulating water system, a water outlet of circulating water system ammonia synthesis, pipelines and valves, a circulating water pumps (A,B), a water unit, a secondary water replenishing port, air outlet, adjusting valve, a primary water flow meter, a water tank (21), soft water adjusting valve, flow meter, soft water tank, a sand filter, water recycling system, online monitoring system, a primary water adjusting valve, a soft water adjusting valve and main control system.    USE - Synthetic ammonia circulating water replenishing device.    ADVANTAGE - The synthetic ammonia circulating water replenishing device is economical and environmentally-friendly, and has simple structure and high stability.
NOVELTY - Active composite suspended filler comprises foaming cement, an activated fly ash as a carrier base material and functional auxiliary materials, which is permeated by the carrier base material to form a porous carrier material with a shape of hollow body and a specific gravity less than 1. The material comprises foaming cement, activated fly ash, functional auxiliary material in a ratio of (15-50):(20-60):(5-30), where the porous carrier material with a porous outer surface adhesive layer and powdered magnetic material layer is made into the active composite suspension filler.    USE - The suspended filler is useful for organic wastewater biochemical treatment.    ADVANTAGE - The filler is honeycomb shaped, rough, and covered with large and small pores, provides high adsorption performance to harmful substances and dissolved oxygen, forms the different dissolving densities, and improves the processing efficiency in removing chemical oxygen demand and ammonia nitrogen.
NOVELTY - Use of Mirabilis jalapa for purifying biogas from livestock breeding, is claimed. The Mirabilis jalapa is planted in a place polluted by methane liquid produced during livestock breeding.    USE - The Mirabilis jalapa is useful in the field of sewage waste water treatment, removing wind, improving blood circulation; and treating turbid urine, vaginal discharge, hematemesis, acute arthritis, and hemoptysis.    ADVANTAGE - The Mirabilis jalapa completely absorbs ammonium-nitrogen, total nitrogen (TN), total phosphorus (TP), chromium chemical oxygen demand (CODcr); and is tenacious. The method cleans the plant old leaves on timely basis, and thus it is environmental-friendly; and is economical; and has simple, and easy operation procedures.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an automatic oxygen supply artificial wetland system comprising a wetland bed body containing a wetland filling substrate and a shale hollow brick, and a hole of the shale hollow brick is utilized for providing oxygen to the wetland system automatically.
NOVELTY - Method for preparing leavening agent, involves using (in %): calcium oxide (quicklime) (65), sodium chloride (edible salt) (19), sodium bicarbonate (edible soda) (9), auxin (5), and microelements (2).    USE - The method is useful for preparing leavening agent.    ADVANTAGE - The method effectively prepares highly nutritional leavening agent in a simple and cost-effective manner as the raw materials are profusely and inexpensively available, can be widely applied in fields of farming, livestock breeding and aquaculture, and is environmentally-friendly.
NOVELTY - Method for synthesizing creatinol phosphate, involves (a) reacting N-methyl-2-aminoethanol with phosphoric acid to obtain 2-(methylamino)ethoxy phosphonic acid and water, and (b) reacting the 2-(methylamino)ethoxy phosphonic acid with O-methylisourea sulfate under alkaline condition to obtain the creatinol phosphate.    USE - The method is useful for synthesizing creatinol phosphate.    ADVANTAGE - The method simply synthesizes highly pure creatinol phosphate under mild conditions at high yield and does not emit any harmful gas or waste acid and hence is environmentally-friendly and safe.
NOVELTY - The formulation comprises 5-15 mg of Trichoderma harzianum spore powder, 0.5-1.0 ml of 98% of Tween-80 (RTM: Polysorbate 80), 1-5 g of maltose, 0.03-0.07 g of ferrous sulfate, 0.4-0.8 g of magnesium sulfate, 0.4-0.7 g of compound amino acid, 0.02-0.06 g of boric acid and 5 ml of ethoxylated trisiloxane.    USE - The formulation is useful for degrading pesticide residue in plant.    ADVANTAGE - The formulation is capable of simply and conveniently degrading the pesticide residue in plant in a safe manner, and can be economically prepared with high efficiency and reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing formulation.
NOVELTY - The insecticide and fertilizer granular formulation comprises 0.5-15 wt.% of carbosulfan, 30-70 wt.% of carrier fertilizer, 0.1-2 wt.% of slow release agent, 0.1-10 wt.% of adhesive, 0.1-0.5 wt.% of coating agent, and kaolin filler.    USE - The insecticide and fertilizer granular formulation is useful for preventing peanut soil insect.    ADVANTAGE - The insecticide and fertilizer granular formulation can be simply and economically prepared with high productivity and less labor intensive and without toxicity in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing insecticide and fertilizer granular formulation.
NOVELTY - A biodiesel is purified by using a polymeric adsorbent.    USE - Method for purifying biodiesel (claimed).    ADVANTAGE - The method improves purity of the biodiesel, and improves recovery ratio and purity of methanol and glycerol.
NOVELTY - Preparing ceramic matrix having bioactivity of biological components, by (a) soaking porous silicon carbide/tourmaline substrate in mixture of sodium alginate and polyvinyl alcohol (PVA), (b) further soaking the substrate in mixture of boric acid and calcium chloride, or (c) soaking the porous silicon carbide/tourmaline substrate in mixed solution of silica solution and PVA to obtain porous silicon carbide substrate/tourmaline substrate loaded with organic induced membrane, fixing selected cells on substrate by surface adsorption method to obtain ceramic matrix.    USE - The method is useful for preparing ceramic matrix having bioactivity of biological components preferably cells used for sewage treatment.    ADVANTAGE - The ceramic matrix has high strength, large specific surface area, good permeability and renewable utilization. The ceramic matrix has good compatibility between the organic materials and cells, hence fixing of the suspending cells is improved. The ceramic matrix is easy to recycle, does not cause any secondary pollution when compared to existing carriers, and has broad application prospects in sewage treatment.    DETAILED DESCRIPTION - Method for preparing ceramic matrix having bioactivity of biological components, involves (a) soaking porous silicon carbide substrate or porous tourmaline substrate in mixture comprising sodium alginate and polyvinyl alcohol (PVA), (b) further soaking the substrate in mixture comprising boric acid and calcium chloride, or (c) soaking the porous silicon carbide substrate or porous tourmaline substrate in mixed solution of silica solution and PVA to obtain porous silicon carbide substrate or porous tourmaline substrate which is loaded with organic induced membrane, fixing selected cells on the substrate by surface adsorption method to obtain ceramic matrix with bioactivity of the biological components.
NOVELTY - The furnace has a gas generator formed by an inner wall, an outer wall and a bottom welding part. A straw is utilized as a raw material to generate combustible gas that supplies a heat source for heating and cooking. A water outlet is connected with the outer wall. An air inlet of the gas generator is welded with the outer wall of the gas generator. A fan is provided in a gas outlet. The air inlet is provided between two tubes. The gas generator is round or square shaped. A gas boiler is provided with a burning water pipe.    USE - Domestic water heating straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a domestic water heating straw gasification furnace.'(Drawing includes non-English language text)'
NOVELTY - Preparation of iloperidone (I) comprises reacting 6-fluoro-3-(4-piperidinyl)-1,2-benzisoxazolehydrochloride and 1-(4-(3-chloropropyl-oxy)-3-methoxyphenyl)ethanone in a reaction medium comprising an aqueous solution of non-ionic surfactant and in the presence of an inorganic acid binding agent and potassium iodide, as catalyst.    USE - (I) is useful to treat schizophrenia. No biological data given.    ADVANTAGE - The process rapidly provides (I) in high yield and high purity, without any adverse impact on the environment.
NOVELTY - A o-hydroxybenzene nitrile dimethyl formamide solution is obtained by mixing triphosgene and salicylamide in dimethyl formamide, and reacting the mixture.    USE - Ortho-hydroxybenzene nitrile dimethyl formamide solution is used for manufacturing azoxystrobin and bunitrolol (claimed).    ADVANTAGE - The ortho-hydroxybenzene nitrile dimethyl formamide solution is environmentally friendly, and is manufactured efficiently and economically by simple method.
NOVELTY - Livestock excretion composting installation, comprises warehousing unit of which exterior is composed by a warehousing and which prepares an excretion storage container inside the warehousing, multiple production units in which agitation unit receiving livestock excretion transmitted from the excretion storage container and mixing livestock excretion, and which composes the exterior by production housing, and delivery part which composes the exterior by the production housing at a place to which compost is produced.    USE - As livestock excretion composting installation.    ADVANTAGE - The livestock excretion composting installation does not produces bad odor, and thus protects environment.    DETAILED DESCRIPTION - Livestock excretion composting installation, comprises warehousing unit of which exterior is composed by a warehousing and which prepares an excretion storage container inside the warehousing, multiple production units in which an agitation unit receiving livestock excretion transmitted from the excretion storage container of the warehousing unit and mixing livestock excretion, and which composes the exterior by a production housing and performs fermentation by repeating movement of the livestock excrement to upper and lower of the center from outer ring inside the production housing, and delivery part which composes the exterior by the production housing at a place to which compost produced in the production units is transmitted and is equipped with a phase difference transporting part to which the compost is transmitted from the producing units.
NOVELTY - Phosphorus and fluorine are recycled from defluorination residue by mixing residue and sulfuric acid, extracting phosphorus and fluorine from the residue to obtain calcium sulfate dihydrate or calcium sulfate hemihydrate, dilute phosphoric acid and ardealite by-product; concentrating the dilute phosphoric acid, recycling fluorine containing gas and converting the gas into fluorosilicic acid, or adding dissolvent to the phosphoric acid and recycling phosphorus resource in the form of fluoride derivative; and converting obtained orthophosphate products into ammonium phosphate.    USE - Method of recycling phosphorus and fluorine from defluorination residue.    ADVANTAGE - The method utilizes waste thus reducing pollution and saving resources.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of recycling phosphorus and fluorine from defluorination residue (Drawing includes non-English language).
NOVELTY - Phosphorus and fluorine from sewage of phosphate fertilizer plant are recycled by resolving sewage using sulfuric acid, extracting phosphorus and fluorine from sewage, taking dehydrated calcium sulfate or calcium sulfate hemihydrates and phosphoric acid, and taking phosphoric acid and byproduct ardealite after solid-liquid separation; and concentrating dilute phosphoric acid, recycling gas containing fluorine, changing these gas into fluoride, and recycling phosphorus resource in form of sodium fluorosilicate.    USE - Method for recycling phosphorus and fluorine from sewage of phosphate fertilizer plant (claimed).    ADVANTAGE - The method makes waste profitable, improves the value of recycling phosphorus and fluorine resources from sewage of phosphate fertilizer plant, and has good performance on environmental benefit and economic benefit.    DETAILED DESCRIPTION - Recycling phosphorus and fluorine from sewage of phosphate fertilizer plant, comprises:    (A) resolving sewage using sulfuric acid, extracting phosphorus and fluorine from sewage, taking dehydrated calcium sulfate or calcium sulfate hemihydrates and phosphoric acid with 15-28% of phosphorus pentoxide, and taking phosphoric acid and byproduct ardealite after solid-liquid separation; and    (B) concentrating dilute phosphoric acid to strong phosphoric acid, recycling gas containing fluorine obtained from processes of concentration and acid making, changing these gas containing fluorine into fluoride such as fluorosilicic acid or adding dissolvent for defluorination, recycling phosphorus resource in form of sodium fluorosilicate, and making orthophosphate products such as ammonium phosphate with strong phosphoric acid.
NOVELTY - Device comprises fermenter, thermophilic microorganisms, animal waste, heating wire apparatus and stirrer. The thermophilic microorganisms ferment animal waste. The heating wire apparatus is accommodated inside the fermenter and increases inner temperature. The stirrer uniformly blends the thermophilic microorganisms and animal waste, and is rotatably arranged inside the fermenter.    USE - The device is useful for preparing fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing fertilizer using animal waste and thermophilic microorganisms, which involves pulverizing animal waste and thermophilic microorganisms and dissolving the powder in water, adding the powder to fermenter, supplying oxygen inside the fermenter, and heating the fermenter.
NOVELTY - Producing a compost, comprises: mixing manure or bird dung with a carrier of organic carbon on concreted area by using self-propelled mixer with simultaneous piling of mixture in heaps and subsequent forced aeration; and packing the finished compost in perforated packets, where the forced aeration of organic mixture is conducted in heap via mobile aerator.    USE - The method is useful for producing compost.
NOVELTY - Compost is prepared by packing initial biomass including manure and litter into a fermenter and supplying oxygen, then compacting biomass without preliminary preparation and mixing with a layer of digested organic carbonaceous component at humidity of 76-78% or mixing with fodder residue and agricultural bedding, and ensuring carbon to nitrogen ratio (C:N) of 25:1.    USE - Method of preparing compost (claimed).
NOVELTY - Production of liquefied fertilizer using butchery blood, involves crushing the butchery blood, fermenting the butchery blood at 50-65 degrees C, adding enzyme to the fermented product, and sterilizing the product.    USE - The method is useful for production of liquefied fertilizer.
NOVELTY - An organic fertilizer comprises (in wt.%) natural guano (15-50), natural potassium (5-10), and fermented dehydrated poultry waste (40-80).    USE - Organic fertilizer for preventing soil acidification.    ADVANTAGE - The organic fertilizer improves sugar content and seed color in fruits and fruit vegetables.
NOVELTY - The device has a gas exhaust port arranged at a top part of a cylinder. An opening and closing door is arranged such that liquefied fertilizer composed of livestock excretion and waste food, is provided through the door. An air supplying part is provided with air supply holes that are utilized for supplying air from an air generation unit. An inner side of a fermenter part is rotatably arranged in an inner side of the liquefied fertilizer. A rotation driving unit i.e. drive motor, is arranged for rotating the air supplying part. The exhaust port is connected with a gas collecting device.    USE - Encapsulated-type liquefied fertilizer manufacturing device.    ADVANTAGE - The device improves liquid state fertilizer efficiency of an organic compound and avoids generation of bad small due to the fermentation gas. The device increases capacity of the liquid state fertilizer fermenter due to the precipitate deposition in an effective manner and reduces liquid state fertilizer manufacturing time.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an encapsulated-type liquefied fertilizer manufacturing device.
NOVELTY - Preparing landscape soil, involves mixing components (in wt.%) e.g. red clay (27-32), and wastewater sludge produced from cosmetic industries (7-12), and wastewater sludge produced from potato processing food industry and corn starch processing food industry (12-17, each) to obtain mixture, adding at least one microbial agent (3-7) containing microorganism e.g. Bacillus subtilis and Rhizopus oligosporus to mixture, subjecting the mixture to aging process, adjusting oxygen level of the mixture, and subjecting aged mixture to fermentation.    USE - The method is useful for preparing landscape soil.    ADVANTAGE - The method enables preparation of landscape soil using environmentally-friendly components and is not associated with generation of gas during secondary fermentation. The landscape soil is environmentally-friendly, as the soil has less content of heavy metals, hence soil contamination is prevented during degradation of garden trees.    DETAILED DESCRIPTION - Method for preparing landscape soil, involves mixing components (in wt.%): sawdust (3-7), red clay (27-32), and wastewater sludge produced from cosmetic industries, dairy industry and cereal processed foodstuff industry (7-12, each), and wastewater sludge produced from potato processing food industry and corn starch processing food industry (12-17, each) to obtain mixture, adding at least one microbial agent (3-7) comprising microorganism chosen from Bacillus subtilis, B.thuringiensis, Streptococcus faecium, Rhodobacter gelantinoca, and Rhizopus oligosporus to mixture, subjecting the mixture to aging process for 15-25 days, adjusting oxygen level of the mixture while aging process, and subjecting aged mixture to fermentation, where the mixture contains 50-70 wt.% of moisture.
NOVELTY - The bioreactor (1) includes a parallel shaped chamber (2) closed by cover (3), where the cover has auto compensating function promoted by lateral communication unit (4). Multiple sub-chambers (S1,S2,S3,S4) are bounded by cross walls (T1,T2,T3) of different heights, which separate material of higher density entering material in bioreactor.    USE - Bioreactor for producing biogas and organic fertilizer using manure as a raw material from pigs, cattle, goats and birds.    ADVANTAGE - The bioreactor includes a parallel shaped chamber closed by cover, where the cover has auto compensating function promoted by lateral communication unit, and thus ensures high possibility of excessive concentration of internal pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the bioreactor.    Bioreactor (1)    Chamber (2)    Cover (3)    Communication unit (4)    Chambers (S1,S2,S3,S4)    Septa (T1,T2,T3)
NOVELTY - N-Substituted phenyl oxime-ether compounds (I) are new.    USE - (I) are useful for preventing pests on crops (claimed), preferably insect and plant diseases, preferably bacterial diseases. Tests details are described but no results given.    ADVANTAGE - (I) have good sterilization, low toxicity and are eco-friendly.    DETAILED DESCRIPTION - N-Substituted phenyl oxime-ether compounds of formula (I) are new.    R = halo (preferably F, Cl, Br or I), CN, nitryl, 1-6C alkyl, 2-6C alkenyl, 2-6C alkynyl, 1-6C alkoxy, 1-6C halo alkoxy, 1-6C alkyl sulfanyl, 1-6C alkyl carbonyl, 1-6C alkoxyl carbonyl or 1-6C alkyl amino;    Z = CH3 or H;    Q = (2-oxooxazolidin-3-yl) or (5-methyl-2-oxo-1,3,4-oxadiazol-3-yl); and    n = 1-5.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - The method involves transferring soil to soil transfer conveyor in soil reservoir. The saw dust stored in sawdust storage tank is mixed with the soil to obtain a mixture. The mixture is crushed and stored in crushed material reservoir. The iron in the mixture is separated. The fermentation liquid fertilizer is sprinkled on the mixture to irradiate harmful bacteria in the soil. The fermented soil is covered using vinyl cover for 10-12 days.    USE - Recycling method for recovering soil from landfill waste.    ADVANTAGE - The recycling efficiency of the landfill waste is improved and recycling cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating recycling process for recovering soil from landfill waste. (Drawing includes non-English language text)
NOVELTY - The method involves passing wood, straw, shell, rice hull or forestry processing residue into gasification furnace with automatic feeding mechanism. A product tar, black waste liquid and combustible gas are passed to activation furnace which uses using black waste liquor steam as activator. The biomass carbon is adopted as pseudosubstrate for catalytic cracking agent in activation furnace. The generated product high temperature gas and waste heat boiler are heat exchanged to generate vapor for obtaining porous carbon material, and pure gas used for driving internal combustion machine.    USE - Biomass gasification-activation combination method for preparing active porous carbon material used in petrochemical industry, medicine industry, food industry and national defense industry (all claimed).    ADVANTAGE - The active porous carbon material is prevented from generating combustible gas tar and black waste liquid, thus the environment is protected. The combustible gas heat value is increased by the carbon material. The purity of the active porous carbon material is improved. The pipeline of the machine is prevented from blockage, thus the machine can be operated continuously. The additional value of the carbon material is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification-activation furnace.
NOVELTY - The method involves enriching low concentration gas through vacuum absorbing and vacuum discharging processes. The vacuumizing gas discharged from vacuum discharging process is passed to absorbing towers (5A,5B) provided with methane as absorbent. The vacuum absorption is performed on gas through boosting, absorbing, uniform pressure dropping, vacuum discharging, vacuumizing, and uniform pressure raising processes. The product gas with methane is extracted from exhausting end of absorbing tower through vacuum pump (12), after finishing uniform pressure dropping of absorbing tower.    USE - Method of enriching coal mine ventilating gas through absorbing tower.    ADVANTAGE - The coal mine ventilating gas is enriched with methane gas, thus the greenhouse gas discharge is reduced.    DETAILED DESCRIPTION - The active carbon, zeolite molecular screen and metal organic skeleton material are used as absorbent in vacuum absorbing process. The absorbing pressure of the absorbing tower is maintained at 0.1-0.16 MPa. The decompressing and desorbing pressure of the absorbing tower is maintained at 0.01-0.08 MPa.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating process of enriching coal mine ventilating gas. (Drawing includes non-English language text)    Gas inlet buffer tank (2)    Absorbing towers (5A,5B)    Uniform pressure control valve (7A)    Vacuum pump (12)    Extracting control valve (14)
NOVELTY - The aqueous phase containing oxygenated organic compound generated in Fischer-Tropsch synthesis of oil is subjected to catalytic hydrogenation, such that oxygenated organic compound is converted to 1-4C alkanes. Thus, organic oxygenated compound is removed from aqueous phase.    USE - Removal method of oxygenated organic compound from aqueous phase generated in Fischer-Tropsch synthesis of oil and wastewater generated from chemical companies and food industries (all claimed).    ADVANTAGE - The method removes oxygenated organic compound at a rate of more than 98%, by converting it to lower alkane which can be reused in the Fischer-Tropsch process. The treated water can be recycled.
NOVELTY - Dehydration of higher alcohols involves testing water content of water-containing higher alcohols, calculating addition amount of aluminum isopropoxide, adding higher alcohols to aluminum isopropoxide, stirring, analyzing the water content, and testing the acidity and alkalinity of sample. When water content is 0.3% or less and not alkaline, the dehydration reaction is stopped. When water content is 0.3% or more, aluminum isopropoxide is added. When sample is alkaline, 1% of higher alcohol is added, stirred and undissolved substances are removed.    USE - Dehydration of higher alcohols used for forming methanol gas additive.    DETAILED DESCRIPTION - Dehydration of higher alcohols involves testing water content (n%) of water-containing higher alcohols, calculating addition amount of aluminum isopropoxide according to a formula: 3.7x wx n% (where, w is the amount of water-containing higher alcohols), adding water-containing higher alcohols to aluminum isopropoxide, stirring for 0.5-1 hour, sampling, analyzing the water content of sample, and testing the acidity and alkalinity of sample. When the water content is 0.3% or less and not alkaline, the dehydration reaction is stopped. When the water content is 0.3% or more, aluminum isopropoxide is calculated based on the formula, and added. When sample is alkaline, 1% of higher alcohol is added, stirred for 0.5 hour and undissolved substances are removed, to obtain liquid (methanol gasoline additive).
NOVELTY - Method for producing organic fertilizer, involves preparing solid fuel with pulverized excretion sludge, and mixing ash which is obtained by burning (in wt.%): rice chaff burnt ash (5-15), diatomite (3-7), bentonite and kaoline (1-5, each), and clay (1-5 with respect to 100 of the excretion sludge mixture).    USE - The method is useful for producing organic fertilizer.    ADVANTAGE - The method is environmentally-friendly and cost-effective and easy to handle.
NOVELTY - The method involves changing biomass into particle size from 0.1 to 0.3 mm. The biomass is mixed with high-boiling hydrocarbon mixtures, where ratio of the biomass and the high-boiling hydrocarbon mixture is 4:100-12:100, and the mixture reacts in a reactor at a temperature of 1200-1400 degree Celsius and pressure of 3-4 MPa to produce hydrogen and synthesis gas.    USE - Method for producing hydrogen.
NOVELTY - Preparation of fertilizer, involves (a) removing impurities from food waste and pulverizing the food waste, (b) adding deodorization material to the pulverized food waste, (c) adding microorganism and decomposing the food waste under anaerobic condition in a fermenter, (d) adding aerobic and anaerobic bacteria and performing fermentation, (e) separating wastewater generated in the fermenter, re-circulating the separated wastewater to the fermenter and accelerating fermentation process and (f) heat-drying fermented product.    USE - The method is useful for preparing fertilizer.    ADVANTAGE - The method enables preparation of high quality fertilizer without having bad odor.
NOVELTY - Method for preparing fertilizer using food waste, involves removing impurity from the food waste, passing the obtained food waste through a fermentor containing microorganism under anaerobic environment for disassembling the food waste, decomposing the obtained food waste in a fermentor under a condition in which anaerobic bacteria and aerobic bacteria are capable of propagating, separating the wastewater generated during the fermentation step, and transferring the wastewater to fermentor, where the food waste without the wastewater is dried using hot air.    USE - The method is useful for preparing fertilizer using food waste.    ADVANTAGE - The method produces fertilizer with improved quality, and minimizes generation of bad odor during fermentation process by optimizing fermenting conditions.
NOVELTY - Invention relates to chemistry and can be used to produce a methane-hydrogen mixture containing H2 and CH4, for producing hydrogen, alcohols, ammonia, dimethyl ether, ethylene, for Fischer-Tropsch processes, for processing hydrocarbon gases, as well as in chemothermal systems for accumulating and transporting energy and methane-methanol thermochemical water decomposition cycles. A stream containing lower alkanes is mixed with steam or steam and carbon dioxide, heated via convectional cooling of a nuclear reactor coolant through air-tight heat-exchange surfaces and then passed through an adiabatic reactor filled with catalyst filling. Steam is removed from the stream after cooling. Coolant, cooled by the heated stream, is used to obtain high pressure steam directed into a steam turbine, from which, after expansion, steam is collected for mixing with the stream.    USE - Chemistry.    ADVANTAGE - Invention enables to lower expenses on producing a methane-hydrogen mixture. 9 cl, 12 tbl
NOVELTY - An air purifying agent comprises (in weight parts) acetic acid (1-2), ethanol (13-22), butane (0.1-0.4), lavender essential oil (0.2-0.5) and water (10-15) as raw materials.    USE - Air purifying agent for preventing influenza and respiratory diseases.    ADVANTAGE - The agent can remove harmful peculiar smell. The agent has smell of lavender to calm the nerves.
NOVELTY - Invention refers to chemical extinguishing measures including gas-forming chemically active substances and, more precisely, to substances retarding chemical reactions containing organic compounds. It can be used to protect industrial premises where hydrogen is produced as a target or by-product, also for storage and transportation of hydrogen. Gas compound preventing inflammation and explosion of hydrogen-air mixture includes hydrocarbon deterrent containing 2-8 atoms of carbon diluted by phlegmatizing carbon dioxide. Gas compound is two-component. As a deterrent, it contains i-C4H8 isobutene - at least 5.0% of protected volume given optimal ratio of components, vol. %: isobutene/carbon dioxide - 1:2.4. The invention ensures guarantee prevention of inflammation of hydrogen-air in the protected volume in all ratios of all its components.    USE - Fire fighting chemicals.    ADVANTAGE - Retardation of chemical reactions containing organic compounds thus allowing extinguishing fire. 1 dwg, 1 dwg
NOVELTY - The apparatus has electrodes that are provided in a vessel. The electrolytic decomposition of water is performed to produce hydrogen in the vessel. A separator is provided to separate the electrodes. The hydrogen is stored in the chemical bond.    USE - Apparatus for producing and storing hydrogen.    ADVANTAGE - Since the hydrogen is stored in chemical bond, the apparatus is safe to use, and the recovery of hydrogen can be reliably controlled.
NOVELTY - Carbon nanohelices production involves adding metal salt into aqueous solution comprising a carbon precursor, where obtained compound is thermally cured at 120 degrees C. The obtained compound is carbonized at 900 degrees C and then washed, where metal salts of the obtained material is eliminated with an oxidizing agent.    USE - Method for producing carbon nanohelices used for making electro-catalyst for making membrane electrode assembly for manufacturing hydrogen or alcohol fuel cells for producing energy (all claimed).    ADVANTAGE - The method reduces environmental impacts of energy activities including global warming and emissions of carbon monoxide, nitrogen oxides, sulfur oxides and other pollutants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for obtaining electro-catalyst, which involves depositing metal on carbon nanohelices through impregnation, colloidal or microemulsion.
NOVELTY - An aircraft fuel cell system comprises a fuel tank for a fuel present in a liquid phase; a reactor for reforming fuel from the fuel tank to a gas that contains hydrogen; heating apparatus for heating the fuel fed to the reactor; a fuel cell; a fuel feed line for feeding fuel from the fuel tank to the reactor; and an outlet line for feeding the gas that contains hydrogen from the reactor to the fuel cell, where the reactor is designed for processing, as a fuel, a synthetic fuel made from biomass.    USE - The aircraft fuel cell system is useful for manufacturing aircraft. The synthetic fuel, which was produced from biomass, is useful as fuel in aircraft fuel cell system; and for generating gas that contains hydrogen (all claimed).    ADVANTAGE - The invention provides aircraft fuel cell system in which the service life of the reformer is extended.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an aircraft comprising the aircraft fuel cell system.
NOVELTY - The cell has a collector (147) whose one main surface is contacted with surface of one of the air electrode layer (141), solid electrolyte layer (143), and fuel electrode layer (144) of cell main portion (140). An lectroconductive element (182) is faced by main portion and connector connected with other main surface of collector. One end of element is connected to air and fuel electrode layers. The other end of element is connected to connector. The element is transformed easily from collector (181) with respect to the fluctuation of distance between main portion and connector.    USE - Solid oxide fuel cell for receiving and generating supply of fuel gas and oxidizing agent gas.    ADVANTAGE - The electroconductive element is transformed easily from collector with respect to the fluctuation of distance between main portion and connector, thus the certainty of the electric continuity between fuel cell main portion and connector of the solid oxide fuel cell can be improved. Since the electroconductive element of the solid oxide fuel cell is formed using metal material, the durability of the solid oxide fuel cell can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Fuel cell main portion (140)    Air electrode functional layer (141)    Solid electrolyte layer (143)    Fuel electrode functional layer (144)    Collectors (147,181)    Electroconductive element (182)
NOVELTY - The method involves preparing a raw material catalyst that makes a carrier to carry a catalyst metallic particle. Water is mixed with the raw material catalyst, and raw material catalyst slurry is created. The catalyst metallic particle of the raw material catalyst is modified by a hydrophilic group. The modified catalyst metallic particle is conveyed through the raw material catalyst slurry in a pipeline (31). The catalyst metallic particle is mixed with an aqueous solution that contains the hydrophilic group.    USE - Method for manufacturing a catalyst of a fuel cell.    ADVANTAGE - The catalyst metallic particle is mixed with the aqueous solution that contains the hydrophilic group, so that the hydrophilic functional group of a side chain of a polymer electrolyte improves the catalyst applied to a reaction layer, and usage-amount of the catalyst metallic particle can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a manufacturing apparatus    (2) a method for manufacturing a paste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a mixing apparatus.'(Drawing includes non-English language text)'    Pipeline (31)    Pump (33,37)    Injection tube (35)    Water tank (38)    Syringe pump (39)
NOVELTY - The method involves producing product gas in a biomass gasification device (1) from woody biomass. The product gas in a methanation reactor (3) is converted into methane-containing fuel gas in an exothermic methanation process. Bio-synthetic natural gas is produced by removing carbon dioxide from the methane-containing fuel gas. Waste heat produced during the exothermic process in the methanation reactor is utilized in a gas- and steam turbine power plant (2) for reheating water vapor that drives a steam turbine (9) of the power plant.    USE - Method for producing fuel gas and electrical energy (all claimed).    ADVANTAGE - The method enables utilizing waste heat produced during exothermic process in the methanation reactor in the gas- and steam turbine power plant for reheating water vapor to drive the steam turbine, thus ensuring energy-efficient and economic use of large amounts of woody biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for producing fuel gas and electrical energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for producing fuel gas and electrical energy.    Biomass gasification device (1)    Gas- and steam turbine power plant (2)    Methanation reactor (3)    Gas turbine (5)    Steam turbine (9)
NOVELTY - A multifunctional pyrolyzing furnace comprises liner, outer cylinder, fire grate, discharge hole and exit pipe arranged outside liner, furnace cover arranged on upper opening of liner, feed inlet, and air inlet arranged on furnace cover. Bottom of liner is connected with discharge hole. Fire grate is arranged between inner cylinder and discharge hole. Gas extraction gallery is formed by air duct, small air outlet hole and ventilating flame retardant coating. Furnace cover is a bell jar and is equipped with distribution assembly.    USE - Multifunctional pyrolyzing furnace for agricultural wastes.    ADVANTAGE - Agricultural wastes are efficiently transformed to biological mixed gas or biomass coal.    DETAILED DESCRIPTION - Multifunctional pyrolyzing furnace comprises liner, outer cylinder, fire grate, discharge hole and exit pipe arranged outside liner, furnace cover arranged on upper opening of liner, feed inlet, and air inlet arranged on furnace cover. Bottom of liner is connected with discharge hole. Fire grate is arranged between inner cylinder and discharge hole. Lower of liner is uniformly distributed with small air outlet hole. An annular air duct is formed between outer cylinder and liner. The exit pipe is arranged on outer cylinder. Gas extraction gallery is formed by air duct, small air outlet hole and ventilating flame retardant coating. Furnace cover is a bell jar and is equipped with distribution assembly.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view illustrating a multifunctional pyrolyzing furnace.
NOVELTY - Plant for torrefaction of biomass, preferably wood chips, wood- and plant remains comprises functional units i.e. a feeding device for biomass, a vacuumable torrefaction device for the torrefaction of biomass by the action of heat, an extraction device for the torrefied biomass from torrefaction device and a supply device for operating the functional units. The plant is transportable, and at least a part of the functional unit of the plant is arranged together on at least one transport rack and is connected together. The supply device is operated independently by an external power supply.    USE - The plant is useful for torrefaction of biomass, preferably wood chips, wood- and plant remains.    ADVANTAGE - The plant: is compact and easy to transport; increases the energy density of biomass; removes the moisture from the biomass; and produces storable final product that is optimally processed in power- and pyrolysis plants.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the plant for torrefaction of biomass. (Drawing includes non-English language text).
NOVELTY - The system has a steam turbine steam generating device arranged with a steam generator, a steam discharge pipe, a steam bag, a steam turbine and an electric generator. The steam bag, the steam turbine and the electric generator are connected. A vapor generator is installed on a rubbish gasification furnace. The steam generator is arranged with an upper annular pipe, straight tubes and a lower annular pipe. An end of the steam discharge pipe is connected to a steam pocket. The lower annular pipe is connected to a water inlet pipe.    USE - Built-in steam tube type rubbish treatment waste heat power generation system.    ADVANTAGE - The steam generator is arranged in a gasification furnace for performing better heat exchange function. The system utilizes heat generated by the rubbish treatment and maximizes waste heat recycling rate. The system is arranged with a four stage hydraulic pushing device for loosening rubbish in a furnace without blockage.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a built-in steam tube type rubbish treatment waste heat power generation system.
NOVELTY - The device (1) has a tubular jacket (2) comprising an inlet (20) and an outlet (21). Inlet and outlet pistons (3, 4) are slidable between an extreme opening and fully closed positions. The outlet piston is retained in the closed position until the inlet piston reaches an intermediate closed position. The inlet piston delimits a volume of a compression chamber in the closure position such that pressure in the volume is equal to that of an outlet chamber (6), and the outlet piston slides from the closed position to the opening position to allow escaping of compressed gas into the outlet chamber.    USE - Piston-type transfer pump device for transferring granular solid matter such as biomass fuel i.e. carbonaceous powder material, between compression and discharge chambers of a biomass gasification reactor (claimed). Can also be used for a fluidized bed reactor.    ADVANTAGE - The device transfers the granular solid matter under different pressures in a simple, efficient, reliable, pollution-free and cost-effective manner. The inlet piston delimits the volume of the compression chamber in the closure position such that the pressure in the volume is equal to that of the outlet chamber, thus enabling transfer of the granular solid matter with reduced energy consumption. The device has a compact structure and is operated in a safe manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for transferring granular solid matter between two chambers under different pressures.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a piston-type transfer pump device.    Piston-type transfer pump device (1)    Tubular jacket (2)    Inlet piston (3)    Inlet piston (4)    Outlet chamber (6)    Inlet (20)    Outlet (21)
NOVELTY - The apparatus (1) has a fuel tank (24) that is provided with a supply port (23) for supplying the fluid fuel to the electric power generation unit (12). The electric power generation unit is provided with a receiving opening connected with the supply port so that electric power is generated using fuel received from fuel tank through the receiving opening. The top wall portion of fuel tank is adjoined with bottom wall portion in a position. The supply port is provided in the corner of the both wall portions.    USE - Electric power generating apparatus for charging battery pack of electrical tool used in construction field.    ADVANTAGE - The malfunctioning generated by gas mixing to the flow path at the side of a fuel liquid can be prevented. The size of the electric power generating apparatus can be reduced and the production cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electric power generating apparatus. (Drawing includes non-English language text)    Electric power generating apparatus (1)    Housing (2)    Electric power generation unit (12)    Supply port (23)    Fuel tank (24)
NOVELTY - Preparing high purity L-alpha glycerylphosphorylcholine involves (a) hydrolyzing a phospholipid solution containing phosphatidylcholine by phospholipase A1 in the presence of calcium salt (CaXn) to prepare a glycerylphosphorylcholine (GPC) mixture; and (b) using a silica gel column chromatography to separate L- alpha -GPC from the GPC mixture.    USE - For preparing L-alpha glycerylphosphorylcholine (claimed) which is used as the precursor for making acetylcholine and phosphatidylcholine in the body; for enhancing cognitive ability and even repairing the partial damaged cognitive ability in early Alzheimer's disease; for protecting liver tissues from poisonous carbon tetrachloride and fatty acid penetration caused by high lipoprotein diet; and for enhancing body's resistance to high blood fat and protect blood vessels.    ADVANTAGE - The method is simple, cost-effective, environmentally friendly, and can be adaptable to large-scale industrial production; and provides L-alpha glycerylphosphorylcholine with high yield (i.e. up to 78.4%) and high chemical and optical purity (i.e. up to 99.8%) without using harmful organic solvents.
NOVELTY - Hydrogen power supply module (40), comprises: hydrogen production unit (42) for storing solid-state reactant; fuel cell unit (44) at least comprising membrane electrode assembly and anode current-collector and cathode current-collector separately disposed on two sides of membrane electrode assembly; and hydrogen flow channel (46) in communication with hydrogen production unit and fuel cell unit, where liquid-state reactant reacts with solid-state reactant to produce hydrogen when liquid-state reactant comes into contact with solid-state reactant.    USE - The hydrogen power supply module is useful in life preserver.    ADVANTAGE - The hydrogen power supply module: exhibits instant and miniature power supply; has competent portability and easy production; and has compliance with environmental standards.    DETAILED DESCRIPTION - Hydrogen power supply module (40), comprises: hydrogen production unit (42) for storing solid-state reactant; fuel cell unit (44) at least comprising membrane electrode assembly and anode current-collector and cathode current-collector separately disposed on two sides of membrane electrode assembly; and hydrogen flow channel (46) in communication with hydrogen production unit and fuel cell unit, where liquid-state reactant reacts with solid-state reactant to produce hydrogen when liquid-state reactant comes into contact with solid-state reactant, and hydrogen flows into fuel cell unit via hydrogen flow channel. An INDEPENDENT CLAIM is also included for a life preserver, comprising a portable carrier and the hydrogen power supply module connected with the portable carrier.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of life jerkin having a hydrogen power supply module.    Hydrogen power supply module (40)    Hydrogen production unit (42)    Fuel cell unit (44)    Hydrogen flow channel (46)    Life jerkin (48)
NOVELTY - An isolated, biologically pure hemiascomycetes yeast strain comprising as metabolic pathways for the catabolism of fatty acid at least one peroxisomal beta -oxidation fatty acid oxidation gene 2 (FOX2) independent pathway, at least one peroxisomal beta -oxidation FOX2 dependent pathway, and at least one mitochondrial beta -oxidation FOX2 dependent pathway, is new.    USE - The isolated strain is useful for producing commodity chemicals. The isolated strain is useful for producing long chain fatty acids; triacylglycerols and ester derivatives; phospholipids, phospholipids esters, phospholipids mono and/or di-esters, and biodiesel; decalactone; lipid derived flavorings and/or fragrances; terpens, sesquiterpens, as well as their adehydes and esters derivatives; where the fatty acids are saturated, mono and/or polyunsaturated fatty acids, or where the fatty acids are in C16-C24, such as preferably linoleic acid or gamma -linoleic acid. The isolated strain is useful for producing lactones, where the lipid derived flavorings and/or fragrances are fruit and/or milk flavorings, preferably saturated and unsaturated delta -and gamma -lactones, or where the lipid derived flavorings and/or fragrances are peach-like flavorings, preferably gamma -decalactone, delta -decalactone, and/or gamma -octalactone, or where the lipid derived flavorings and/or fragrances are coconut milk-like flavorings, preferably 4-dodecanolide and/or 4-octanolide (all claimed).    ADVANTAGE - The isolated strain is used for improved production of commodity chemicals with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of producing commodity chemicals by providing the isolated strain above; growing the strain in a suitable medium; and recovering the commodity chemicals.
NOVELTY - Method for processing organic waste, involves subjecting target organic waste to high temperature or ultra-high-temperature solubilization process using high temperature solubilization microbe or ultra-high-temperature solubilization microbe, and subjecting the solubilized waste to anaerobic digestion treatment.    USE - The method and apparatus are useful for processing organic waste which is used for producing biogas, preferably hydrogen and methane (all claimed). The organic waste is chosen from sewage sludge, organic refuse, and livestock farming excrement.    ADVANTAGE - The method is stable, produces biogas at very high yield, and reduces volume concentration of organic waste.    DETAILED DESCRIPTION - Method for processing organic waste, involves subjecting target organic waste to high temperature or ultra-high-temperature solubilization process using high temperature solubilization microbe or ultra-high-temperature solubilization microbe, and subjecting the solubilized waste to anaerobic digestion treatment. The method involves subjecting sludge chosen from (i) anaerobic digestion sludge obtained from the anaerobic digestion process, (ii) anaerobic digestion thickened sludge obtained by carrying out the separation concentration process of the anaerobic digestion sludge obtained from the anaerobic digestion process, and (iii) anaerobic digestion dewatered sludge obtained by dehydrating the anaerobic digestion sludge obtained from the anaerobic digestion process as a supply source for high temperature or ultra-high-temperature solubilization process. An INDEPENDENT CLAIM is included for apparatus for processing organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram of organic waste processing apparatus. (Drawing includes non-English language text)    High temperature or ultra-high-temperature solubilization tank (2)    Anaerobic digestion tank (3)    Solid-liquid separation tank (6)    Dehydrator (7,8)
NOVELTY - The system (10) has a water electrolysis apparatus (12) which electrolyzes water to generate oxygen and high pressure hydrogen. A gas liquid separator (52) which isolates the moisture content is positioned by a hydrogen piping (50). A high-pressure hydrogen derivation piping leads-out the high-pressure hydrogen in which the water is isolated. The drain piping (56) discharges water from the gas-liquid separator. The controlling-valve apparatus (78) connects the water electrolysis apparatus, hydrogen piping, gas-liquid separator and hydrogen derivation piping.    USE - High-pressure water electrolysis system installed in electric vehicle.    ADVANTAGE - The dissolved hydrogen is collected effectively. The durability of the high-pressure water electrolysis system is enhanced. The pressure water electrolysis system is installed effectively. The water electrolysis process is performed stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of the high-pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Water electrolysis apparatus (12)    Hydrogen piping (50)    Gas liquid separator (52)    Drain piping (56)    Controlling-valve apparatus (78)
NOVELTY - A fuel cell system (100) comprises a modifier (15) which generates reformed gas containing hydrogen from supplied mixed gas, a fuel cell (11), from which reformed gas is supplied to anode pole (11b) and air is supplied to cathode pole (11a) and water vapor is generated at anode pole, a circulation unit for circulating anode exhaust gas discharged from anode pole of fuel cell to modifier, a fuel-supply unit for supplying fuel, a air-supply unit for supplying air, a mixed gas-supply unit for supplying mixed gas of circulating gas and air to modifier, and a control unit.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system has improved fuel cell modification efficiency.    DETAILED DESCRIPTION - A fuel cell system comprises a modifier which generates reformed gas containing hydrogen from supplied mixed gas, a fuel cell, from which reformed gas is supplied to anode pole and air is supplied to cathode pole and water vapor is generated at anode pole, a circulation unit for circulating anode exhaust gas discharged from anode pole of fuel cell to modifier, a fuel-supply unit for supplying fuel, a air-supply unit for supplying air, a mixed gas-supply unit for supplying mixed gas of circulating gas and air to modifier, and a control unit which controls the fuel-supply amount by fuel-supply unit, air-supply amount by air-supply unit and circulating gas-supply amount by circulating unit such that the ratio of water and carbon of mixed gas supplied to modifier is fixed.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of fuel cell system. (Drawing includes non-English language text)    Fuel cell (11)    Cathode pole (11a)    Anode pole (11b)    Fuel modifier (15)    Fuel cell system (100)
NOVELTY - A low organic sludge anaerobic sludge fermentative production of methane gas comprises mixing concentrated sludge and dewatered sludge to prepare mixed sludge, subjecting mixed sludge for anaerobic digestion, and collecting methane gas. Content of mixed sludge is 85-95%. Volatile organic solid is 20-45%. Anaerobic digestion sludge in the sewage treatment process time is 20-30 days.    USE - Low organic sludge anaerobic sludge fermentative production of methane gas.    ADVANTAGE - The method shortens low organic material sludge anaerobic starting time, increases organic material sludge anaerobic digestion gas amount, and promotes low organic material sludge resource utilization.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a low organic sludge anaerobic sludge fermentative production of methane gas. (Drawing includes non-English language text).
NOVELTY - A sludge two-phase reflux heating strengthening anaerobic digestion technology comprises mixing the concentrated sludge and dewatered sludge to prepare mixed sludge, taking the mixed sludge hydrolysis acidification reaction, carrying out heat-treatment on the returned sludge, and circulating for hydrolysis acidification reaction, carrying out the methane from the hydrolysis acidification reaction stage discharging sludge, and collecting methane.    USE - A sludge two-phase reflux heating strengthening anaerobic digestion technology.    ADVANTAGE - The method has high processing efficiency and stable operation, and is suitable for large sewage treatment plant.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the sludge two-phase reflux heating strengthening anaerobic digestion technology (Drawing includes non-English language text).
NOVELTY - Method for preparing bioactive protein feed involves preparing seed culture liquid of Aspergillus niger and Saccharomyces cerevisiae, inoculating the cultured liquids to liquid culture medium in fermentation tank, obtaining mature culture broth, inoculating the mature culture broths into sterilized bran, mixing the bran to obtain compound microbial distillers yeast, crushing straws, mixing the distillers yeast with urea, inoculating the mixture into crushed straws, fermenting mixture, drying fermented straw and extruding and molding dried particles.    USE - The method is useful for preparing bioactive protein feed (claimed).    ADVANTAGE - The method prepares protein feed that is capable of replacing coarse feed of ruminants, and having excellent palatability and high nutrient content.    DETAILED DESCRIPTION - Method for preparing bioactive protein feed by straw fermentation involves (a) culturing Aspergillus niger and Saccharomyces cerevisiae in a tube, shaking culture tubes, preparing seed culture liquid for culturing the strains in tank, inoculating the cultured liquids (8-25 vol.%) to liquid culture medium in fermentation tank and incubating the liquids for 20-48 hours to obtain mature culture broth, (b) inoculating the mature culture broths into sterilized bran at a ratio of 5-6:4-5, incubating the bran at 22-34 degrees C for 20-48 hours and mixing the bran to obtain compound microbial distillers yeast, (c) crushing straws into particles having diameter of less than 1 cm, mixing the cultured compound microbial distillers yeast (1-5 wt.%) with urea, inoculating the mixture into the crushed straws, adding water (70-130 wt.%), uniformly stirring the mixture and fermenting the mixture at 20-36 degrees C for 20-48 hours, and (d) dehydrating and drying the fermented straw particles using a dryer until the moisture content is less than 12%, and extruding and molding the particles.
NOVELTY - Use of liliaceae in purifying livestock breeding biogas slurry, is claimed, where the liliaceae is planted in a polluted environment of the livestock breeding biogas slurry.    USE - The liliaceae is useful for purifying livestock breeding biogas slurry, where a regular harvest part of liliaceae is useful for pharmaceutical purposes (claimed) such as for treating tuberculosis, cough haemoptysis, chronic bronchitis, asthma and rheumatoid arthritis.    ADVANTAGE - The liliaceae effectively and simply purifies the livestock breeding biogas slurry in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an automatic oxygen supplying artificial wetland system, where an inner part of a bed part of the wetland consists of a wetland filling substrate and shale hollow bricks. Oxygen is supplied to the inner part of the wetland system through gaps between the shale hollow bricks. A grain size of the filling substrate and the filling thickness are both processed by artificial screening. The wetland is filled with a gravel layer with 15 cm thickness and 10-20 mm grain size, a slag layer with 20 cm thickness and 1-10 mm grain size and sandy soil layer of 15 cm thickness.
NOVELTY - The system has negative electrode reaction tank (130) that is provided with positive-electrode electrolytic vessel (120) provided with positive electrode (240) and negative electrode (230). Inlet tube (500) is set to supply hydrogen generated from reaction tank of hydrogen-producing apparatus (100) to carburetor or intake manifold (101) of engine (900) through regulating valve (400) and mixed with air to burn with fossil fuel. An electrolysis controller (600) is set to control and supply electric power of battery to positive electrode and negative electrode.    USE - Hydrogenation system for vehicle such as gasoline-engine vehicle and diesel engine vehicle such as environment-friendly car.    ADVANTAGE - Since the electrolysis controller is set to control and supply electric power of battery to positive electrode and negative electrode, the vehicle hydrogenation system uses hydrogen with high combustion efficiency for vehicle fuel and the running performance of vehicle by fossil fuel can be improved. The hydrogen-producing apparatus can be mounted in vehicle easily so that the need to need to mount the storage facility with dangerous hydrogen of explosion in large quantities can be avoided and the safety of the electric vehicle can be ensured. Hence the hydrogen-producing apparatus can be manufactured at low cost and the emission of carbon-dioxide can be avoided in the manufacturing process of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vehicle hydrogenation system. (Drawing includes non-English language text)    Hydrogen-producing apparatus (100)    Intake manifold (101)    Positive-electrode electrolytic vessel (120)    Negative electrode reaction tank (130)    Negative electrode (230)    Positive electrode (240)    Regulating valve (400)    Inlet tube (500)    Electrolysis controller (600)    Engine (900)
NOVELTY - Waste lime and food waste are dehydrated and pulverized to 100 mesh. Yellow soil powder, elvan powder, zeolite powder, germanium stone powder, and feldspar powder are mixed to obtain an additive. (In wt.%) waste lime powder (15-20), waste coal powder (15-20), food waste powder (30-35), iron ore powder (15-20), waste oil (8-12), and the additives (13-17) are mixed. The obtained mixture (90-95) and water (5-10) are mixed, pelletized using a pellet molding machine, and dried to obtain a magnetized solid type fuel.    USE - Manufacture of magnetized solid type fuel (claimed).    DETAILED DESCRIPTION - Waste lime and food waste are dehydrated in a dehydrator and a dryer to a moisture content of 30-50%. Waste lime, food waste, waste coal, iron ore, yellow soil, elvan, zeolite, germanium stone, and feldspar are then pulverized in a pulverizer to obtain the corresponding powders of 100 mesh. Yellow soil powder, elvan powder, zeolite powder, germanium stone powder, and feldspar powder are mixed to obtain an additive. (In wt.%) waste lime powder (15-20), waste coal powder (15-20), food waste powder (30-35), iron ore powder (15-20), waste oil (8-12), and the additives (13-17) are mixed. The obtained mixture (90-95) and water (5-10) are mixed, pelletized using a pellet molding machine, and dried to obtain a magnetized solid type fuel. An INDEPENDENT CLAIM is included for magnetized solid type fuel.
NOVELTY - Hydrodeoxygenation of supply material containing triglyceride is carried out, and byproduct is separated into gas component and liquid component. Impurities (DD) and light components are separated from liquid component. Isomerization (II) and recirculation of some byproducts are carried out and mixed with supply material, and remainder is obtained as final product (KK). Thus, biodiesel of paraffin form is produced.    USE - Manufacture of biodiesel of paraffin form.    ADVANTAGE - The biodiesel of paraffin form is efficiently produced without generating side reaction. The excessive temperature increase of reactant is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining manufacture of biodiesel. (Drawing includes non-English language text)    Feed Oil (AA)    Impurities (DD)    Water (FF)    Isomerization (II)    Product (KK)
NOVELTY - The apparatus has a pulverizing unit (12) which pulverizes the food waste (S). A fermenter (22) is equipped with microbe habitation carrier (23), in order to ferment crushed material. A transfer pipe (28) is provided to transfer fermentation product processed at fermenter. A stirring unit (36) is equipped in agitation vat (34). A microbe habitation carrier (24) is provided to habitat microorganism to inner side bottom. An air pump (27) is connected with air supply pipe (26), in order inhale and supply external air to microbe habitation carrier.    USE - Food garbage disposal apparatus used in home, commercial enterprise, school, and public institution.    ADVANTAGE - The processing efficiency of the food waste can be improved effectively. The installation and maintenance of the food garbage disposal apparatus can be facilitated. The food garbage disposal apparatus has simple structure, convenient operation and can be manufactured with reduced cost. The generation of the environmental pollution can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory diagram of the food garbage disposal apparatus.    Pulverizing unit (12)    Fermenter (22)    Microbe habitation carriers (23,24)    Air supply pipe (26)    Air pump (27)    Transfer pipe (28)    Agitation vat (34)    Stirring unit (36)    Food waste (S)
NOVELTY - The generator has a power output load end connected with a buffer battery device and a potential energy converting kinetic energy device. An output end of the buffer battery device generates electrical resonance of oscillating eddy current to replace cutting magnetic field. A magnetic fuel cell stack generating device generates high frequency electric energy, and is provided with a winding iron core that is formed with a coil forming magnetic field loop. A kinetic energy conversion device comprises an electric damper and a high frequency capacitor.    USE - Magnetic generating symbiotic electric generator.    ADVANTAGE - The generator provides stable output power, and has better environment protection effect.    DETAILED DESCRIPTION - The potential energy converting kinetic energy device is an integrated circuit oscillator or exchange controller.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a magnetic generating symbiotic electric generator. '(Drawing includes non-English language text)'
NOVELTY - Method for disposing carcass animal flesh involves mixing carcasses of animal with microbial formulation, and decomposing the carcasses in aerobic conditions.    USE - The method is useful for disposing carcass animal flesh.    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - A mannanase separated from Clostridium cellulovorans and comprising a 657 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The mannanase is useful in composition for hydrolyzing galactomannan in lignocellulosic biomass (all claimed) which is useful for producing biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the mannanase;    (2) recombinant vector containing the gene;    (3) transformant obtained by transforming the above-cited vector;    (4) method for hydrolyzing galactomannan in lignocellulosic biomass, involves processing the lignocellulosic biomass with the above-cited enzyme; and    (5) composition comprising cellulosome complex comprising mannanase and endoglucanase-E.
NOVELTY - Biomass comprehensive transformation device comprises a pyrolysis tank, a tri-state purification separation device, a static separation device, a gas purification device, a gas storage tank and a pneumatic device, placed on a connecting pipe of the tri-state purification separation device and the gas purification device. The pyrolysis tank connected with the tri-state purification separation device. The tri-state purification separation device is connected with the static separation device and the gas purification device. The gas purification device is connected to the gas storage tank.    USE - Used as a biomass comprehensive transformation device.    ADVANTAGE - The device is simple in structure, easy to operate, simplifies the pyrolysis device, and is suitable for use in rural areas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the device for comprehensive transformation of biomass comprising compacting straw in the pyrolysis tank and performing ignition combustion, simultaneously opening pneumatic device for introducing oxygenated air, completing the combustion of the straw layer, adding straw, continuing reaction and adding straw in a uniform speed, transforming straw into mixed gas or gas mixture and biological carbon, where the biological carbon is left behind in the pyrolysis tank and is regular discharged, separating the mixed gas into a mixed liquid and non-condensable gases by passing through a tri-state purification separation device, passing the mixture liquid through the static separation device to obtain tar and pyroligneous liquor, processing the uncondensed gas in a gas purification device and passing into a gas storage tank to obtain biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass comprehensive transformation device.
NOVELTY - Method for continuous production of biological diesel oil using waste oil, mixing the waste oil and water in a ratio of 3:4 to carry out hydrolysis, preparing water-fatty acid for the hydrolysis of the crude fatty acid natural sedimentation for 0.5-5 hours for removing water and impurities, dealcoholizing the water-fatty acid, adding concentrated sulfuric acid into the esterification kettle, adding methanol, compressed gas, adding soda powder and stirring mixture, and processing the neutralized crude biodiesel by multistage distillation.    USE - The method is useful for continuous production of biological diesel oil using waste oil.    ADVANTAGE - The method does not require mechanical vacuum distillation, reduces reverse reaction, cooling equipment investment, labor intensity, and production of waste water, and is stable.
NOVELTY - Alkali and salt tolerant xylanase producing Streptomyces viridochromogenes comprising a preservation no. CGMCC No. 5565, is new.    USE - The strain is useful in industrial production of alkali salt tolerance xylanase (claimed); and degrading biomass containing hemicellulose, corn stalks, straw, Helianthus tuberosus stalks and seaweed fiber to produce bio-based chemicals. The xyalanse enzyme is useful as a marine-derived enzyme composition in paper making, food, feed, wine and other industries.    ADVANTAGE - The strain has good tolerance to oligotrophic conditions. The produced xylanase enzyme has high pH stability and thermal stability, and can tolerate high concentrations of sodium chloride.
NOVELTY - Deodorizing device comprises air suction mechanism and odor processing mechanism connected with the automatic control system, where the pumping mechanism, fermentation tank and odor processing mechanism are connected through pipeline.    USE - The deodorizing device is useful for producing bio-organic fertilizer.    ADVANTAGE - The deodorizing device reduces odor in fermentation tank, is environmentally-friendly and can be used continuously for three months. The materials filled in odor processing tank have strong adsorption effect.
NOVELTY - The furnace has a combustion cylinder installed in a water jacket furnace body. Height of a plate top surface is 5-10 cm. A plate is symmetrically arranged with multiple combustion holes. Center throat diameter of each combustion hole is 5 cm. An upper part of an outer bottom plate is provided with a flame guide groove along radial direction. The guide groove is connected to an end of a peripheral edge of the plate. Periphery of the plate is in arc-shape. Diameter of the plate is 10-18 cm. A top surface of the cylinder is provided with outlets.    USE - Multi-functional straw gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a multi-functional straw gasification furnace.
NOVELTY - Method for processing wastewater generated during paper making, involves reacting wastewater generated during papermaking and biomass together to obtain small molecule organic compound.    USE - The method is useful for processing wastewater generated during paper making for processing of biomass for producing small molecule organic and aromatic compound (all claimed).    ADVANTAGE - The method is environmentally-friendly, and produces high yield of organic and aromatic compound.
NOVELTY - Method for preparing fuel, involves using raw materials chosen from (in wt.%): methanol (60-93), benzene (10-40), gasoline (40), and additive (2-5).    USE - The method is useful for preparing fuel.    ADVANTAGE - The method is simple, rapid, multifunctional and environmentally-friendly. The method enables producing fuel safely under normal temperature and pressure, can replace the cooking fuel and diesel used in boiler and gas turbine and reaches output power at high rate. The obtained fuel has corrosion resistance, high octane content, no transparent layer, and replaces ignition components with gasoline easily.
NOVELTY - Organic fertilizer, is claimed, where the fertilizer is prepared by fermenting and crushing collected edible fungi leftovers, adding water and chitosan oligosaccharide to the crushed leftovers, piling the mixture, covering a plastic film, fermenting the mixture, drying the fermentation material, crushing into fine particles, adding inorganic fertilizer into the fine particles, drying the edible fungi and crushing into the particles, adding urea, potassium sulfate and diammonium phosphate inorganic fertilizer into crushed particles, and uniformly stirring and sealing the particles.    USE - The organic fertilizer is useful for growing green vegetables and fruit tree.    ADVANTAGE - The organic fertilizer improves yield and quality of the fruits.    DETAILED DESCRIPTION - Organic fertilizer, is claimed, where the fertilizer is prepared by fermenting and crushing collected edible fungi leftovers, adding water and chitosan oligosaccharide to the crushed edible fungi leftovers and keeping in water at 45%, where ratio of sugar and leftovers is 1:200, piling the mixture under weather condition of the lowest outdoor temperature of more than 10 degrees C, covering a plastic film, fermenting the mixture for 10-20 days, drying the fermentation material, crushing into fine particles, adding inorganic fertilizer into the fine particles, drying the edible fungi and crushing into the particles, adding urea, potassium sulfate and diammonium phosphate inorganic fertilizer in a ratio of 40:30:20:10 into crushed particles, and uniformly stirring and sealing the particles.
NOVELTY - Electronic grade ultra-pure ammonia purifying device comprises a liquid ammonia storing tank, a liquid ammonia pump, a carburetor, an eliminator, a rectifying tower, a purifier, a condenser and a product storage tank. The rectifying tower comprises first and second rectifying towers. The pump passes the liquid ammonia into the liquid ammonia storage tank and carburetor. The carburetor is connected to the eliminator, which is connected to the first rectifying tower. The first rectifying tower from tower top is connected to the second rectifying tower. The purifier is connected to the condenser.    USE - Used as an electronic grade ultra-pure ammonia purifying device.    ADVANTAGE - The device: simplifies the refining process; greatly reduces the energy consumption; improves the production efficiency; utilizes electronic grade ultra-pure ammonia automatic online detection device comprising sampling assembly and a control system; has short sampling time; and analyzes the quality of the product to control the production process.
NOVELTY - Bait comprises photocatalyst material containing apatite having photocatalytic activity.    USE - The bait is used in tool for breeding livestock feed, and feed for fish and shellfishes in hen house, pigsty, dairy cow shed, farm, poultry farm, hoggery, water tank for breeding fish and shellfishes, and fishery of fish and shellfishes. The breeding tool includes vehicle, clothes, spectacles, bucket, shovel, feed box, glove, boots, egg case, and raiser (all claimed).    ADVANTAGE - The method is simple and environmentally-friendly, and enables to prevent livestock and fishes from pathogens including virus, bacteria and fungi during breeding, and hence white spot disease and tail rot disease can be prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) breeding tool containing an unit for holding the photocatalyst material to contact pathogen;    (2) breeding environment facility containing the holding unit; and    (3) method for preventing infection caused by pathogen, involves providing photocatalyst material containing apatite in the rearing facility and out of the breeding environment.
NOVELTY - Methane utilization system comprises a gas generator for producing fermenting gas by waste, and a gas separation membrane assembly connected with the gas generator. The membrane assembly is used for separating the fermenting gas from the gas generator into a first gas product taking methane as a main component and a second gas product taking carbon dioxide as a main component.    USE - Used as a methane utilization system.    ADVANTAGE - The utilization system recycles carbon dioxide and heat of the catalytic combustion, improves the recovery rate of the first gas product and energy utilization efficiency, produces the first gas product with high content of methane, and improves the value of methane in a large-scale.
NOVELTY - Tropisetron is synthesized by conducting esterification reaction of indole-3-formic acid and tropine in an inert solvent in the presence of a catalyst that is an aromatic organic sulfonic acid compound.    USE - Method for synthesis of tropisetron (claimed).    ADVANTAGE - The method has simple technology and easy operation and slight pollution, achieves high product purity and ideal yield, and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparation of Tropisetron hydrochloride comprising conducting synthetic reaction, extracting the Tropisetron in the gained reaction product with inorganic acid aqueous solution, adjusting the pH value of the extracted material to be 9-10, and conducting salt crystallization in the hydrochloric acid ethanol solution.
NOVELTY - An oleuropein is extracted from olive leaves by cutting the olive leaves; adding purified water or aqueous ethanol solution in the cut olive leaves; extracting at low temperature; concentrating the extracted solution or using two macroporous adsorption resin series chromatography column or performing primary adsorption; concentrating and performing secondary adsorption; washing with purified water; eluting resin with 5-80% fatty alcohol; collecting the effluent when the concentration of fatty alcohol is 5%; concentrating the eluent at low temperature; and freezing or spray drying.    USE - Method for extraction of oleuropein from olive leaves (claimed).    ADVANTAGE - The method has advantages of saving power consumption, short production cycle, economic and environment protection, and simple operation. It is suitable for large-scale industrial production.
NOVELTY - Fermentation culturing of Bacillus vallismorti comprises seed cultivation and fermentation culturing work procedures, where the initial pH of the culture medium is 6-7, the strain temperature is 30-37 degrees C, nitrogen source dosage is 5-10 g/l, and the carbon source dosage is 15-25 g/l.    USE - The method is useful for producing a compound microbial fertilizer.    ADVANTAGE - The method effectively utilizes waste resources, and is ecofriendly and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a compound microbial fertilizer from Bacillus vallismorti, comprising (i) processing materials by crushing hydrolysis slag generated during the production process of the amino acids to obtain a powder or small particles, mixing with alkaline matter, adjusting the pH of the hydrolysis slag material after processing to 5.5-8, (ii) fermentation culturing Bacillus vallismorti by the above mentioned-method to obtain the bacterial agent after absorbing the fermentation liquid through an absorption medium, independently fermenting and producing Bacillus subtilis and Bacillus mucilaginosus to obtain the bacterial agent after absorbing the fermentation liquid through the absorption medium, and mixing and crushing the three bacterial agents, and (iii) adding the mixed bacterial agent into the materials obtained from the step (i) to obtain the finished product compound microbial fertilizer, where the mixed bacterial agent is 5-20% of the finished product compound microbial fertilizer.
NOVELTY - The system has a chamber (4) and a dry electrolysis part (5) that are provided with nano electrodes (17). Cathodes (20) are coated with nanoparticle layers i.e. graphene sheets. A hydrogen-oxygen generator (1) is connected to an electrolyte tank (7) for collecting ionized gas mixture through a pipe (6). The pipe is passed through an inner space of the tank. An electrolyte outlet tube (8) is connected to an upper part of the tank. The hydrogen and oxygen generator is connected to an air filter, an intake manifold part (11), a combustion chamber (2) and a motor truck (3) via a connecting hose.    USE - Energy system for connecting an ionized hydrogen-oxygen generator with a driving unit of camion.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an energy system.    Hydrogen-oxygen generator (1)    Combustion chamber (2)    Motor (3)    Chamber (4)    Dry electrolysis part (5)    Pipe (6)    Electrolyte reservoir (7)    Electrolyte outlet tube (8)    Intake manifold part (11)    Nano electrodes (17)    Cathodes (20)
NOVELTY - Methanol-gasoline blend comprises 30-50% denatured methanol and 50-70% modified gasoline, which are mixed uniformly and filtered. The denatured methanol comprises 60-82% methanol, 8-24% fatty alcohol, 4-8% fatty ether, 4-9% aliphatic ketone, 0.3-0.8% oxidant, 0.07-0.8% corrosion inhibitor, and 0.005-0.01% less volatile soluble compound containing fluorine (F), oxygen (O), and/or nitrogen (N).    USE - Methanol-gasoline blend.    ADVANTAGE - The methanol-gasoline blend achieves reduced vapor lock problem; can be used in extreme weather; has greatly increased safety and low cost; and is easily produced.    DETAILED DESCRIPTION - Methanol-gasoline blend comprises 30-50% denatured methanol and 50-70% modified gasoline, which are mixed uniformly and filtered. The denatured methanol comprises 60-82% methanol, 8-24% fatty alcohol, 4-8% fatty ether, 4-9% aliphatic ketone, 0.3-0.8% oxidant, 0.07-0.8% corrosion inhibitor, and 0.005-0.01% less volatile soluble compound containing F, O, and/or N. It is prepared by mixing and uniformly stirring at 500-800 revolutions/minute (rpm). The modified gasoline comprises 65-90% gasoline, 0-30% aromatic hydrocarbon, 0-10% naphtha, 0.07-0.8% defoamer, and 0.7-1.3% active agent. It is prepared by mixing and uniformly stirring at 500-800 rpm.
NOVELTY - A sugar beet silage methane fermentation method involves utilizing sugar beet silage as substrate, and regulating pH to perform biodegradation of organic matter into biogas, where the process is carried out in a biogas plant comprising fermenter piston for separating fermentation and methanogenesis zones.    USE - Method for methane fermentation of sugar beet silage.
NOVELTY - Circulating glyphosate waste liquor used for recycling in a glyphosate production system involves concentrating waste mother solution for forming concentrated solution, where an alkali liquid is added in the concentrated solution.    USE - Circulating glyphosate waste liquor used for recycling in glyphosate production system.    ADVANTAGE - The glyphosate waste liquor is recylced in a simple, eco-friendly and cost-effective manner with high yield and saves liquid alkali consumption.
NOVELTY - Method for reclaiming livestock stamping-out, involves making an inclination angle on the underground to obtain reclaiming hole, installing waterproof member on bottom surface of the reclaiming hole, installing sterilizing member on upper surface of the waterproof member, installing leach collecting pipe at one side of the reclaiming hole, introducing landfill cover after adding livestock into the reclaiming hole, fermenting the livestock by coating fermenting agent on the landfill cover, and collecting byproduct of the fermented livestock.    USE - The method is useful for reclaiming livestock stamping-out.    ADVANTAGE - The method is rapid and environmentally-friendly.    DETAILED DESCRIPTION - Method for reclaiming livestock stamping-out, involves making an inclination angle on the underground to obtain reclaiming hole, installing waterproof member on bottom surface of the reclaiming hole, installing sterilizing member on upper surface of the waterproof member, installing leach collecting pipe at one side of the reclaiming hole, introducing landfill cover after adding livestock into the reclaiming hole, fermenting the livestock by coating fermenting agent on the landfill cover, and collecting byproduct of the fermented livestock through the leach collecting pipe.
NOVELTY - Preparation of a modified starch adhesive comprises oxidizing a plant starch to obtain oxidized starch; and adding a gelatinizing agent to the oxidized starch, and crosslinking.    USE - Method for the preparation of modified starch adhesive (claimed) used for granulating organic fertilizer.    ADVANTAGE - The method is inexpensive, environment-friendly, and achieves better granulation adhesion effect. The modified starch adhesive improves transportation and utilization rates of the organic fertilizer, and enhances the promotion application efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a modified starch adhesive.
NOVELTY - The device has a sealed box type outer container provided with a gas inlet and a gas outlet at a side top part. A partition wall is formed with a fluid path and utilized for separating multiple cooling pipes from each other in the outer container in horizontal direction. The partition wall is formed in an upper side or a lower-side of the outer container. A stack is provided with a vent at a top side part, and penetrates through the cooling pipes. A ventilation fan is equipped in the vent and utilized for generating suction force.    USE - Environment-friendly cooling device for use in an environment-friendly mature fermentation fertilizer manufacturing apparatus (claimed).    ADVANTAGE - The device enables condensing moisture generated during fertilizing process. The device enables the environment-friendly mature fermentation fertilizer manufacturing apparatus to produce fertilizer using processed life waste, so that bad smell is removed, and contaminants are prevented from being ejected out. The inside part of the fertilizer manufacturing apparatus is segmented to multiple spaces, and the life waste is consecutively administered to the fertilizer manufacturing apparatus, so that the waste is successively passed through the segmented spaces, thus achieving consecutive production of high-quality fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an environment-friendly mature fermentation fertilizer manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an environment-friendly cooling device.'(Drawing includes non-English language text)'
NOVELTY - An additive manufacturing method involves preparing Big-cone pine improper languge and Aralia elata Seeman hit. The Big-cone pine improper languge and the Aralia elata Seeman hit are washed. The washed Big-cone pine improper languge and the Aralia elata Seeman hit are distilled at constant temperature for predetermined time. The distilled Big-cone pine improper languge and the Aralia elata Seeman hit are classified into an additive.    USE - Method for manufacturing additive that is utilized for cultivating wild greens.    ADVANTAGE - The method enables growing green bean sprouts to produce high quality wild greens in a reliable and environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an additive.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing additive.'(Drawing includes non-English language text)'
NOVELTY - Bio-fertilizers and/or organic fertilizer composting and pelletization involve using co-products, agricultural residues and agro-industrial products. The composting process is performed according to physico-chemical-mechanical properties of material, where the material is processed in autoclave without contacting water vapor with waste products in order to obtain bio-fertilizer. An extruder is utilized to obtain fertilizer, where the extruder has a nozzle. Oil is automatically injected to the extruder, particularly cottonseed oil or sludge oil.    USE - Method for composting and pelletizing bio-fertilizers and/or organic fertilizer (claimed).    ADVANTAGE - The bio-fertilizers and/or organic fertilizer composting and pelletizing method is useful on industrial scale.    DETAILED DESCRIPTION - Bio-fertilizers and/or organic fertilizer composting and pelletization involve using co-products, agricultural residues and agro-industrial products. The composting process is performed according to physico-chemical-mechanical properties of material, where the material is processed in autoclave without contacting water vapor with waste products in order to obtain bio-fertilizer. An extruder is utilized to obtain fertilizer, where the extruder has a nozzle. Oil is automatically injected to the extruder, particularly cottonseed oil or sludge oil. Bio-fertilizer and/or organic fertilizer are utilized in pellet form, where water vapor is removed by cottonseed oil or sludge oil.
NOVELTY - The method involves obtaining concentration of water-soluble humic acid. The water-soluble humic acid is poured in an aeration tank (33) through a blower (51) for 24 hours. The water-soluble humic acid is supplied to a mixture tank (50). The water-soluble humic acid is stored in a reservoir (60). The mixture tank suspends material oxidation through a rice hulls waterspout (70) to remove impurity. Night soil sludge is mixed in an original water tank (40). A bio-reactor (31a) is provided by another aeration tank (35).    USE - Method for preparing livestock excretions reducing odor based liquefied fertilizer.    ADVANTAGE - The method enables improving seed production so as to increase income of a farmhouse. The method enables reducing damage to the seed by continuous cropping function when extracting large distress of nutritive element. The method enables reducing sample reduction transaction problem in a better manner. The method enables satisfying livestock excretion effluent standard through a microbial treatment by utilizing the bio-reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a livestock excretions reducing odor based liquefied fertilizer manufacturing method. '(Drawing includes non-English language text)'    Bio-reactor (31a)    Aeration tanks (33, 35)    Original water tank (40)    Mixture tank (50)    Blower (51)    Reservoir (60)    Rice hulls waterspout (70)
NOVELTY - Improving yield of ethane and propylene, comprises (a) feeding methanol as a raw material to the reaction at the gas line speed of 1-3 meters/second to contact catalyst, to obtain product stream of ethylene, propylene, and catalyst, (b) dividing the catalyst into at least two parts, returning one part to the reaction zone and feeding the other part to the regenerator to form the regenerated catalyst, and (c) deaerating the regenerated catalyst and then feeding to 1/3-4/5 height of reaction zone, where the conversion rate of methanol is more than 30%.    USE - The method is useful for improving yield of ethane and propylene.    ADVANTAGE - The method is capable of economically improving yield of ethane and propylene in large scale.    DETAILED DESCRIPTION - Improving yield of ethane and propylene, comprises (a) feeding methanol as a raw material to the reaction at the gas line speed of 1-3 meters/second to contact catalyst containing silicoaluminophosphate molecular sieve catalyst, to obtain a product stream of ethylene, propylene, and catalyst, (b) dividing the catalyst into at least two parts, returning one part to the reaction zone, and feeding the other part to the regenerator to form the regenerated catalyst with active index more than 0.7, and (c) deaerating the regenerated catalyst and then feeding to 1/3-4/5 height of reaction zone.
NOVELTY - The device (100) has a fermentation degradation tub which is provided for opening and closing the cover (10a) to inject the food. An aging decomposition bath provided with partition wall is installed in the fermentation degradation tub. The analysis completion tub provided with partition wall is perpendicularly installed in the bottom surface of the aging decomposition bath. The thermal medium storage tank (60) is installed with respect to analysis completion tub, fermentation degradation tub and aging decomposition bath.    USE - Manufacturing device of solid burning fuel and fertilizer.    ADVANTAGE - The carbon generation can be reduced in environment-friendly manner. The bad smell produced during fermentation degradation of microorganism can be prevented without any need for purifier. The structure of the device can be simplified with reduced manufacturing cost and maintenance cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of fertilizer.    Supporting frame (4)    Cover (10a)    Thermal medium storage tank (60)    Heater (62)    Manufacturing device of solid burning fuel and fertilizer (100)
NOVELTY - System comprises hopper (110), first classifying pulverizer (120), dehydrator (130), fine pulverizer (140), dissolving bath (150), first methane fermenting bath (160), second methane fermenting bath (170), solid-liquid separator (180), solid storing tank (190), filtering liquid storing tank (200), desulfurizer (210) and gas holder (220).    USE - The system and method are useful for processing food waste for producing methane gas, fermented feed, and liquid fertilizer (claimed).    ADVANTAGE - The system improves quality of fermented feed and liquid fertilizer and prevents environmental contamination.    DETAILED DESCRIPTION - System comprises hopper (110), first classifying pulverizer (120), dehydrator (130), fine pulverizer (140), dissolving bath (150), first methane fermenting bath (160), second methane fermenting bath (170), solid-liquid separator (180), solid storing tank (190), filtering liquid storing tank (200), desulfurizer (210) and gas holder (220). The dissolving bath stores effluent from the fine pulverizer and solid materials supplied from the outside and solubilizes the effluent. The first methane fermenting bath generates methane gas by fermenting the solubilized effluent. The desulfurizer desulfurizes the methane gas. The gas holder stores the methane gas from the desulfurizer. An INDEPENDENT CLAIM is included for method for processing food waste, which involves using the above-cited system.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of system.    Hopper (110)    First classifying pulverizer (120)    Dehydrator (130)    Fine pulverizer (140)    Dissolving bath (150)    First methane fermenting bath (160)    Second methane fermenting bath (170)    Solid-liquid separator (180)    Solid storing tank (190)    Filtering liquid storing tank (200)    Desulfurizer (210)    Gas holder (220)
NOVELTY - The method involves spreading liquefied fertilizer. The aging of aerobic microorganism is performed for reducing bad smell. The ripening of waste is completed and is recycled to seed. The percentage of water content modulation of the compost deposit tank is provided, after allowing aeration through after residue microorganism. The aerobic microorganism is purified, after the solid-liquid separation is performed inside the tank. The leachate generated in input is reused for fermentation to the leachate reservoir.    USE - Organic waste composting method.    ADVANTAGE - The activation of the aerobic microorganism can be maximized according to the caustification and fermenticide for minimizing the amount of the moisture content, so that the degradability can be secured as well as the generation of bad small can be prevented. Hence the environment can be protected safely.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the organic waste composting process. (Drawing includes non-English language text)
NOVELTY - The system has a hydrogen transmission pipe connected to a side of a seawater electrolysis facility. The hydrogen transmission pipe is connected to a fuel cell. The hydrogen transmission pipe supplies an effluent generated in an electrolysis process to produce electricity. A hydrogen storage part is connected to the hydrogen transmission pipe. A hydrogen refining facility refines the hydrogen storage part to generate high purity hydrogen.    USE - Fuel cell and hydrogen charge combined system for a seawater electrolysis facility.    ADVANTAGE - The system generates power from the cooling water emitted in a nuclear power generation and a thermal power generation system, so that the waste heat of the cooling water ejected in the fuel cell can be utilized, thus suppressing the generation of carbon dioxide gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell and hydrogen charge combined system.'(Drawing includes non-English language text)'
NOVELTY - The invention relates to an organic treatment equipment and method for animal bones in which an engine bed is disposed with an input port located on a top portion of the engine bed and a stirring tank located below the input port, and a channel for animal bones to be input from the input port is formed between the input port and the stirring tank, wherein crashing means for dismembering and twisting animal bones that fall into the stirring tank are installed on the channel, and stirring and heating means are disposed to the engine bed to stir, steam boil and dry crashed animal bones in the stirring tank for a while. Further, proper amount of water, thermophilic bacterium having a certain dosage and a predetermined weight percentage of culture medium can be injected into the stirring tank. Accordingly, after the processes of the foregoing stirring, steam boiling and drying is performed, the crashed animal bones can ferment and be decomposed into powder organic substances.
NOVELTY - Catalyst comprises: a semiconductor; and a semiconductor material having elevated phosphorus content.    USE - The catalyst is useful in a water splitting process (claimed).    ADVANTAGE - The catalyst: is insoluble in water and some other common solvents; exhibits improved stability, and reduced over-potential of electrodes; performs more efficient electrochemical reactions; and can be manufactured in a more cost efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the semiconductor or the semiconductor material of the catalyst, comprising either: (a1) preparing an aqueous solution comprising at least one principal electrolyte, and at least one supporting electrolyte, (b1) applying a source of energy to the aqueous solution, and (c1) depositing the principal electrolyte, and optionally the supporting electrolyte at a cathode using electrolysis; or (a2) preparing an ionic liquid comprising at least one electrolyte, (b2) applying a source of energy to elevate the temperature of the ionic liquid to at least 130 degrees C, and (c2) depositing the electrolyte at a cathode using electrolysis;    (2) electrodeposition process, comprising the steps (a2)-(c2) as above per se;    (3) the semiconductor comprised in the catalyst; and    (4) the semiconductor material having elevated phosphorus content comprised in the catalyst.
NOVELTY - A carbon-monoxide-conversion catalyst comprises copper-zinc-aluminum catalyst containing copper, zinc, aluminum, and oxygen in which the copper, zinc, and aluminum are converted into copper oxide (30-90 mass%), zinc oxide (3-30 mass%) and aluminum oxide (7-60 mass%). The copper oxide has specific surface area of 80-200 m2/g, crystalline diameter of less than or equal to 120 Angstrom , volume density of 0.6-1.5 g/cm3, pore volume of 0.3-0.6 cm3/g and average pore radius of 45-120 Angstrom .    USE - Carbon-monoxide-conversion catalyst for hydrogen production process (claimed). Can also be used in domestic fuel cell or vehicle fuel cell, and as hydrogen production catalyst, methanol synthesis catalyst, high temperature shift catalyst of water gas shift reaction, and steam-reforming catalyst of methanol other than the low-temperature shift catalyst of water gas shift reaction.    ADVANTAGE - The catalyst is excellent in activity and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of the carbon-monoxide-conversion catalyst involving coprecipitating the metal salt solution containing copper, zinc, and aluminum and precipitant containing aqueous solution obtaining a catalyst precursor, cleaning the catalyst precursor, drying the catalyst precursor, molding the catalyst precursor, baking the molded catalyst precursor, and adding deposit containing organic compound additive before the molding process;    (2) carbon-monoxide-conversion process involving reducing carbon monoxide concentration in the hydrogen-containing-gas which contains carbon monoxide by carbon monoxide shift reaction in 150-500 degrees C using the carbon-monoxide-conversion catalyst; and    (3) hydrogen production process involving reducing the carbon monoxide concentration without using carbon monoxide selective-oxidation reaction after reducing the carbon monoxide concentration by the carbon-monoxide-conversion process.
NOVELTY - The method involves fastening (S120) the laminated (S100) several fuel stacks. An aging treatment process (S110) is performed to advance initial stage creep by applying a vibrational load to the lamination direction of a fuel cell (10). A vibrational load is applied in the perpendicular direction with respect to the surface of the fuel cell.    USE - Method for manufacturing fuel cell stack.    ADVANTAGE - since the aging treatment process is performed by a comparatively low load, the membrane electrode assembly with which a fuel cell equipped by a load and damage of gas diffusion layer can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for aging method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the method for manufacturing fuel cell stack. (Drawing includes non-English language text)    Fuel cell (10)    Cell laminated housing (20)    Step for laminating several fuel stacks (S100)    Step for performing aging treatment process (S110)    Step for performing fastening (S120)
NOVELTY - The manufacturing method involves forming catalyst substance embedded with polymer electrolyte. The carbon particle embedded with polymer electrolyte is formed. The catalyst ink is produced. The catalyst ink is coated and the electrode catalyst layer is formed on base material selected from gas diffusion layer, transfer sheet and polymer electrolyte membrane.    USE - Manufacturing method of fuel cell electrode catalyst layer of fuel cell membrane electrode assembly of polymer electrolyte fuel cell (all claimed).    ADVANTAGE - The reaction-active point is increased by improving the proton conductivity on the surface of the catalyst. The output performance of the polymer electrolyte fuel cell can be improved. The optimization examination of the amount of embedding can be performed easily. Since the dormant faculty of the catalyst substance can be withdrawn, the industrial utility value is increased.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell electrode catalyst layer;    (2) fuel cell membrane electrode assembly; and    (3) polymer electrolyte fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the membrane electrode assembly. (Drawing includes non-English language text)    Polymer electrolyte membrane (1)    Electrode catalyst layer of air electrode side (2)    Electrode catalyst layer of fuel electrode side (3)    Gas diffusion layer of air electrode side (4)    Membrane electrode assembly (11)
NOVELTY - The system (1) has fuel cell (8) to produce electric power by making fuel gas and oxidizing agent gas react electrochemically. A fuel gas generator (3) reforms source gas and generates fuel gas. A combustor (4) burns the gas and heats fuel gas generator. A detector (7) detects concentration of carbon monoxide in combustion exhaust gas discharged from combustor. A controller (12) adjusts electric power supplied to detector. The controller stops supply of electric power to carbon monoxide concentration detector in stop treatment process for fuel cell system to stop.    USE - Fuel cell system for domestic use.    ADVANTAGE - The stop treatment process to stop the fuel cell system can prolong the lifetime of the carbon monoxide concentration detector by stopping the electric power supply to the detector. Thus the need for periodic exchange of carbon monoxide concentration detector can be eliminated. The usability of the apparatus can be improved. The power consumption of a fuel cell system can be reduced and the energy utilization efficiency can be improved. The combustion stability of a combustor can be monitored stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system.(Drawing includes non-English language text)    Fuel cell system (1)    Fuel gas generator (3)    Combustor (4)    Carbon monoxide concentration detector (7)    Fuel cell (8)    Controller (12)
NOVELTY - The device has a gasification furnace whose top or bottom portion is provided with an opening having gasification air inlet pipe. The outlet is provided with air guide pipe which is connected with a temperature filter dust remover. The filter dust remover is connected in series with tar collector through air pipe. Each tar collector is provided with cooler and coke collecting pool. The bottom of the coke tank is provided with coke discharging pipe.    USE - Biomass gasification device.    ADVANTAGE - The structure of the biomass gasification device can be simplified. The biomass gasification device is environment friendly. The user convenience can be improved.
NOVELTY - The device has microwave carbonization furnace that is connected with storing cavity through collecting pipe. The outlet of cabin is connected with high temperature gasification furnace through tube. The pipeline is provided with high temperature gasification furnace which is connected with pneumatic conveyer. The high temperature gasification furnace is connected to discharging case and lower portion of temperature gasification furnace is connected with sensible heat recovery device.    USE - Biomass gasification device.    ADVANTAGE - The biomass property of the biomass gasification device can be improved. The structure of the biomass gasification device can be simplified. The efficiency of the biomass gasification device can be improved.
NOVELTY - Device comprises biogas fermentation tank, heating coil, solar energy collector, and hot water tank. The solar energy collector is connected through hot water tank with heating coil. The fermentation tank is connected with water inlet of heating coil. The heating coil is connected with solar energy collector. The device further comprises biogas boiler. The biogas boiler is connected with inlet pipe and water outlet pipe with hot water tank.    USE - The device is useful in production of biogas.    ADVANTAGE - The device produces biogas with stability.
NOVELTY - The disposal plant has swimming bed reactor and up-flow reactor. The swimming bed reactor is connected with exposure pump (3). The water outlet of swimming bed reactor is connected with flow tank. The water distributor (9) is installed with circular baffle (11) such that reaction layer is divided into upper reaction chamber and lower reaction chamber. A triphase separator (10) is equipped between water distributor and circular baffle for separating water, gas and granule sludge. The lower reaction chamber is formed of polyvinyl sponge padding in vertical arrangement.    USE - Integrated waste disposal plant.    ADVANTAGE - The anaerobic ammonium oxidation and denitrifying process can be performed efficiently with reduced installation space and improved denitrification efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of integrated waste disposal plant. (Drawing includes non-English language text)    Exposure pump (3)    Water distributor (9)    Triphase separator (10)    Circular baffle (11)    Outlet (20)
NOVELTY - Use of Aglaonema commutatum, is claimed for purifying livestock breeding biogas slurry, where the A.commutatum is planted in the livestock breeding biogas slurry polluted environment.    USE - The A.commutatum is useful for purifying livestock breeding biogas slurry, treating wastewater, and protecting environment and landscape construction.    ADVANTAGE - The A.commutatum is perennial, absorbs pollutant substances e.g. ammonium, total nitrogen and total phosphorus from the livestock breeding biogas slurry, has strong tenacious vitality and excellent practical applicability, can be directly planted cost-effectively and simply, requires no special management, permanently solves pollution problem of the livestock breeding biogas slurry, provides excellent economic benefit, and restores environment.
NOVELTY - Sludge treatment method for preparing oil by liquefying sludge, involves subjecting the sludge to liquefaction reaction in a subcritical or supercritical state of water.    USE - Sludge treatment method for preparing oil by liquefying sludge.
NOVELTY - Mixed sludge is prepared by mixing concentrated sludge and dewatered sludge. The mixed sludge is subjected to hydrolysis-acidification and microwave-treatment reflux, and methane generated by methanogenesis during hydrolysis-acidification is discharged and collected.    USE - Two-phase reflux microwave reinforced anaerobic digestion of sludge.    ADVANTAGE - The method provides high and stable processing efficiency, and can be applied in both medium and small sewage treatment plants.
NOVELTY - Method for treating biochemical sludge or animal dung using earthworm involves (a) collecting biochemical sludge and animal dung and adding brown sugar, Effective microorganisms (RTM: Lactic acid bacteria, yeasts, actinomycetes, photosynthetic bacteria and fungi) and urea, (b) adding the mixture in bags, arranging the bags on the ground, (c) placing earthworm germchits in each bag, (d) maintaining the temperature and humidity in the earthworm bags and (e) separating the treated dung from the earthworm.    USE - The method is useful for treating biochemical sludge and animal dung for cultivating lawn, turf, seedlings or landscape (all claimed).    ADVANTAGE - The method produces treated animal dung and biochemical sludge, which is suitable as organic manure having excellent quality.    DETAILED DESCRIPTION - Method for treating biochemical sludge or animal dung using earthworm involves (a) collecting biochemical sludge and animal dung and adding brown sugar (100-300 g), Effective microorganisms (RTM: Lactic acid bacteria, yeasts, actinomycetes, photosynthetic bacteria and fungi) (500-1500 g) and urea (50-150 g), (b) adding the mixture in bags, arranging the bags on the ground such that 400-500 bags are placed in each unit of area, (c) placing earthworm germchits (7000-10000) in each bag, (d) maintaining the temperature and humidity in the earthworm bags at 15-30 degrees C and 62-79%, and (e) separating the treated dung from the earthworm after 30-60 days, where each bag comprises 0.6-1 ton of biochemical sludge and animal dung. The earthworm germchit comprises artificial rearing earthworm and wild earthworm, where the volume of wild earthworm is 8-12% with respect to total volume of earthworm.
NOVELTY - A domestic sewage treatment device comprises crusher, water inlet pump, saturator, chemical agent box, chemical agent pump, flotation cabinet, scrum cabinet, sludge pump, sludge cabinet, discharge pump, sterilizing device, and electric control cabinet. The crusher is connected to a storage cabinet storing the sewage, and is connected to the saturator through the water inlet pump. The flotation cabinet is connected to the scum cabinet.    USE - Domestic sewage treatment device using flotation method.    ADVANTAGE - The device has compact volume, high efficiency and stable performance.
NOVELTY - Fermentation device comprises main body composed of soft garage type fermentation system and percolate circulation refluxing system.    USE - As fermentation device.    ADVANTAGE - The fermentation device has convenient feeding and discharging, and no post-treatment of waste liquor, and is simple, rapid, reliable and easy for large scale production, and produces high gas.    DETAILED DESCRIPTION - Fermentation device comprises main body composed of soft garage type fermentation system and percolate circulation refluxing system, where the soft garage type fermentation system comprises garage type fermentation chamber, soft sealing membranes, biogas outlet, percolate spray header and percolate collecting groove, the soft sealing membranes are mounted on the side surface and top opening of the garage type fermentation chamber, the soft sealing membranes and the wall of the garage type fermentation chamber are sealed by air expansion soft tube-C type groove, the biogas outlet is arranged on the top of the soft sealing membranes, the percolate spray header is arranged on the top of the percolate spray header, the percolate collecting groove is arranged on the bottom of the garage type fermentation chamber, the percolate circulation refluxing system comprises a percolate collecting tank and a water pump, the percolate collecting tank is provided with liquid extraction port, liquid inlet, and inoculation port, the liquid inlet is arranged on the bottom of the percolate collecting tank, the liquid extraction port and the inoculation port are arranged on the lower part of the percolate collecting tank, the water pump is mounted between the liquid extraction port and the spray header, the percolate spray header is connected to the water pump of the percolate refluxing device through a pipeline, and the percolate collecting groove is connected to the liquid inlet.
NOVELTY - Fuel rods are prepared by drying mechanically dewatered papermaking sludge to moisture content of 20-25% and controlling granularity to less than 20 mm; removing moisture from screened waste materials by sun drying and extruding, coarsely grinding the waste materials to granularity of 50-60 mm, and then finely grinding to granularity of 15-25 mm; and mixing the dried papermaking sludge and waste materials at weight ratio of 35-40%:60-65%, and extruding and forming the mixture to prepare fuel rods.    USE - Method of preparing fuel rods (claimed).    ADVANTAGE - The method has low cost, effectively recycles waste resource while protecting the environment, and is convenient in operation and suitable for mass industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for preparing fuel rods, comprising a drying chamber (1) and a crushing chamber (19). Walls around the drying chamber are made from tempered transparent glass. The drying chamber is provided with a sludge recovery equipment (6), a geothermal coiled pipe connected with a ground source heat pump and a hot air nozzle which is connected with a heat exchanger (17). The crushing chamber is provided with mutually connected coarse crushing machine (11) and fine crushing machine (12). Material outlets of the drying chamber and the crushing chamber are respectively communicated with a mixer (13). The mixer is communicated with a punching machine via auger delivery equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for preparing fuel rods.    Drying chamber (1)    Sludge recovery equipment (6)    Coarse crushing machine (11)    Fine crushing machine (12)    Mixer (13)    Heat exchanger (17)    Crushing chamber (19)
NOVELTY - Production of hydrocarbons from biomass involves: providing a biological feedstock containing free fatty acids and/or fatty acid esters; and subjecting the biological feedstock to heat in the presence of hydrogen with a catalyst slurry having an equivalent particle diameter of 10-400 microns to produce hydrocarbons which are predominantly even carbon number paraffins.    USE - For production of hydrocarbons, which are predominantly even carbon number paraffins (selected from n-octadecane, n-hexadecane or n-docosane) from biomass (claimed) as phase change material (PCM).    ADVANTAGE - The method produces converts biological feedstocks into even carbon number paraffin (at least 75, preferably at least 80 wt.%). The paraffin composition has superior properties as phase PCM material. The shorter diffusion path length, more accessible pores, and lower intra-catalyst temperature gradients in the smaller catalyst system reduce thermal decarboxylation and consequent co-production of odd number paraffins.
NOVELTY - Fuel composition for boiler station includes petroleum tailing - residual oil, oil sludge and wastes of solid fossil fuels semi-coking production - pyroligneous liquor at component ratio, wt: oil sludge 30-70, pyroligneous liquor 0.5-5.0, residual oil is the rest. Note that oil sludge from oil and oil product reservoirs containing 10-20% of water is used as oil sludge.    USE - Oil and gas production.    ADVANTAGE - Production wastes use, reduction of energy consumption, obtained fuel composition has low viscosity, high stability, low corrosion activity. 1 cl, 1 tbl, 4 ex
NOVELTY - Method for obtaining fuel composition for boiler plant consists in preliminary cleaning of oil sludge from oil and oil product reservoirs that contains 10-20% wt of water due to water excess and mechanical impurities at 70-80 degrees C. Mixing of cleaned oil sludge in quantity 30-70% wt, with residual oil M-100 and wastes of solid fossil fuels semi-coking production - pyroligneous liquor in quantity 0.5-5.0% wt. Water steam is supplied through the obtained mixture at temperature 90-95 degrees C. The mixture emulsification is carried out for 20-30 minutes.    USE - Oil and gas production.    ADVANTAGE - Method allows using wastes, reducing energy consumption and obtaining fuel of low viscosity, high stability and resistance to corrosion. 1 cl, 1 tbl, 4 ex
NOVELTY - In purifying poultry and livestock culturing biogas slurry, where the loquat is planted in the polluted environment of poultry and livestock culturing biogas slurry, loquat is used.    USE - In purifying poultry and livestock culturing biogas slurry (claimed).    ADVANTAGE - The loquat has the little investment, low operation cost, good effect, easy operation, and good purifying effect in winter. The harvested loquat can treat the disease such as cough and asthma, vomiting, polydipsia, and chronic cough. Using the loquat to treat wastewater as well as combining the environment protection and the landscape construction reflects the sustainable development idea of covering the wastewater treatment, ecological restoration, landscape construction, and economic benefit; the loquat can change the operation mode of the traditional ecological engineering perennially depending on the fund from the government.
NOVELTY - The apparatus (1) has a methane fermentation tank (11) that generates biogas by using organic waste. A pressure detection unit (13) detects pressure of biogas. A gas storage unit (15) stores biogas emitted from the methane fermentation tank. Several gas-engine generators (61-63) burn biogas and air supplied from the gas storage apparatus to drive generators (51-53). A control unit (18) inputs detected pressure value of biogas to control start and stop operation of gas-engine generator.    USE - Biogas apparatus.    ADVANTAGE - The start and stop operation of gas-engine generator can be controlled effectively, since control unit is provided to input detected pressure value of biogas to control start and stop operation of gas-engine generator. The gas-engine generator can be operated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas apparatus. (Drawing includes non-English language text)    Biogas apparatus (1)    Methane fermentation tank (11)    Pressure detection unit (13)    Gas storage unit (15)    Control unit (18)    Generator (51-53)    Gas-engine generator (61-63)
NOVELTY - Method for preparing biodiesel, involves reacting feedstock oil, short-chain alcohol, water, and liquid lipase in single-stage or multi-stage enzymatic reactor, separating the reaction fluid into an enzyme-containing heavy phase and light phase, recycling and reusing enzyme within the heavy phase using light phase in subsequent immobilized enzyme conversion, adding the light phase and the short-chain alcohol into the enzymatic reactor containing immobilized lipase, and performing online dehydration during entire reaction process or stage of reaction process.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The method produces feedstock oil-to-biodiesel conversion rate greater than 90% in early stage and biodiesel yield of greater than 98% in later stage, and product acid value of less than 0.5 mg potassium hydroxide/g oil.    DETAILED DESCRIPTION - Method for preparing biodiesel, involves reacting feedstock oil, short-chain alcohol, water, and liquid lipase in single-stage or multi-stage enzymatic reactor, separating the reaction fluid into an enzyme-containing heavy phase and light phase, recycling and reusing enzyme within the heavy phase using light phase in subsequent immobilized enzyme conversion, adding light phase and the short-chain alcohol into the single-stage or multi-stage enzymatic reactor containing the immobilized lipase, and performing online dehydration by barrier separation or molecular sieving during entire reaction process or stage of reaction process.
NOVELTY - Method for preparing biodiesel using feedstock oil, involves adding suitable quantity of the feedstock oil and lipase into single-stage or multi-stage enzymatic reactor, and aqueous ethanol into the system during reaction process.    USE - The method is useful for preparing biodiesel using feedstock oil.    ADVANTAGE - The method directly uses the ethanol crude product to prepare the biodiesel, and thus reducing the raw material costs in the biodiesel preparation process, and allows feedstock oil-to-biodiesel conversion rate of greater than 90%.
NOVELTY - Special fertilizer, comprises (in wt.%): chicken manure (60-70), bacterial fermented liquid (0.1-0.4), urea and potassium sulfate (1-5, each), calcium-magnesium-phosphate fertilizer (20-30), and borax and zinc sulfate (0.5-1, each).    USE - The special fertilizer is useful for nanmu tree.    ADVANTAGE - The fertilizer increases height of nanmu tree to 10% or more and diameter of the tree to 12% or more compared to existing compound fertilizers.
NOVELTY - Method for manufacturing fuel gas, involves removing aquatic biomass and sludge from lake by dredging the lake, mixing and grinding the obtained materials to form a slurry, adding water and catalyst to the slurry, mixing the mixture uniformly, adding the mixture into a supercritical reaction device, reacting obtained mixture by performing gasification process in the device to obtain supercritical liquid, reacting obtained liquid, cooling the liquid and separating the fuel gas.    USE - The method is useful for manufacturing fuel gas.    ADVANTAGE - The method is economical as it utilizes lake waste as raw material and less amount of catalyst, and does not cause secondary pollution during supercritical reaction.    DETAILED DESCRIPTION - Method for manufacturing fuel gas using lake waste, involves removing the aquatic biomass and sludge from lake by dredging the lake, mixing and grinding obtained materials to form a slurry, where the concentration of mud is 20-70 wt.%, adding water and catalyst to the slurry, mixing the mixture uniformly, adding the mixture into a supercritical reaction device, where the ratio of water added and the sludge and biomass in the reactant mixture is 5-50:1, reacting obtained mixture by performing gasification process in the supercritical reaction device under pressure of 16-22 MPa at 120-3740 degrees C for 5-10 minutes to obtain supercritical liquid, reacting the obtained liquid under 22.1-45 MPa at 374-700 degrees C for 10-30 minutes, cooling the liquid and separating the fuel gas.
NOVELTY - Composite fuel comprises (in wt.%): sludge from sewage treatment plant (30-40), crop straw (40-50), coal powder (10-30) and coalification agent (4-8).    USE - As composite fuel.    ADVANTAGE - The fuel can be used as organic fertilizer with rapid effect, is environmentally-friendly and nontoxic, causes no chemical hazards, consumes less energy, has an adjustable thermal value, increased calorific value of 5000-6000 J, releases degradable ash after combustion, and is suitable for industrial and civil applications.
NOVELTY - Biodiesel production device with parabolic trough type condenser comprises a storage tank, a valve, a pipeline reactor, a receiver, a condenser, a support and a reservoir tank. The lower part of the storage tank is connected to a pipeline reactor. The bottom of the storage tank is higher than the pipeline reactor outlet. The valve is located between the storage tank and the pipeline reactor. The pipeline reactor is connected to a support via the receiver of the trough type condenser, and the other end is connected to the receiver. The pipeline reactor outlet is provided with a reservoir tank.    USE - Used as a parabolic trough type condenser biodiesel production device.    ADVANTAGE - The device is simple, compact and economical; and consumes inexhaustible and renewable solar energy instead of high-grade electrical energy, and hence reduces the production cost of biodiesel.
NOVELTY - Preparation of clean diesel oil comprises providing (pts.wt. based on 1000 kg clean diesel oil) catalytically modified coal tar, wood tar, or bamboo tar (40-50), jet fuel or kerosene (30-40), diesel oil (10-40), and isooctyl nitrate (0.1-0.3); adding catalytically modified coal tar, wood tar, or bamboo tar into a reactor; adding jet fuel or kerosene; adding isooctyl nitrate as catalyst; reacting at 60 degrees C for 4-8 minutes and 2 atm; adding diesel oil; and stirring for 5-6 minutes.    USE - Preparation of clean diesel oil (claimed).
NOVELTY - Sewage treatment system in plant pharmaceutical factories comprises a first sedimentation tank, a second sedimentation tank, an aerobic tank, a clarifying tank, a fan and a water pump, where the aerobic tank is present between the first sedimentation tank and the second sedimentation tank. The first sedimentation tank is sequentially connected to the aerobic tank through the pipeline, and the second sedimentation tank and the clarifying tank are connected in series.    USE - Used as a sewage treatment system in plant pharmaceutical factories.    ADVANTAGE - The device: achieves sewage chemical oxygen demand (COD) and biochemical oxygen demand (BOD) removal rate of 80-90%; has high purifying efficiency; saves space and investment; is convenient to operate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the sewage treatment system in plant pharmaceutical factories.
NOVELTY - A high density environmental mechanism of charcoal is produced by using Eupatorium adenophorum, adding sawdust and original binder without peculiar smell, and using pulverizer machine for making rod and cutting machine.    USE - Method for production of high density environmental mechanism of charcoal (claimed).    ADVANTAGE - The method is easy and simple to handle with low cost. The high density mechanism of charcoal produced without dust and peculiar smell is non-toxic and harmless to human body. The method changes Eupatorium adenophorum into wealth, and has value in use and produces economic benefits.    DETAILED DESCRIPTION - Production of high density environmental mechanism of charcoal involves removing or cutting Eupatorium adenophorum artificially and dehydrating to medium dry or dried-up; building pool of carbonization; feeding material; lighting and controlling the fire; sifting Eupatorium adenophorum without carbonizing; crushing Eupatorium adenophorum carbonized into charcoal powder with pulverizer, filtering, and stirring with adding binder; and getting charcoal rod with using machine of making rod, cutting, drying with putting in pallet, and getting the high density environmental mechanism of charcoal. The binder is original type without peculiar smell, and is prepared by 3-5% lime, 8-10% clay, and 3-5% grapevine immersion liquid.
NOVELTY - Carbonylation synthesis of sorafenib involves reacting 4-(4-aminophenoxy)-pyridino-2-carbolyic acid formamide with carbon dioxide to obtain carbamic acid in presence of alkali metal carbonate catalyst and alkali solvent such as N-methylpyrrolidone to obtain carbamic acid, and then reacting carbamic acid with 4-chloro-3-trifluoromethylaniline in alkali solution to obtain substituted urea product, which is the sorafenib. The reaction is carried out at 5-30 atm and 50-200 degrees C for 2-50 minutes.    USE - Method for carbonylation synthesis of sorafenib (claimed).    ADVANTAGE - The method has simple operation, utilizes easy to obtain raw materials, is safe and environmentally friendly, and obtains product having stable quality.    DETAILED DESCRIPTION - Carbonylation synthesis of sorafenib comprises reacting 4-(4-aminophenoxy)-pyridino-2-carbolyic acid formamide with carbon dioxide to obtain carbamic acid in presence of alkali metal carbonate catalyst and alkali solvent such as N-methylpyrrolidone to obtain carbamic acid, and then reacting carbamic acid with 4-chloro-3-trifluoromethylaniline in alkali solution to obtain substituted urea product, which is the sorafenib. Mole ratio of 4-(4-aminophenoxy)-pyridino-2-carbolyic acid formamide to 4-chloro-3-trifluoromethylaniline is 1:5-5:1. Mole ratio of alkali metal carbonate to the main reactant is 1:3-3:1. The reaction is carried out at 5-30 atm and 50-200 degrees C for 2-50 minutes.
NOVELTY - The apparatus has a waste collecting unit (10) for collecting food waste through the inlet port (11a). A food waste treatment unit (20) is provided for fermenting and dissolving food waste collected by waste collection unit so as to dehydrate moisture with the air cooler such that the food waste is processed in the analysis completion tub to eject the powder used as material of environment-friendly fertilizer and fuel.    USE - Collection and disposal apparatus of food waste materials.    ADVANTAGE - The food waste can be easily collected and processed so that the generation of bad smell can be avoided. The solid fuel for combustion or environment-friendly fertilizer can be manufactured efficiently with simple structure and reduced maintenance cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of collection and disposal apparatus.    Waste collecting unit (10)    Inlet port (11a)    Lower connection pipe (15)    Cylinder pipe (16)    Food waste treatment unit (20)
NOVELTY - This utility model is provided a hiogas reactor, which comprises a shel11-like body (1) with internal hollow chamber, a feed pipe (2) passing through the body (1) extending to a lower portion of the chamber; a hiogas discharging pipe (4) passing through the body (1) and extending to a upper portion of the chamber; a reactor effluent pipe (3) passing through the body (1) from the top portion of the body (1) extending to the middle portion of the hollow chamber; the part of the reactor effluent pipe (3) below the top of the body (1) the hollow chamber forming a varying section tube (301) in the vertical direction. With the varying section tube (301) provided on the reactor effluent pipe (3), when the level of the hiogas slurry in the chamber is coming up or down, the surface area of the hiogas slurry in the tube is changed such that the slag shell can not be formed easily, and the biogas reactor can be producing biogas continuously.
NOVELTY - A hydrogen methane fermentation apparatus comprises biomass supply unit (2) which connects with fermenter (1) of single tank and supplies biomass in fermenter, biogas collection unit (3) which collects biogas connected with and emitted in fermenter out of fermenter, fermentation residue collection unit (4) which collects fermentation residues that are generated in fermenter, stirring unit which stirs inside perforated diaphragm which isolates the inside of fermenter in upper part and the lower part, and transfer unit (15) which transfers fermented liquor in upper part into the lower part.    USE - A hydrogen methane fermentation apparatus.    ADVANTAGE - The apparatus efficiently collects biogas from biomass. Environmental pollution is prevented. Energy can be reproduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen methane fermentation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen methane fermentation apparatus.    Fermenter (1)    Biomass supply unit (2)    Biogas collection unit (3)    Fermentation residue collection unit (4)    Transfer unit (15)
NOVELTY - The processing device has carbonizing furnace, stirring tank, separating device, drying furnace and grinding unit. The carbonizing furnace having alkaline solution is provided with stirring tank. The outlet of the carbonizing furnace is attached with liquid outlet of the carbonizing rice hull outlet. The separating device is connected with the outlet of the drying furnace which is connected with the silicon dioxide grinding machine.    USE - Continuous rice husk processing device.    ADVANTAGE - The rice hull can be continuously processed with improved energy-saving effect in environment-friendly manner.
NOVELTY - Producing methane gas from solid biomass material, comprises: preparing a feedstock slurry containing microbially fermentable components by combining biomass (comprising matter derived from a plant belonging to genus Pennisetum) with an aqueous phase and optionally, subjecting biomass to pre-treatment resulting in reduced resistance to enzymatic degradation; and incubating feedstock slurry at 46-60 degrees C or 20-40 degrees C and under oxygen depleted atmosphere, in presence of methane-producing thermophilic or mesophilic microorganisms and collecting methane gas released from feedstock slurry.    USE - The process is useful for producing biogas, methane and syngas from solid biomass.    ADVANTAGE - The process: provides methane production/yield exceeding 275 m3 per kg of dry biomass material; and utilizes material derived from plant belonging to the genus Pennisetum as a feedstock, which provides high overall efficiency (economical factors including agricultural yield of the biomass, quality of the biomass, retention time of the substrate in the digestion process, methane yield per unit biomass or syngas yield per unit biomass, methane content per unit volume of biogas and other factors that affect the overall cost of methane or syngas production) of energy recovery, both in digestive biogas/methane processes and in gasification processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing syngas from solid biomass material, comprising providing biomass, preparing a gasification feedstock by dehydrating the biomass to a dry matter content greater than 85% and subjecting the biomass to a treatment yielding a particulate material and subsequently subjecting the gasification feedstock to a gasification process comprising reacting it with oxygen and/or steam at temperature exceeding 700 degrees C, where the biomass is derived from a plant belonging to genus Pennisetum.
NOVELTY - Reducing nitrogen and phosphorus contents of spill water of wastewater sludges and producing increased quantity of biogas: comprises setting toxic material content of spill water by a measuring and controlling unit, and producing algae using spill water containing the nutritive materials by photosynthesis; processing the aqueous mixture of algae depending on the composition of the spill water; producing spill water with high water content and biomass with high dry material content; and leading the biomass into biogas producing unit to produce biogas, or as fuel to produce heat.    USE - The process is useful for: reducing nitrogen and phosphorus content of spill water of wastewater sludges; and producing increased quantity of biogas.    ADVANTAGE - The process provides the biogas at high yields.    DETAILED DESCRIPTION - Reducing nitrogen and phosphorus contents of spill water of wastewater sludges and producing increased quantity of biogas: comprises setting toxic material content of spill water by a measuring and controlling unit, based either on continuous measurement or on sampling, in such a way that the resulting spill water containing the nutritive materials is used for producing a large quantity of algae by providing all the other requirements of photosynthesis; processing the aqueous mixture of algae depending on the composition of the spill water; producing spill water with high water content and biomass with high dry material content; and leading the biomass into biogas producing unit to produce biogas, or as fuel to produce heat. An INDEPENDENT CLAIM is also included for the apparatus, comprising the carbon dioxide producing heating unit, at least one algae producing photobioreactor, lighting unit, air conditioning unit and dewatering unit, sludge compacting unit, technological preparing unit, measuring and controlling unit, and biogas producing unit.
NOVELTY - Fermenting system comprises feeding system, dry type anaerobic fermenting tank of stirring system, heating heat preserving heat preserving system, biogas slag treatment system, exhaust gas and control system.    USE - As fermenting system capable treating organic waste.    ADVANTAGE - The fermenting system require low energy and is cost-effective.    DETAILED DESCRIPTION - Fermenting system comprises feeding system, dry type anaerobic fermenting tank of stirring system, heating heat preserving heat preserving system, biogas slag treatment system, exhaust gas and control system, where the feeding system comprises storage box and conveyor, half-wet crusher and pre-treating tank arranged sequentially, the biogas slag treatment system comprises sludge dehydration device and sewage processor connected with each other by a pipeline, the pretreating tank of the feeding system is connected with the feeding port of the dry-type anaerobic fermenting tank by a pipeline, the dry-type anaerobic fermenting tank is connected with heating heat-preserving system by a circulation line, the dry-type anaerobic fermenting tank is respectively connected with sludge dehydration device and the sewage processor by pipeline.
NOVELTY - Preparing an improved spray-dried fluid catalyst by the removal of greater than 50% of particles above a threshold value, where such removal results in a fraction with improved accessibility or diffusion, or by the removal of greater than 50% of particles below a minimum threshold and greater than 50% of particles above a maximum threshold, to create a catalyst with improved diffusion constraint and in which most particles that are insufficiently retained by commercial cyclones have been removed, is claimed.    USE - The process is useful for preparing spray-dried catalyst precursors, which are useful for making in-situ hydrocarbon conversion catalysts (claimed).    ADVANTAGE - The process provides high yield and/or selectivity of chemical reactions to enhance the value of hydrocarbons.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an improved catalyst composition created by spray drying a mixture of components and removing greater than 50% of the particles below a minimum threshold and greater than 50% of particles above a maximum threshold; and    (2) a hydrocarbon conversion process, an improved fluid catalytic cracking process, improved biomass conversion process and improved naphtha cracking process, using the improved catalyst compositions.
NOVELTY - Organic fertilizer obtained through sustainable recycling from the residue resulting from oil-palm bunch milling, is claimed, where the production comprises pre-composting, vermicomposting, sieving and catalysis of the chelating ions in the vermicompost.    USE - Used as organic fertilizer. No biological data given.    ADVANTAGE - The organic fertilizer has a better assimilation by plants and does not pollute groundwater, and does not destroy the soil structure.
NOVELTY - The process comprises resolving and reducing fallen leaves and afforesting garbage composed by wood cellulose, grass cellulose and skeleton, breaking chain of the wood cellulose and grass cellulose in the fallen leaves and afforesting garbage, reducing and reclaiming the fallen leaves and afforesting garbage, and treating the fallen leaves and afforesting garbage using solar energy without any additional motive power, where the zymolysis of the fallen leaves and afforesting garbage is realized under the effect of sunshine and microorganism.    USE - The process is useful for treating fallen leaves and afforesting garbage to obtain fertilizer.    DETAILED DESCRIPTION - The process comprises resolving and reducing fallen leaves and afforesting garbage composed by wood cellulose, grass cellulose and skeleton, breaking chain of the wood cellulose and grass cellulose in the fallen leaves and afforesting garbage, reducing and reclaiming the fallen leaves and afforesting garbage, treating the fallen leaves and afforesting garbage using solar energy without any additional motive power, where the zymolysis of the fallen leaves and afforesting garbage is realized under the effect of sunshine and microorganism, the temperature in the reaction tank is more than 10 degrees C and the harmless degradation of fallen leaves is realized, avoiding transportation by reducing the fallen leaves and afforesting garbage to prepare organic matter fertilizer, heating the fallen leaves and afforesting garbage, where the microorganism is restrain the growth of malignant bacteria and decomposing ovum into the fallen leaves and afforesting garbage to suppress the harmful bacteria through microbial fermentation reaction process and packaging the product as fertilizer.
NOVELTY - Carbon dioxide is selective-electrochemically-converted into 2C hydrocarbon at room temperature and atmospheric pressure in a two-phase liquid/solid system comprising electrochemical cell having an anode and a cathode. The cathode is modified by copper electrodeposits having monolayer porous structure/morphology with craters or multilayer three-dimensional pore structure with different porous sizes.    USE - Selective electrochemical conversion of carbon dioxide into 2C hydrocarbon e.g. ethane and ethylene (claimed).    ADVANTAGE - The method enables efficient and stable selective-electrochemical conversion of carbon dioxide into 2C hydrocarbon.
NOVELTY - A hydrogen-producing catalyst contains nickel-silicon group intermetallic compound.    USE - Catalyst is used for producing hydrogen (claimed) for fuel cell.    ADVANTAGE - The catalyst has excellent thermal load responsiveness and high activity in short time with respect to decomposition of methanol and steam reforming reaction of hydrocarbon.    DETAILED DESCRIPTION - A hydrogen-producing catalyst contains nickel-silicon (Ni3Si) group intermetallic compound. INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen from methanol or hydrocarbon using hydrogen production apparatus;    (2) hydrogen production apparatus, which consists of heating portion for heating the catalyst, and supply portion for supplying methanol or hydrocarbon to the catalyst; and    (3) method for activating hydrogen-producing catalyst, which involves contacting intermetallic compound in catalyst and gaseous methanol, and performing decomposition of methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of catalyst structure.    Disk-shaped components (15a,15b)    Boards (16,17)    Laminate (20)
NOVELTY - An alcohol production method involves producing alcohol from carbon source using basidiomycete of Neolentinus genus.    USE - Alcohol production method for production of alcoholic beverage (claimed).    ADVANTAGE - Alcohol production is efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production method of alcoholic beverage which involves producing liquid which contains alcohol from a carbon source using the basidiomycete of Neolentinus; and    (2) alcohol production material comprising carrier which supports hypha for producing alcohol from a carbon source, where hypha is from basidiomycete of Neolentinus genus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram which demonstrates the recycling method of unused biomass resources using Neolentinus genus basidiomycete. (Drawing includes non-English language text).
NOVELTY - Method for manufacturing biodiesel fuel, involves introducing microorganisms having lipase activity and glycerol assimilation ability into reaction system and producing biodiesel fuel from fats, oils and alcohol by the enzymatic action of the above-mentioned microorganisms.    USE - The method is useful for manufacturing biodiesel fuel and feed or fertilizer (claimed). The biodiesel fuel is manufactured from fat and oil, particularly used and unused vegetable oil.    ADVANTAGE - The method is environmentally-friendly and reduces the amount of glycerol by-product. The microbial cells can be reused.
NOVELTY - The apparatus has a catalytic converter (20) i.e. bismuth oxide converter, comprising a cylindrical substrate element (22) with a honeycomb cell configuration to allow steam to pass through the converter, where the element is coated with an oxide. A separator (30) is arranged intermediate to the converter and a fuel cell (40), and channels hydrogen to an input (42) of the fuel cell and oxygen to an output (46) of the fuel cell, where the hydrogen and the oxygen are combined at the output to form water and heat for producing steam that is recycled to the converter.    USE - Apparatus for supplying hydrogen to a fuel cell e.g. polymer exchange membrane fuel cell, solid oxide fuel cell, and molten-carbonate fuel cell (all claimed), to produce electricity.    ADVANTAGE - The converter contains the substrate element coated with the oxide that is oxidizable with steam and reducible back to an original state without using a chemical agent, so as to produce electricity efficiently in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a supply system.    Catalytic converter (20)    Cylindrical substrate element (22)    Separator (30)    Fuel cell (40)    Input of fuel cell (42)    Output of fuel cell (46)
NOVELTY - Microbial inoculum comprises protein degrading bacterium, starch degrading bacterium, degrading bacterium, and cellulose degrading bacteria having a weight ratio of 1-2:1-2:1-2:2-3.    USE - The microbial inoculum is useful for degrading Chinese kitchen rubbish.    ADVANTAGE - The microbial inoculum can be prepared with less energy consumption in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the microbial inoculum comprising culturing the strain by performing centrifugation to obtain thallus and mixing obtained thallus according to proportion to obtain compound strain, mixing the bamboo carbon, wood, soil, zeolite and rice bran to obtain carrier material, and mixing obtained compound strain and carrier material.
NOVELTY - Gasifying furnace comprises three bin hydraulic hopper-type feeding port, valve plate, hydraulic cylinder and cylindrical guide rail.    USE - The gasifying furnace is useful for garbage pyrolysis.    ADVANTAGE - The furnace has excellent sealing property.
NOVELTY - Organic waste processing box comprises box unit, separating unit in middle portion of box unit, space layer at top of the separating unit, liquid passing hole having several separating plate, collecting tank for collecting waste liquid through the separating plate, groove at the bottom of the collection tank having inclined structure to drain liquid waste, opening valve in the separating unit for collecting waste, and compost fermentation storehouse comprising breeding box and culture box for performing biological degradation of the waste using earthworm.    USE - As organic waste processing box.    ADVANTAGE - The box is simple to operate, occupies less space and affordable for individual farmers.    DETAILED DESCRIPTION - Organic waste processing box comprises (a) box unit, where the box unit has cavity on the top, (b) separating unit existing in middle portion of box unit, (c) space layer at top of the separating unit, where upper portion of the separating unit is provided with inlet and outlet, (d) liquid passing hole having several separating plate, (e) collecting tank for collecting waste liquid through the separating plate, (f) groove at the bottom of the collection tank having inclined structure to drain liquid waste, (g) opening valve in the separating unit for collecting waste, and (h) compost fermentation storehouse comprising breeding box and culture box for performing biological degradation of the waste using earthworm and obtaining processed fertilizer.
NOVELTY - The furnace has a hearth (2) provided with an air annular channel (3) that is connected with an inlet pipe (4), where the hearth is provided with an air outlet channel (6) and a movable sealing cover (10). A furnace body (1) is provided with a brick-concrete structure. The hearth is arranged at an upper part of a water return pipe (8) that is connected with the air outlet channel. A rod (12) is inserted into the sealing cover. An upper part of the air outlet channel is connected with an inner wall of an anti-blocking bump (15). An inner wall of the hearth is provided with a refractory plate.    USE - Brick kiln-type biomass gas furnace for use in a mountainous area flue-cured tobacco manufacturing field.    ADVANTAGE - The furnace ensures better heating capacity and better quality. The furnace has prolonged service life, and is inexpensive. The furnace reduces processing time and saves biomass gas source.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a brick kiln-type biomass gas furnace.    Furnace body (1)    Hearth (2)    Air annular channel (3)    Inlet pipe (4)    Air outlet channel (6)    Water return pipe (8)    Movable sealing cover (10)    Rod (12)    Anti-blocking bump (15)
NOVELTY - The gasifier has a vertical central gasification chamber whose upper part is provided with a fuel gas outlet and lower part is provided with a gasification raw material inlet that is provided with a horizontal auger. A periphery gasification chamber is sleeved on center gasification chamber that is connected with a gasification room. A cone-shaped residual carbon return chamber is located at lower part of the periphery gasification chamber. An annular heating chamber is provided with a gasification chamber fuel inlet and an ignition port.    USE - Internal circulation and external thermal type gasifier for urban organic waste, agricultural and forestry waste and cracking- gasification gas.    ADVANTAGE - The device has high heat utilization rate, high heat transfer efficiency and high gasification efficiency.
NOVELTY - Utilizing bamboo branch tip leftover material, comprises (a) passing bamboo branch tip leftover material into a carbonizing furnace for heating and carbonizing, to obtain carbide and carbonized smoke, (b) outputting the carbide, and passing the carbonized smoke into a dust remover, to remove dust (c) conveying the dust removed smoke into a condenser, for cooling, to obtain a tar, wood acid and wood gas, (d) separating and collecting the tar and wood acid, (e) conveying the wood gas into a water scrubber, for washing, and (f) obtaining the pure wood gas for further use.    USE - The method is useful for utilizing bamboo branch tip leftover material.    ADVANTAGE - The method converts a waste into a useful material with a value of more than 2000 yuan per ton, to produce different products; increases the additional value of the leftover material by more than 4%; and ensures low emission of pollutants e.g. carbon and other pollutants to 0.01 tons.
NOVELTY - A multi-functional packaging material comprises (in wt.%) biocidal substance (0.05-25.0), hydrocarbon solvent (1.0-90), co-solvent (1.0-50.0), an organic stabilizer (0.05-1.0), oxidation inhibitors (0.5-60.0), corrosion inhibitors (0.5-10.0) and/or metal deactivator (0.03-5.0), where the biocidal substance comprises methylene-bis (thiocyanate) and/or 2-thiocyano-methyl sulfenyl-1,3-benzothiazole.    USE - Multi-functional packaging material for packing biofuels.
NOVELTY - The method involves pressing a particulate structure of jagged particles to 20 mm in a hydraulic particulate biomass briquetting press. The particulate structure of the jagged particles is dried to humidity of 12 to 20 percent of the biomass that is fed to the hydraulic briquetting press with a screw conveyor. The biomass is compressed under 500 to 1500 atmospheric pressure in side walls of a bale chamber with dimensions of 5 to 15 cm.    USE - Method for producing biomass briquettes.
NOVELTY - Preparing activated carbon livestock waste fuel comprises (wt.%) mixing livestock wastes (60-80), biomass powder (10-30), and activated carbon (1-30); dehydrating the mixed raw material; and prilling with the dehydrated raw material.    USE - Method for preparing activated carbon livestock waste fuel (claimed).    ADVANTAGE - The method can be easily operated.
NOVELTY - A biorenewable fuel preparation method involves performing transesterification process on triglycerides with alcohol in presence of an alkaline catalyst (0.5-2%, preferably 1%), adding fat or vegetable oil, stirring the mixture at 20-50 degrees C, preferably 40 degrees C for 1-5 minutes, preferably 2 minutes, and adding aliphatic alcohol to the mixture, and placing resultant product in microwave flow reactor at intensity of 0.07-0.7 kWh-1, at 50-65 degrees C for 1-10 minutes, preferably 3 minutes to obtain finished product, where molar ratio of alcohol to oil is 5:9.    USE - Method for preparing biorenewable fuel.
NOVELTY - Itraconazole is obtained by (a) dissolving polyvinyl alcohol and polyoxyethylene polyoxypropylene-polyoxyethylene triblock copolymer (10 mg/l, each) F108 in deionized water (6.4 ml), (b) uniformly mixing the solution, and heating the solution until the solution is clear to obtain copolymer gel, (c) dissolving lysozyme and itraconazole in phosphate buffer and adding the solution to the obtained copolymer gel, and (d) spinning the obtained product.    USE - The itraconazole is useful for preventing microbial contamination in internal chamber (claimed).    ADVANTAGE - The itraconazole is cost-effective and environmentally-friendly.
NOVELTY - A methane-carbon adsorbent is formed by layering, carbonizing and activating coal powder (100), coal tar (35-45), potassium hydroxide (3-8), potassium nitrate (2-6), calcium carbonate (3-8), magnesium chloride (2-6) and water (10-20), and has iodine value of 900-1000 mg/g and methylene blue value of 100-150 mg/g. The content of ash in the coal powder is less than 5 wt.% and the coal tar is high-temperature coal tar.    USE - Methane-carbon adsorbent is used for pressure swing adsorption process.    ADVANTAGE - The adsorbent has high strength of more than 95%, methane adsorption capacity of 25 mL/g (which is 2.0 mL/g less than carbon monoxide adsorption), high adsorption and desorption speed, and large pore volume.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of methane-carbon adsorbent. A precursor is formed by mixing coal powder with a particle size of more than 200 meshes, coal tar, potassium hydroxide, potassium nitrate, calcium carbonate, magnesium chloride and water, stripping by a stripping machine, leaving aside for 2-3 days and carbonizing. The obtained precursor is placed in a step furnace or multifunctional converter, activated at 850-950 degrees C in the presence of steam, soaked in 3-10% hydrochloric acid solution for 8-24 hours, washed until the pH is 7-9 and dried at 120 degrees C for 1 hour, to obtain carbon adsorbent.
NOVELTY - A purification system comprises biological desulfurization tank which is filled with filler which fixes microorganisms, feed pipe which disperses water containing microorganisms, drain pipe which is connected with bottom part of biological desulfurization tank and discharges water in biological desulfurization tank, air injection apparatus which injects air to inlet port of biological desulfurization tank, watering plate (41) which is provided above filler and has discharge hole (42), and pipe-shaped overflow body (45) which is provided in upper surface of each discharge hole.    USE - Purification system for removing impurities such as hydrogen sulfide in biogas.    ADVANTAGE - The purification system can disperse water containing microorganisms equally.    DETAILED DESCRIPTION - A purification system comprises biological desulfurization tank which is filled with filler which fixes microorganisms, feed pipe which disperses the water containing microorganisms and is connected with upper part of biological desulfurization tank, drain pipe which is connected with bottom part of biological desulfurization tank and discharges the water in biological desulfurization tank, air injection apparatus which injects air to inlet port of biological desulfurization tank, watering plate (41) which is provided above the filler and has discharge hole (42), and pipe-shaped overflow body (45) which is provided in the upper surface of each discharge hole.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional enlarged view of the overflow body and discharge hole.    Watering plate (41)    Discharge hole (42)    Overflow body (45)
NOVELTY - A fuel rod is prepared by drying papermaking sludge having granularity less than 20 mm after mechanical dehydration to moisture content of 20-25%; removing moisture from biomass to make moisture content to 8-12%, then performing crushing to obtain coarse particles of 30-40 mm, and performing fine crushing to obtain fine particles having granularity of 10-15 mm; and mixing dried paper sludge (50-55 wt.%) with biomass fine particles (45-50 wt.%), and extruding to make high density fuel rod.    USE - Method of preparing fuel rod (claimed).    ADVANTAGE - The method can achieve paper sludge drying at low cost and maximizes use of resource, which recycles waste resources effectively and protects the environment. Further, the method is simple and convenient in operation, and suitable for large-scale industrialized production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for preparing fuel rod, comprising a drying chamber (1) and crushing chamber (19). Surrounding walls of the drying chamber are made of toughened transparent glasses. The drying chamber is provided with a sludge recovery device (6), a terrestrial heat coiler connected with a ground source heat pump and a heat shower nozzle connected with a heat exchanger. The crushing chamber is provided with a coarse crusher (11) and a fine crusher (12) connected each other. Material outlets of the drying chamber and the crushing chamber are connected with an agitator which is separately connected with a puncher via a screw conveying device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing fuel rod.    Drying chamber (1)    Sludge recovery device (6)    Coarse crusher (11)    Fine crusher (12)    Crushing chamber (19)
NOVELTY - A biomass briquette fuel is prepared by preparing raw materials comprising crushed biomass particles, and composite adhesive comprising high-calcium fly ash (8-20 wt.%) and sawdust (balance); uniformly mixing the crushed biomass particles and the composite adhesive at 85-95 degrees C; and sending mixture into a molding machine to generate biomass briquette fuel particles, and cooling. The composite adhesive is present at 13-28 wt.%.    USE - Method of preparing biomass briquette fuel (claimed).    ADVANTAGE - The method is environmentally-friendly, and has low device cost and labor cost.
NOVELTY - Application of Rheum palmatum in processing livestock breeding biogas slurry comprises planting R. palmatum in the livestock breeding biogas slurry-polluted environment.    USE - Application of R. palmatum in processing livestock breeding biogas slurry.    ADVANTAGE - The application method fully uses absorbing effect of the R. palmatum to the pollutants such as ammonium nitrogen (NH4+-N), total nitrogen (TN), total protein (TP) and chemical oxygen demand determined by potassium dichromate method (CODcr) in the livestock breeding biogas slurry. The R. palmatum is tenacious in vitality, capable of being directly planted, unnecessary in special management and perennial. The livestock breeding biogas slurry pollution problem is permanently solved. The method has less investment, low operation cost, excellent effect, and is simple and capable of ensuring the purification effect of artificial wetlands in winter. The harvested R. palmatum can be further used medicinally for treating heat aggregation and chest obstruction, dampness-heat and diarrhea-dysentery, jaundice, gonorrhea, edema and flatulence, postpartum stasis and abdominal pain, abdominal mass and accumulation, and traumatic injury. The method combines environmental protection with economic construction, and has potential to change the operation mode that the traditional ecological engineering depends on funds invested by the government for long term.
NOVELTY - The method involves providing blank work piece having slotted region. The corresponding slots of slotted region are arranged in form of rows, and are separated from each other by using struts and ribs. The blank work piece is stamped with die along corresponding directions, to create voids and lands in struts and ribs.    USE - Method for manufacturing electrode of fuel cell e.g. solid oxide fuel cell (SOFC) and polymer exchange membrane fuel cell (PEMFC).    ADVANTAGE - The electrode of the fuel cell is easily manufactured at low cost, by using the method for manufacturing the electrode of the fuel cell. The efficiency of the electrode of the fuel cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for die for stamping fuel cell electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the stamping die.    Projection (24')    Top surface (26')    Lateral side (28')    Raised shoulder (32')    Corner portion (40)
NOVELTY - Method for producing carbon monoxide from solid fine-grained organic fuel involves conveying fuel to a gas generator (1) and heating the fuel in generator and producing carbon monoxide, and conveying produced carbon monoxide through fine-grained fuel and filtering carbon monoxide leaving behind impurities in the fuel.    USE - The method and system are useful for producing carbon monoxide from solid fine-grained organic fuel, preferably wood chips (all claimed), where the carbon monoxide is useful for reducing metals from its oxides in metallurgy and useful as raw materials in chemical industry. The method and system are useful for producing combination of heat and electricity, where carbon monoxide produced is useful for rotating generator in combustion engine.    ADVANTAGE - The method enables to produce purified carbon monoxide continuously without interruption. The method is cost-effective as it produces carbon monoxide utilizing agricultural, forestry and construction waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system, which comprises gas generator (1) for gasifying the fuel and producing carbon monoxide, fuel conveyor (2) for transferring the fuel to the gas generator, gas recovery unit (3) for recovering the carbon monoxide, where the gas recovery unit comprises a gas circulation (4) for circulating and filtering the carbon monoxide gas in the fuel being conveyed to the gasification unit.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of system.    Gas generator (1)    Fuel conveyor (2)    Gas recovery unit (3)    Gas circulation (4)    Suction (5)    Blast (6)    Second suction (7)    Spark arrestor (8)
NOVELTY - Extracting oil from human and animal hair and using the oil and cellulose as energy sources, comprises: collecting hair from a variety of sources; liquefying the hair; extracting oil and cellulose from the hair; and utilizing the oil and cellulose extracted from the hair in the same manner as oil derived from fossil fuels.    USE - The process is useful for extracting oil and cellulose from human and animal hair, where the oil and cellulose is useful as energy sources for use in powering homes, businesses, automobiles, airplanes, boats and possibly any fuel driven equipment.    ADVANTAGE - The process provides oil and cellulose, which eliminate or reduce dependence on oil and natural resources and provide consumers with a practical and environmentally friendly way to power their homes.
NOVELTY - Preparing a torrefied biomass fuel, comprises extracting moisture from a relatively wet biomass fuel in a dryer, extracting all remaining moisture to produce a dried biomass fuel, conveying the dried biomass fuel downward using gravity for subsequent processing, torrefying the dried biomass fuel, venting a gaseous mixture of the steam and the torrefaction gases to a heat exchanger, heating the gaseous mixture via heat exchange with a flue gas and using the heated gaseous mixture to support the extraction of the remaining moisture.    USE - The method is useful for preparing a torrefied biomass fuel.    ADVANTAGE - The method can be carried out in a simple and cost-effective manner.    DETAILED DESCRIPTION - Preparing a torrefied biomass fuel, comprises extracting moisture from a relatively wet biomass fuel in a dryer to produce a relatively dry biomass fuel, extracting all remaining moisture from the relatively dry biomass fuel using steam at a temperature of 482 degrees C to produce a dried biomass fuel, conveying the dried biomass fuel downward using gravity for subsequent processing, torrefying the dried biomass fuel to produce the torrefied biomass fuel and torrefaction gases, venting a gaseous mixture of the steam and the torrefaction gases to a heat exchanger, heating the gaseous mixture via heat exchange with a flue gas and using the heated gaseous mixture to support the extraction of the remaining moisture from the relatively dry biomass and the torrefaction of the dried biomass fuel.
NOVELTY - The system (100) has an electrolyzer electrolyzing water (180) to produce hydrogen and oxygen, where the electrolyzer comprises an electrolysis reactor arranged to perform electrolysis reaction with the water. A continuous-flow circulator i.e. water pump (150), circulates a flow of the water through the electrolyzer and comprises a product sweeper structured to sweep the hydrogen and the oxygen through the electrolysis reactor, where the hydrogen and the oxygen are injected to an internal combustion engine (110).    USE - Hydrogen fuel system for electrolyzing water to provide combustible hydrogen fuel i.e. brown's gas, to assist fueling an internal combustion engine of a diesel engine vehicle.    ADVANTAGE - The system allows the water to continuously flow through an electrolysis chamber according to pumping action of the water pump, so that accumulation of generated hydrogen gas and oxygen gas on surfaces of electrode plates within the electrolysis chamber is prevented. The water pump utilizes a diaphragm of a four diaphragm water pump, which is a relay controlled four-diaphragm water pump, so that the pump can pump the water at flow rate of about three and half gallons per minute, thus achieving improved design with higher water flow rate at reduced cost. The system allows a co-combustor to be structured and arranged to co-combust the hydrogen produced by the electrolyzer with a hydrocarbon fuel source, so that fuel efficiency of the internal combustion engine can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen fuel system.    Hydrogen fuel system (100)    Electrolysis chamber (105)    Internal combustion engine (110)    Hydrocarbon fuel source (120)    Water pump (150)    Water (180)    Radiator unit (190)
NOVELTY - Device (10) comprises a pressure vessel (12) with at least one heatable inner space (18) for receiving the reaction educts, preferably at least a portion of an organic material (16), an amount of water and/or additives for carrying out the hydrothermal carbonization, where the inner space of pressure vessel is sealed in the inner space at an elevated pressure relative to the environment in a pressure-tight manner. At least one inner container (14) filled with at least a part of the reaction educts is interchangeably arranged in the inner space of the pressure vessel.    USE - The device is useful for hydrothermal carbonization of organic material, preferably biomass.    ADVANTAGE - The device is suitable for large-scale industries and has smooth outer walls for heating and cooling, which can be easily removed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for hydrothermal carbonization of organic material, preferably biomass, comprising filling at least part of reaction educts, preferably organic material and/or water in the inner space of a pressure vessel (12) is filled, where the interior of the pressure vessel is pressure-sealed and heated, preferably heated for hydrothermal carbonization of the organic material, removing at least a part of the reaction products, preferably the carbonized material, after the hydrothermal carbonation from the inner space of the pressure vessel, and introducing at least a portion of the reaction educts into the inner space of the inner container.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for hydrothermal carbonization.    Device (10)    Pressure vessel (12)    Inner container (14)    Organic material (16)    Inner space (18)
NOVELTY - The equipment (1A) has an anaerobic-treatment tank (4) that maintains a methane producer and a sulfate reducer. A sulfate addition apparatus (8) adds the sulfate stored by a sulfate storage tank (5) to the waste water flowing into the anaerobic-treatment tank. A sulfate addition amount control apparatus (7A) adjusts the addition amount of the sulfate to be increased or decreased with the waste water, when the methane producer and sulfate reducer are coexisted.    USE - Equipment for treating waste water such as industrial waste water and sewage water.    ADVANTAGE - The waste water treatment process can be performed at high speed, by effectively decomposing the organic substance.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the waste water treating equipment. (Drawing includes non-English language text)    Waste water treating equipment (1A)    Anaerobic-treatment tank (4)    Sulfate storage tank (5)    Sulfate addition amount control apparatus (7A)    Sulfate addition apparatus (8)
NOVELTY - A biogas production process involves methane fermentation process which ferments methane and generates biogas after performing the enzyme treatment process which adds the cellulase mixture article which has endocellulase as main component to the waste water which contains wood type biomass as a main component.    USE - A biogas production process.    ADVANTAGE - The biogas is efficiently produced from wood type biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the flow of the biogas production process. (Drawing includes non-English language text.)    Enzyme treatment tank (1)    Enzyme treatment tank body (10)    Separating plate (21)    Waste water supply path (L1)    Transfer path (L2)
NOVELTY - Wastewater treatment method, involves processing organic wastewater containing nonionic surfactant, at least one bacteria of Phyllobacterium having decomposition ability of the nonionic surfactant, and Acidovorax.    USE - The wastewater treatment method is useful for suppressing abnormal foaming, and chemical oxygen demand (COD) and biological oxygen demand (BOD) of the organic wastewater containing nonionic surfactants, such as aqueous coating material wastewater and for industrial coating e.g. auto painting.    ADVANTAGE - The wastewater treatment method is cost-effective.
NOVELTY - Waste material and alkali containing chlorine are introduced into reactor. The resulting waste material containing chlorine is decomposed and demineralized at high temperature, dried and superheated steam is supplied to the reactor. Chlorine is vaporized within the reactor and solid content in the regenerated solid fuel is remained in the reactor. The regenerated solid fuel is washed with water.    USE - Processing of waste material e.g. medical refuse, plastic waste, building waste, motor vehicle shredder dust and municipal solid waste.    ADVANTAGE - The chlorine contained in the waste material is removed efficiently and economically, and the wastewater is treated within a short period of time. The solid fuel with excellent quality is produced.    DETAILED DESCRIPTION - Waste material and alkali containing chlorine are introduced into reactor. The resulting waste material containing chlorine is decomposed and demineralized at high temperature, dried and superheated steam is supplied to the reactor. Chlorine is vaporized within the reactor and solid content in regenerated solid fuel is remained in the reactor. The regenerated solid fuel is washed with water. The water washing time (Y') (in minutes) satisfies the relation: Y'=0.8X2-2.5X+11.7, where X is the mass ratio of water (A) (in g) to the solid content (B) (in g).    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating relationship of solid-liquid ratio and water washing time. (Drawing includes non-English language text)
NOVELTY - Method for separating and recovering microalgae from raw water containing microalgae, involves adjusting salt concentration of raw water so that surface zeta potential of microalgae tends to aggregate, carrying out aggregation reaction by adding inorganic coagulant to the raw water, and separating solid and liquid from the aggregate by solid-liquid separation process.    USE - The method is useful for separating and recovering microalgae from raw water and culture medium used as biofuel, diesel fuel and health food.    ADVANTAGE - The method is simple, reduces usage amount of coagulant, and recovers and separates large amount of microalgae.
NOVELTY - Method for separating and recovering microalgae from raw water containing microalgae, involves adjusting salt concentration of raw water so that surface zeta potential of microalgae tends to aggregate, carrying out aggregation reaction by adding inorganic coagulant to the raw water, and separating solid and liquid from the aggregate by pressurized floatation process.    USE - The method is useful for separating and recovering microalgae from raw water and culture medium used as biofuel, diesel fuel and health food.    ADVANTAGE - The method is simple, reduces usage amount of coagulant, and recovers and separates large amount of microalgae.
NOVELTY - Storing electrical excess energy from electric power plant (1) comprises: (a) producing hydrogen with electric current using at least one hydrogen producing device (5); (b) producing methane containing gas from hydrogen and carbon dioxide separated from flue gases of internal combustion, using at least one methanation device (8); (c) supplying the produced methane containing gas to a gas reservoir (10); and (d) producing electrical energy by combusting the produced methane containing gas using a power producing device (11).    USE - The method is useful for storing electrical excess energy from electric power plant.    ADVANTAGE - The method is cost-efficient and ensures a long-term storage of electrical excess energy.    DETAILED DESCRIPTION - Storing electrical excess energy from electric power plant (1) comprises: (a) producing hydrogen by using electric current using at least one hydrogen producing device (5); (b) producing methane containing gas from hydrogen and carbon dioxide separated from flue gases of internal combustion, using at least one methanation device (8); (c) supplying the produced methane containing gas to a gas reservoir (10); and (d) producing electrical energy by combusting the produced methane containing gas from the gas reservoir using a power producing device (11). The carbon dioxide is separated from the flue gas of internal combustion in the power producing device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the assembly for performing the above method.    Electric power plant (1)    Hydrogen producing device (5)    Methanation device (8)    Gas reservoir (10)    Power producing device (11)
NOVELTY - Manufacture (S10) of electrolytic vessel having anode, ion-exchange membrane and cathode as components involves preparing (S1) condensed water by condensing evaporation steam generated by carrying out evaporative-concentration of sodium hydroxide aqueous solution, contacting (S2) ion-exchange membrane and/or cathode, and condensed water, and assembling (S3) the components.    USE - Manufacture of electrolytic vessel e.g. zero gap-type ion-exchange membrane brine-electrolysis tank used for manufacture of sodium hydroxide, chlorine and hydrogen by electrolysis of solution containing salt (all claimed) e.g. alkali metal salt.    ADVANTAGE - The vessel has favorable electrolysis capability. The elution of metal ion from the cathode in the vessel is suppressed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) usage of condensed water as wash water and/or moisture water during assembly of electrolytic vessel; and    (2) manufacture of sodium hydroxide, chlorine and/or hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacture of the electrolytic vessel. (Drawing includes non-English language text)    Step for preparing condensed water (S1)    Manufacture of the electrolytic vessel (S10)    Step for contacting ion-exchange membrane and/or cathode, and condensed water (S2)    Step for assembling components (S3)
NOVELTY - The apparatus (10) has electrolytic element (14) whose sides are provided with a porous electric power feeding component. A separator is stacked on the porous electric power feeding component. The porous electric power feeding component is provided with a base element. A surface layer element is provided on the opposite side to the electrolytic element side of base element. The porosity of surface layer element is set lower than the porosity of base element, when the porous electric power feeding component is provided in the surface layer element.    USE - High-pressure hydrogen manufacturing apparatus.    ADVANTAGE - The densification and smoothing of surface layer element can be improved effectively, so that durability of the apparatus can be improved efficiently. The damage of the electrolytic element can be prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of porous electric power feeding component of high pressure hydrogen manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the high-pressure hydrogen manufacturing apparatus.    High-pressure hydrogen manufacturing apparatus (10)    Unit cell (12)    Electrolytic element (14)    Anode side separator (16)    Cathode side separator (18)
NOVELTY - The system (10) has gas-liquid separation apparatus (22) which is configured to separate the water content contained in high-pressure hydrogen. A high-pressure water discharge line (26) is configured to discharge high pressure water from gas-liquid separation apparatus. The high-pressure water discharge line is provided with solenoid valve (94) and flow control valve (98). The flow control valve provides pressure loss to water circulated in high-pressure water discharge line, when the solenoid valve is opened.    USE - Water electrolysis system.    ADVANTAGE - The water flows along high-pressure water discharge line can be blocked by connecting tank portion of gas-liquid separation apparatus to flow control valve, so that the durability of solenoid valve can be improved.    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)    Gas-liquid separation apparatus (22)    High-pressure water discharge line (26)    Solenoid valve (94)    Flow control valve (98)
NOVELTY - The apparatus (1) has a gas storage unit that stores biogas emitted from methane fermentation tank (11). A gas-engine generator burns biogas and air which are supplied from gas storage unit (15). A control unit (18) inputs the pressure of the biogas detected by pressure detection unit (13), and controls startup and stop of gas-engine generators (61-63) and excessive combustion equipment (17). The gas-engine generator is operated, after passing for the predetermined time from the time of start-up instruction input into input unit (29).    USE - Biogas apparatus for electric power generation plant.    ADVANTAGE - The gas engine generator is operated, at the time of start-up instruction input into input unit, by preventing the stoppage of gas-engine generator. The low calorie content of biogas can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas apparatus.    Biogas apparatus (1)    Methane fermentation tank (11)    Pressure detection unit (13)    Gas storage unit (15)    Excessive combustion equipment (17)    Control unit (18)    Input unit (29)    Gas-engine generators (61-63)
NOVELTY - Method for preparing ethanol from waste material involves using used paper as paper pulp raw material, subjecting the raw material to low- temperature heat treatment at 60-100 degrees C, cooling the heat treated product to 40-50 degrees C which is suitable for growth of microorganisms, subjecting the product to saccharification and fermentation simultaneously, and adding antibiotic when saccharification and fermentation is simultaneously carried out.    USE - The method is useful for preparing ethanol from waste material collected from office, household and industry. The waste material is preferably used paper.    ADVANTAGE - The method is cost-effective and environmentally-friendly and prevents adverse effects of microorganism during ethanol preparation.
NOVELTY - Preparation of an organic fertilizer containing phosphorus comprises pre-treating lees by uniformly mixing with water; uniformly mixing (pts.wt.) pre-treated lees (25-65), phosphorus mine tailing powder (35-60), water (5-20), inoculating Aspergillus seed culture solution, Bacillus megaterium seed culture solution, and lactic acid bacteria seed culture solution; uniformly mixing, and fermenting; and granulating, and packing.    USE - Method for the preparation of an organic fertilizer containing phosphorus (claimed) used for crops.    ADVANTAGE - The method utilizes the main waste of wine industry and the main waste of phosphate industry. The fertilizer improves crop yield, and improves soil fertility.
NOVELTY - A microbial agent comprises mixed strain (A1) containing Bacillus subtilis, Bacillus megaterium, Bacillus licheniformis and Cellulomonas flavigena.    USE - As microbial agent for processing kitchen waste (claimed) to decompose the waste.    ADVANTAGE - The microbial agent is efficient, and which decomposes kitchen waste with shorter degradation time, and high degradation rate. The strain has fast decomposing ability and the waste can be completely decomposed, and reducing rate can reach 96%. The strain is not toxic, harmless, safe and stable. The process basically reaches the pollution after zero discharge, and the residue can be used as excellent organic fertilizer to the soil, crops for cultivation or city greening, which totally satisfies the standards of organic fertilizer. By using microbial agent, grease of kitchen garbage is effectively degraded; and completely meets the national dietary structure of grease at high feature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of microbial agent involving culturing mixed strain (A1) in the culture medium, putting the mixed strain into the sterilizing wood, and crushing, where the solid culture medium is uniform after crushing; and    (2) a method for processing kitchen waste with the microbial agent involving placing the sterilizing wood chips into processing container, adding water to make the water content of the wood chips to 60-70%, adding the microbial agent to activate, and adding kitchen waste to carry out degradation process.
NOVELTY - The apparatus has rotating disc driving apparatus that drives a rotating disc apparatus. The waste plastic film or lungs drag net on rotating disc apparatus separates soil or mud. An exhausting apparatus collects and removes foreign substances. A conveyor (2) collects foreign substances from the rotating disc apparatus. Another conveyor (3) is installed at the rotating disc apparatus. A frame (1) is provided with partitioning apparatus.    USE - Apparatus for separating dreg e.g. soil or mud with industrial waste or farming and fishing villages waste, used during manufacturing refused plastic fuel.    ADVANTAGE - The foreign substance, mud, and oil meal etc. can be discharged separately through the waste plastic film and the lungs drag net. The useful effect of the apparatus can be improved. The collection effect of the garbage can be improved. The economical efficiency and work efficiency of the apparatus can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the apparatus for separating dreg.    Frame (1)    Conveyors (2,3)    Shaft (12)    Rotary plate (18)    Vane (19)
NOVELTY - A bagasse fermenting organic fertilizer comprises (wt.%): bagasse mortar (16-20), chicken manure (8-13), filter mud (4-8), oil cake (4-8), biological strain (2-10), humic acid (10-12), vermiculite (6-14), bagasse (5-8), and ferment powder waste water concentration liquid (4-8). The concentration of organic matter is more than 60%, nitrogen, phosphorus and potassium is not less than 8%, the water is not less than 20%, effective viable count is not less than 4 million per gram, pH value is 10-13.5.    USE - As bagasse fermenting organic fertilizer (claimed).    ADVANTAGE - The bagasse fermenting organic fertilizer has high efficiency organic fertilizer, it changes waste into valuable product, it improves the soil, improves yield of crop and improves crop quality and reduces the production cost and increases economic income, provides environment protection, and ensures food security. The efficient biological organic fertilizer can supplement soil organic component, improves and regulates the soil organic matter, nitrogen, phosphorus, potassium, ratio of the soil beneficial microorganism and carrier, improves soil structure, and develops ecological agriculture, green food and organic food.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bagasse fermenting organic fertilizer involving: culturing high concentration strain, humic acid, vermiculite, fermenting powder waste water concentrated liquid and bagasse, weighing the high concentration strain and bagasse mortar, chicken manure, filter mud, oil cake, biological strain according to the prescription proportion, putting the stack tank, fully stirring, at the same time, paving a floor on the stack tank, the fermentation time is 7-10 days, uncovering the floor, turning the components, after drying, adding biological calcium, turning and stirring to form particles.
NOVELTY - Agrobacterium tumefaciens strain is new.    USE - The Agrobacterium tumefaciens is useful for removing nitrogen and phosphorus in sewage water using heterotrophic nitrification-denitrification process (claimed).    ADVANTAGE - The Agrobacterium tumefaciens is capable of simply and economically removing the nitrogen and phosphorus in an environmentally friendly manner.
NOVELTY - The method comprises ultrasonically cracking surplus sludge for 15-25 minutes, centrifuging the sludge at 3600-5500 revolutions per minute for 9-20 minutes and then separating, adding enzyme precipitating agent (36-48 vol.%) into the supernatant after mixing and then standing for 2 hours, and filtering the supernatant to obtain the hydrolase. A solid content ratio of the residual sludge is 2-4%. The ultrasonic frequency is 18-25 kHz. The cracking device has a diameter of 20-25 mm. The ultrasonic sound energy density is 0.96-44 kW/l.    USE - The method is useful for recycling hydrolase from surplus sludge.    ADVANTAGE - The method is capable of recycling the hydrolase with high efficiency.
NOVELTY - The method involves sending ecological filter water from culture pond for breeding water ecological filter channel. The water channel aquatic plants are planted. The plant photosynthesis principle is used for ecological filter water absorbing ammonia nitrogen in aquaculture water flowed to the biochemical filter channel. The biochemical filter channel is provided with channel for formation of aquatic plant and beneficial bacteria cluster. The bacteria cluster in the cultivation water of organic waste is used. The lead ammonia is oxidized into nitride.    USE - Cultivation water layer multi-ecological filtering method.    ADVANTAGE - The water purifying effect can be realized efficiently without changing water. The quality of the water can be improved.
NOVELTY - Use of Camellia, is claimed in purification of livestock and poultry biogas slurry, where the Camellia is planted in livestock and poultry biogas slurry pollution environment.    USE - The Camellia is useful in purification of livestock and poultry biogas slurry (claimed) and for treating nosebleed, hemoptysis, cough, burn, scald and mosquito bite.    ADVANTAGE - The Camellia is environmentally-friendly, and purifies slurry with less investment and reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for automatic oxygen supply artificial wetland system, which comprises wetland bed unit comprising wetland filling substrate and shale hollow brick, where the hole of shale hollow brick is equipped with wetland system automatically provides oxygen.
NOVELTY - The system has a spray cooling tower (1) and a tar absorber (4) provided with a lower part feeding port. A tar storage tank (3A) and a flash evaporation tower (5) are provided with an upper feeding port. A condenser (6) is provided with an upper part air outlet. The spray cooling tower is connected with a heat exchanger (2A). A bottom outlet of the tar absorber is connected with the flash evaporation tower that is connected with another heat exchanger (2B). A bottom outlet of the condenser is connected with a top feeding port of a light tar storage tank (3B).    USE - Biomass gas cooling absorption coupled depth tar removal system.    ADVANTAGE - The system removes dust and tar steam through a primary purification process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gas cooling absorption coupled depth tar removal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas cooling absorption coupled depth tar removal system.    Spray cooling tower (1)    Heat exchangers (2A, 2B)    Tar storage tank (3A)    Light tar storage tank (3B)    Tar absorber (4)    Flash evaporation tower (5)    Condenser (6)
NOVELTY - The system has a heavy tar storage tank (3A) provided with an upper feeding port and a discharging port. A condenser (4) is provided with a top air outlet and a bottom discharge hole. The condenser is coupled to a top part of a light tar storage tank (3B). A first valve (5E), a second valve (5G), a third valve (5A) and a fourth valve (5C) are connected to a tar absorption tower (I). A fifth valve (5F), a sixth valve (5H), a seventh valve (5B) and an eight valve (5D) are connected to another tar absorption tower (II).    USE - Biomass gas coupled adsorption depth tar removal system.    ADVANTAGE - The system is inexpensive. The system reduces wastage of ammonia water and waste water discharge. The system realizes oil-water separation so as to obtain better oil product, thus achieving purpose of deep denitrification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing a biomass gas tar coupled absorbs depth tar removing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas coupled adsorption depth tar removal system.    Tar absorption towers (I, II)    Heavy tar storage tank (3A)    Light tar storage tank (3B)    Condenser (4)    Valves (5A-5H)
NOVELTY - Method for processing domestic garbage and other waste into rod-like fuel using garbage fuel rod forming machine, involves spraying aqueous solvent (100 kg) on piles of domestic garbage for inhibiting growth of bacteria and uniformly mixing the garbage, mixing dicyclopentadienyl iron (750-850 kg) and acetate (2-5 kg) with the garbage, and performing extrusion process and drying the product until water content of the product reaches 10-30%.    USE - The method is useful for processing domestic garbage and other waste into rod-like fuel.    ADVANTAGE - The processed domestic garbage has high sulfur denitrification effect and combustion rate, and excellent portability, and is odorless and convenient to store.
NOVELTY - Improving survival rate of wintercreeper cuttings involves preparing substrate comprising fully fermented chaff, humus, bio-organic fertilizer, garden soil, chlorothalonil, perlite and vermiculite; plowing the field, laying black plastic film with excess part hanging on both sides of the furrow, tearing to form openings, and filling the substrate; spraying aqueous formalin solution on substrate at 45 ml/m2; and covering with first layer of white plastic thin film and second layer of black plastic film for 4 days, drying for 5 days, and putting cut wintercreeper branches.    USE - Method for improving survival rate of wintercreeper cuttings (claimed).    ADVANTAGE - The method effectively inhibits or kills plant diseases and insect pests in the soil, without causing environmental pollution, thus, saving production cost; and improves rooting and survival rates to 98%.    DETAILED DESCRIPTION - Improving survival rate of wintercreeper cuttings involves:    (A) preparing substrate comprising (pts. wt.) fully fermented chaff (30-50, preferably 40), humus (50-70, preferably 60), bio-organic fertilizer (6-10, preferably 8), garden soil (5-8, preferably 6), chlorothalonil (0.3-0.6, preferably 0.4), perlite (3-5, preferably 4) and vermiculite (3-5, preferably 4);    (B) plowing the field with furrow height of 15-25 cm and furrow width of 100-150 mm, laying 200-mm black plastic film, in which excess part of the film hangs on both sides of the furrow, tearing to form openings, and filling the substrate;    (C) diluting formalin to 40-80 times with water and spraying on substrate at 45 ml/m2; and    (D) covering with first layer of white plastic thin film and second layer of black plastic film for 4 days, in which the distance between first and second film layers is 20-40 (preferably 30) cm, drying for 5 days, and putting cut wintercreeper branches.
NOVELTY - Nutritional agent is prepared by adding (in parts weight) fulvic acid as organic sequestering agent (50-65), corn starch (10-15), yeast powder (5-10), sodium citrate (1), dithiophosphate (0.76-2), cytokinin (0.8-1), ammonium nitrate (6-10), disodium hydrogen phosphate dodecahydrate (1-2), potassium dihydrogen phosphate (0.5-1), magnesium sulfate (0.2-1), and cobalt chloride hexahydrate (0.02-0.5) to reactor, and uniformly stirring the obtained mixture at normal temperature and normal pressure and at 60 rounds per minute for 60-90 minutes.    USE - The nutritional agent is useful for improving growth of microorganisms, preferably Zoogloea and activity of sludge and used as biological debugging aid or biochemical reagent (all claimed).
NOVELTY - The system has denitrification reactor that is connected to chemical sedimentation tank via a water outlet pipe. A chemical preparation dosing pump is mounted on water outlet pipe. A detector connected with control device is arranged in chemical sedimentation tank. A chemical preparation dosing pump and the detector are connected to control device.    USE - Treatment system for developing sludge inner carbon source.    ADVANTAGE - The rest of sludge and recycle resource substance in the sewage can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the treatment system.
NOVELTY - A livestock excretion briquettes comprises a sample reduction sludge from raw manure selected from pig manure, chicken manure, human excrement, dog excrement, powder compression, farm animal waste, meat animal excrement, anaerobic digestion residue sludge, and livestock wastewater facility, quicklime (10-40 weight parts), and deodorizing agent (10-40 weight parts), where calorific value of the raw manure is 3000-8000 kcal/kg, and the coal of 100-200 weight parts is included based on the raw sample reduction material weight.    USE - Livestock excretion briquettes.    ADVANTAGE - The deodorizing agent in the composition effectively removes poor odor generated in the livestock excretion briquettes or sample reduction sludge.    DETAILED DESCRIPTION - A livestock excretion briquettes comprises a sample reduction sludge from raw manure selected from pig manure, chicken manure, human excrement, dog excrement, powder compression, farm animal waste, meat animal excrement, anaerobic digestion residue sludge, and livestock wastewater facility, quicklime (10-40 weight parts), and deodorizing agent (10-40 weight parts), where the calorific value of the raw manure is 3000-8000 kcal/kg, and the coal of 100-200 weight parts is included based on the raw sample reduction material weight, and the deodorizing agent is made of water treatment plant sludge, phosphoric acid or sulfuric acid (0.01- 0.1 per kg), microorganisms and water. An INDEPENDENT CLAIM is also included for a method for manufacturing livestock excretion sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing livestock excretion sludge.'(Drawing includes non-English language text)'
NOVELTY - Removing oxygen methyltransferase gene to obtain geldanamycin derivative, comprises establishing insertion mutation of oxygen methyltransferase gene to obtain oxygen-methyltransferase gene mutant strain; and performing fermentation to generate geldanamycin derivatives such as 17-oxygen-demethylated geldanamycin and 17-amino-17-demethylated geldanamycin.    USE - The method is useful for removing oxygen methyltransferase gene to obtain geldanamycin derivative. The fermentation product is useful for performing fermentation culture for oxygen-methyltransferase mutation engineered bacteria, and for performing extraction, HPLC detection, mass spectra, and 1H and 13C nuclear magnetic resonance analysis for fermentation product (all claimed). The geldanamycin derivative is useful as precursor of anti-tumor drug or the synthetic anti-tumor drug.    ADVANTAGE - Compared with other method, the method for establishing the engineered bacteria to synthesize two compounds is more economical and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a fermentation product for performing fermentation culture for oxygen-methyltransferase mutation engineered bacteria, and for performing extraction, HPLC detection, mass spectra, and hydrogen isotope (1H) and carbon isotope (13C) nuclear magnetic resonance analysis for fermentation product.
NOVELTY - The method involves inoculating sterilized substrate with soybean, corn and expeller rapeseed. A compost is derived from biomass waste material such as annual crops and energy crops, where initial power of hydrogen value of a tap water is maintained at 4.6-5.0 and at static temperature of 29-31 degree Celsius. The substrate is stirred. Solid substrate components are prepared from lipase after cultivation of mycelium.    USE - Method for preparing immobilized lipase intracellularly racemosus Mucor from solid culture medium.
NOVELTY - The method involves inoculating sterilized substrate with soybean, corn and expeller rapeseed. Compost is derived from biomass waste material such as annual crops and energy crops, where initial power of hydrogen value of a tap water is maintained at 4.6-5.0 at static temperature of 29-31 degree Celsius. The substrate is stirred. Solid substrate components are prepared from lipase after cultivation of mycelium.    USE - Method for preparing immobilized lipase intracellularly racemosus Mucor using solid culture medium.
NOVELTY - Organic fertilizer is manufactured by crushing mixture of bark and leaf of Eucalyptus with dryness degree of 20-40% into 20-60 meshes; uniformly mixing fermentation bacterium and rice bran to obtain fermentation matrix; drying and crushing animal wastes into 10-50 meshes; uniformly mixing the materials, adding water into the mixture, stacking the mixture and covering a plastic film to control temperature in the material stack; fermenting material stack at 30-35 degrees C for 30-60 days, and ending fermentation process when white hypha appears in the stack.    USE - Method of manufacturing organic fertilizer (claimed).    ADVANTAGE - The method has convenient operation and reduced usage of auxiliary materials.    DETAILED DESCRIPTION - Manufacture of organic fertilizer comprises: (A) crushing mixture of bark and leaf of Eucalyptus with dryness degree of 20-40% into 20-60 meshes; (B) uniformly mixing fermentation bacterium and rice bran at weight ratio of 1:10 to obtain fermentation matrix; (C) drying and crushing animal wastes into 10-50 meshes; (D) uniformly mixing materials in steps (A), (B) and (C) at weight ratio of 70-90:1-3:7-27; (E) adding water into the mixture to make water content to 60-65%; (F) stacking the mixture and covering a plastic film to control temperature in the material stack; (G) fermenting material stack at controlled temperature of 30-35 degrees C for 30-60 days, and ending fermentation process when sealing condition of the plastic film has no change while the temperature in the stack begins to reduce and odor of ammonia water and/or wine fragrance occurs, and white hypha appears in the stack at the same time; and (H) and spreading the fermented material stack and drying till the water content is less than or equal to 30%.
NOVELTY - The method involves mixing 20-30 percent humidity feathers with additives plant and lignite coal dust. The mixture is mixed and aerated with bacterial vaccine in an amount of 1012-1014 colony forming units per 100 kg of feathers. A compost mass vaccine is introduced with Trichoderma filamentous fungi. The mixture is stirred periodically, where compost mixture is maintained at 40-60 percent humidity. The treatment is continued till disappearance of the visual structure of the feathers and reaction compost occurs at power of hydrogen value of 6.5-7.5.    USE - Method for removing waste feathers of poultry i.e. chicken, in slaughterhouses and composting places.
NOVELTY - The method involves subjecting a raw material into coal flotation concentrate or silt or fine coal with grain size of 0-4 mm. A particulate biomass and a corn derivative are mixed with hot water to form a mass with water content of 10-15 weight percent. The mass is granulated and dried to final moisture content in the range of 0-10 weight percent. Mixing of raw coal and biomass is carried out with specific mixing intensity, where peripheral speed of mixing tools is 6-10 meter per second.    USE - Method for producing solid fuel boilers i.e. retort boilers.
NOVELTY - The method involves filling a storage tanks with components provided on a mixer. The components are mixed under optimal conditions and optimal composition. The component mixture is fed into a chamber of a conditioner and a baling chamber by buffer tank tube feeders. A granulator product is compressed in a matrix form by a cylindrical hole, where diameter of the hole is 8 mm. The product is cooled and transferred to a storage area.    USE - Method for producing multi-component pellets.
NOVELTY - The system has a biomass and biofuel breeding circuit connected to a plug-in module such that electricity is generated in the breeding circuit from the protein-vitamin concentrate of ethyl esters.    USE - System for producing electricity from biomass and biofuel products.
NOVELTY - Disclosed is novel and green approach for phytosynthesis of gold nanoparticle using Jatropha curcas callus extract. Rare cyclic peptides and a protease enzyme curcain may be responsible for the formation of nanoparticle of different shape and size. The physicochemical characterization of the nanoparticle is carried out using various spectroscopy and microscopy facility chosen from differential scanning calorimetry (DSC), X-ray diffraction (XRD), infrared spectroscopy (IR), transmission electron microscopy (TEM), zetasizer and UV-visible spectroscopy. Image 0/0
NOVELTY - The method involves solidifying sewage sludge for subjecting a fermentation process in a bioreactor, where prepared excess sludge is added with 0.2-0.5 g of sodium hydroxide per 1 gram of dry excess sludge organic matter to homogenize for 20 min. The prepared excess sludge is kept under anaerobic condition at 20 to 30 degree Celsius with a pH value of 9-11. A modified excess sludge is added to a reagent i.e. hydrochloric acid. The prepared excess sludge is mixed with sediment subjected to thermal treatment.    USE - Method for obtaining biogas from sewage sludge.
NOVELTY - Extracting and purifying ginsenoside Rg1, comprises e.g. taking total saponins of Panax pseudoginseng, ginseng or American ginseng extract, adding water to dissolve, passing through a non-polar or weak polar macroporous absorption resin column, washing with water, removing the eluent, eluting with ethanol, collecting the eluate, condensing, drying, adding ethanol to the ginsenoside Rg1 crude product, dissolving, adding silica gel, stirring, volatilizing the solvent on a silica gel column using organic solvent as eluent, collecting the eluate, drying to obtain the dried product.    USE - The method is useful for extracting and purifying ginsenoside Rg1.    ADVANTAGE - The method reduces the production cost, is ecofriendly and suitable for industrial production, has high extraction rate, and produces high yield and high purity (up to 98%) product.    DETAILED DESCRIPTION - Extracting and purifying ginsenoside Rg1, comprises (i) taking total saponins of Panax pseudoginseng, ginseng or American ginseng extract, adding water to dissolve, passing through a non-polar or weak polar macroporous absorption resin column, washing with water, removing the eluent, eluting with ethanol (10-70%), collecting the eluate, condensing, drying, and obtaining ginsenoside Rg1 crude product; and (ii) adding ethanol to the ginsenoside Rg1 crude product, dissolving, adding silica gel, uniformly stirring, volatilizing the solvent on a silica gel column using organic solvent as eluent, collecting the eluate, drying to obtain the dried product; and (iii) dissolving the dried product in water, adding activated carbon (0.1-5), stirring, filtering to remove the activated carbon, and drying to obtain ginsenoside Rg1.
NOVELTY - Method for extracting launobine from Cassytha, involves obtaining Chinese herbs, crushing the herbs, adding crushed herbs and entrainer to supercritical carbondioxide extractor, adding water to macroporous adsorption resin column with ethanol, decompressing and recycling ethanol, drying the ethanol, adding the dried ethanol to silica gel chromatography column, eluting the column, adding absolute ethyl alcohol crystal to concentrated eluate, separating and crystallizing the mixture and washing and drying the mixture to obtain the product.    USE - The method is useful for extracting launobine from Cassytha.    ADVANTAGE - The method extracts launobine easily, simply, cost-effectively and environmentally-friendly with high purity.    DETAILED DESCRIPTION - Method for extracting launobine from Cassytha, involves obtaining Chinese herbs, crushing the herbs, adding crushed herbs and entrainer (1-3%) to supercritical carbondioxide extractor, where entrainer is ethanol and extraction is carried out at pressure of 20-40 MPa at 40-50 degrees C, and the ratio of carbondioxide to crude herbs is 1-3 ml/g and the extracting time is 130-150 minutes to obtain extract, adding water to macroporous adsorption resin column with ethanol (70%), collecting 3-8 times the volume of the column, decompressing and recycling ethanol, concentrating the ethanol, drying the ethanol, adding the dried ethanol to silica gel chromatography column, where the volume ratio of methanol-chloroform mixed solvent is 1:1, eluting the column, combining eluate of 4-6 column volume, concentrating the obtained eluate, adding absolute ethyl alcohol crystal to concentrated eluate, separating and crystallizing the mixture and washing and drying the mixture to obtain the product.
NOVELTY - Manufacture of ammonia comprises converting carbon monoxide to produce carbon dioxide. Methanation and membrane separation are carried out to obtain ammonia. Ammonia is obtained by two-stage conversion process. The outlet temperature of the two-stage conversion process is 740-780 degrees C.    USE - Manufacture of ammonia.    ADVANTAGE - The ammonia is manufactured under mild reaction conditions with reduced equipment investment. The gas load during the process is reduced.
NOVELTY - The device has three-way valve whose outlet is connected with inlet of reaction kettle through the pipeline. The outlet of the three-way valve is connected with inlet of decolorizing tank through pipeline. The inlet of the decolorizing tank is connected to outlet of air compressor through pipeline. The outlet of the decolorizing tank is connected to biodiesel material tank through pipeline and connected to the biodiesel production line. The polyester ether is obtained by using ethanediamine as starting agent, and epoxypropane is copolymerized with ethylene oxide.    USE - Pre-processing device of biodiesel raw material.    ADVANTAGE - The pre-preprocessing of biodiesel material can be performed effectively. The quality assurance to the source of the biodiesel raw material can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pre-processing device of biodiesel raw material.
NOVELTY - A quinazoline derivative is prepared by reacting quinazoline compound with chlorine-containing compound in the presence of strong oxidant.    USE - Method for preparing quinazoline derivatives (claimed) used in Gefitinib preparation.    ADVANTAGE - The method uses easily obtained raw materials, has warm reaction condition, less side effect, high yield, and less environmental pollution.    DETAILED DESCRIPTION - Preparing quinazoline derivatives of formula (Ic) comprises reacting quinazoline compound of formula (II) with chlorine-containing compound of formula (III) in the presence of strong oxidant.    R1=Ra or C(O)Ra;and    Ra=alkyl, alkenyl, alkynyl, cycloalkyl, heterocyclic radical, aryl, or heterocyclic aryl, all optionally substituted.
NOVELTY - Preparation of candesartan intermediate (I) comprises performing acyl chlorination to 2-carboxyl-3-nitroethyl benzoate and thionyl chloride to produce 2-chloroformyl-3-nitroethyl benzoate; reacting 2-chloroformyl-3-nitroethyl benzoate with trinitride to produce 3-nitro-2-formyl azido ethyl benzoate; reacting 3-nitro-2-formyl azido ethyl benzoate with tert-butanol to produce 2-tert-butoxy carbonyl amino-3-nitroethyl benzoate; and performing nucleophilic substitution to 2-tert-butoxy carbonyl amino-3-nitroethyl benzoate and 4'-bromethyl-2-phenyl cyanide.    USE - Preparation of candesartan intermediate (I0.    ADVANTAGE - The method increases solubility of alkali catalyst in reaction system, reduces dosage of alkali catalyst and added phase transfer catalyst, and has low cost. It does not need heating, has simple operation, fast reaction speed, and high conversion rate. It saves energy consumption and minimizes environmental pollution.    DETAILED DESCRIPTION - Preparation of candesartan intermediate (I) comprises performing acyl chlorination to 2-carboxyl-3-nitroethyl benzoate and thionyl chloride to produce 2-chloroformyl-3-nitroethyl benzoate; reacting 2-chloroformyl-3-nitroethyl benzoate with trinitride to produce 3-nitro-2-formyl azido ethyl benzoate; reacting 3-nitro-2-formyl azido ethyl benzoate with tert-butanol to produce 2-tert-butoxy carbonyl amino-3-nitroethyl benzoate; and performing nucleophilic substitution reaction to 2-tert-butoxy carbonyl amino-3-nitroethyl benzoate and 4'-bromethyl-2-phenyl cyanide to produce 2-(N-(tert-butoxy carbonyl)-N-(((2'-phenyl cyanide)-4-yl) methyl) amino)-3-nitroethyl benzoate, in which nucleophilic substitution reaction is performed in presence of phase transfer catalyst and alkali catalyst and in heterogeneous reaction system.
NOVELTY - Magnetic nanoparticles production involves using ionic liquids as reaction solvent in thermal decomposition of complex iron (III) or iron (II) in absence or presence of complexes of other transition metals. A mixture of transition metal ions, surfactants and ionic organic liquid is prepared in a reactor. The obtained mixture is heat treated at 200 degrees C under constant stirring to form black solid. The formed black solid is removed from the ionic liquid by multiple washings with polar organic solvent such as acetone.    USE - Method for producing magnetic nanoparticles for producing static magnetic fluid, medicinal formulations and vectoring systems for drugs (all claimed).    ADVANTAGE - The method produces the magnetic nanoparticles with recycling properties, reduced production cost and surface modification promoting effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of the size distribution of the produced nanoparticles. (Drawing includes non-English language text).
NOVELTY - Preparation of N-(5-methoxy-indolo-ethyl)-4-substituted phenylpiperazine-1-acetamide (I), involves: adding N-4-substituted phenylpiperazine-1-acetamide (II) in an ether solvent; dripping the ether solution containing 5-methoxytryptamine (III) in the presence of strong base catalyst; reacting for 1-4 hours; reacting for 3-5 hours at 30-50 degrees C; and collecting the target product.    USE - For curing benign hyperplasia of prostate.    ADVANTAGE - The method overcomes the shortcoming of high toxicity of the benzene solvent, difficult recycling and complex operation and avoids the environment-friendly hidden trouble of using the pyridine and the zinc powder as the catalyst. Thus, the toxicity of the raw material is reduced, and the yield is largely improved. The operation is safe and simple and the product quality is stable.    DETAILED DESCRIPTION - Preparation of N-(5-methoxy-indolo-ethyl)-4-substituted phenylpiperazine-1-acetamide of formula (I), involves: adding N-4-substituted phenylpiperazine-1-acetamide of formula (II) in the ether solvent; dripping the ether solution containing 5-methoxytryptamine (III) in the presence of strong base catalyst; reacting for 1-4 hours, reacting for 3-5 hours at 30-50 Celsius ,and collecting the target product. The molar ratio of the (II) to (III) is 1:1-2. The mass ratio of the (II) to strong base catalyst is 1:0.04-0.10. The step of collecting the target product involves: washing the reaction fluid until the pH value is 5-6 by using 5-10 wt.% of diluted hydrochloric acid and washing the reaction fluid until the pH value is 7 by using the saturated sodium chloride solution respectively; drying by using the anhydrous sodium sulfate; filtering, depressurizing and recycling the ether solvent; and re-crystallizing the solvent by using the alcohol solvent.    R1 = F, Cl, Br, I, CH3, C2H5, i-C3H7, n-C3H7, i-C4H9, n-C4H9, OCH3, OC2H5, or CF3; and    R2 = CH3, C2H5, i-C3H7, n-C3H7, i-C4H9, or n-C4H9.
NOVELTY - A two stage process of producing fatty acid esters from palm fatty acid distillate (PFAD) which is a byproduct of palm oil refining, using acid chloride route for biodiesel, is discussed. Palm fatty acid distillate is subjected to hydrophilization to separate it into saturated and unsaturated fatty acids. The saturated fraction is heated to 120 degrees C for one hour in a constant temperature oven to remove traces of water present in it. Upon, cooling to room temperature a suitable chlorinating agent is mixed and heated to the appropriate temperature to convert the saturated fatty acids into corresponding acid chlorides to which a stoichiometric amount of alcohol is added and stirred to give saturated fatty alkyl esters and hydrogen chloride gas. The evolving hydrogen chloride (HCl) gas is captured in sufficient amount of alcohol to give alcoholic HCL, which in turn is mixed with the unsaturated fatty acids in a stoichiometric amount to yield unsaturated fatty acids alkyl esters. The unsaturated fatty acids alkyl esters are neutralized and filtered to obtain unsaturated alkyl esters which can be used as cold tolerant biodiesel. Image 0/0
NOVELTY - Atomized carbon hydrogen fuel fog drops are introduced to a coaxially arranged annular plasma discharging area, such that drops produce plasma reforming reaction. Active particles, small molecule mixtures and small amount of unreacted macromolecular hydrocarbon chain substances are directly introduced and filled to a chemical catalyzing reaction bed layer in the cylindrical inner electrode hollow cavity such that sharp catalytic reaction occurs. The generated small molecule mixture is discharged to obtain hydrogen-rich fuel gas with high concentration.    USE - Manufacture of hydrogen-rich fuel gas.    ADVANTAGE - The hydrogen-rich fuel gas is economically and efficiently manufactured using compact device.    DETAILED DESCRIPTION - Atomized carbon hydrogen fuel fog drops are introduced to a coaxially arranged annular plasma discharging area formed by a cylindrical inner electrode and a cylindrical outer electrode, such that the atomized carbon hydrogen fuel fog drops produce plasma reforming reaction based on free radical under the action of the high energy electronic impact. The majority of macromolecular hydrocarbon chain substance is interrupted and activated to generate lots of active particles and small molecule mixtures. Active particles, small molecule mixtures and small amount of unreacted macromolecular hydrocarbon chain substances are directly introduced and filled to a chemical catalyzing reaction bed layer in the cylindrical inner electrode hollow cavity such that sharp catalytic reaction occurs on the surface of the chemical catalysts, and small molecule mixtures are produced. The heat produced by the cylindrical inner electrode is used for heating the chemical catalyzing reaction bed layer. The generated small molecule mixture is discharged to obtain hydrogen-rich fuel gas with high concentration.
NOVELTY - A cost effective and eco-friendly process for the preparation of dapoxetine, chemically known as S(+)-N,N-dimethyl-1-phenyl-3(1-naphthalenyloxy)propanamine hydrochloride with high yield and purity, is disclosed. Further, a process for recovering racemic (+/-)-dapoxetine and its acid addition salts from mother liquors containing salts of unwanted R(-)-enantiomer, is disclosed. Image 0/0
NOVELTY - A solid-liquid separator (120) separates solid and liquid of livestock excretion kept in waterspout (110). An ingredient facility portion (300) introduces influx of air within liquefied fertilizer production unit (100) and compost production unit (200) in order to remove bad smell. A sludge line (420) supplies solid excrements separated from solid-liquid separator to compost production unit. A liquefied fertilizer withdrawal line (430) supplies liquefied fertilizer stored in liquefied fertilizer reservoir (150) to fermentation tank with stirrer (220).    USE - Recycling system for domestic animal excretion.    ADVANTAGE - The livestock excretion of domestic animal can be recycled effectively. The productivity of the compost can be improved effectively. The environmental contamination can be prevented. The residue generated in the liquefied fertilizer can be utilized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the domestic animal excretion recycling system. (Drawing includes non-English language text)    Liquefied fertilizer production unit (100)    Raw water waterspout (110)    Solid-liquid separator (120)    Liquefied fertilizer reservoir (150)    Compost production unit (200)    Stirrer (220)    Ingredient facility portion (300)    Sludge line (420)    Liquefied fertilizer withdrawal line (430)
NOVELTY - Disclosed is an improved cattle dung biogas digester useful for achieving higher efficiency production of biogas and reduced total hydraulic retention time (HRT) for digestion of slurry. The digester is useful for anaerobic digestion of cattle dung slurry, preferably applicable to all fermentable materials viz., starch and sugar containing materials e.g., molasses, high biological oxygen demand (BOD) industrial wastewater, solvents such as acetone, butyl alcohol, acids such as butyric, propionic, acetic and lactic acids to yield combustible biogas. Image 0/0
NOVELTY - Plant includes the following equipment in-series installed and connected by means of pipelines: raw plant waste crusher connected to waste receivers, the outlet of which is connected via pipeline to inlet of the first centrifugal or screw pump for substrate pumping; pump outlet is connected via pipeline to inlet of reactor of preliminary acid fermentation, the outlet of which is connected via pipeline to inlet of the second centrifugal or screw pump for substrate pumping, the outlet of which is connected via pipeline to inlet of the main reactor - methane tank; at that, gas outlet of reactor -methane tank is connected to inlet of biogas compressing compressor the outlet of which is connected to high pressure gas holder inlet, and high pressure gas holder outlet is connected through cyclone and biogas cleaning system to catalytic biogas converter the outlet of which is connected to inlet of battery of solid oxide fuel cells; at that, catalytic biogas converter and battery of solid oxide fuel cells are contained in temperature-controlled chamber; at that, battery of solid oxide fuel cells is electrically connected to battery of accumulators and inverter; besides, outlet for warmed-up gases of battery of solid oxide fuel cells is connected via heat pipeline to inlet of heat recuperation system the outlet of which is connected to submersible heat exchanger located in reactor of preliminary acid fermentation, which is in-series connected to submersible heat exchanger in the main reactor - methane tank.    USE - Power industry.    ADVANTAGE - Utilisation of agricultural wastes, obtaining of biogas, generation of electric and thermal power, and obtaining of useful biofertiliser. 1 dwg
NOVELTY - The process involves flashing carbon dioxide and residual gas e.g. hydrogen, from a carbon dioxide-rich solvent stream (24) to form a carbon dioxide-rich flash stream (54). The carbon dioxide-rich flash stream is compressed to predetermined high pressure. The carbon dioxide-rich flash stream is cooled and expanded to predetermined low temperature and pressure to form a cooled expanded carbon dioxide-rich flash stream. The cooled expanded carbon dioxide-rich flash stream is fractionated to form a carbon dioxide-ultra-rich product stream (150) and a residual gas stream (152).    USE - Process for removing acid gas e.g. carbon dioxide and residual gas such as carbon monoxide, hydrogen and methane (all claimed), water and hydrogen sulfide, from synthesis gas (syngas) e.g. water vapors and light hydrocarbons, to form a carbon dioxide-ultra-rich product stream with ultra high content of carbon dioxide with ultra low amounts of carbon monoxide. Can also be used for removing carbonyl sulfide, sulfur compounds and hydrogen cyanide.    ADVANTAGE - The process enables removing hydrogen sulfide from the compressed carbon dioxide-rich flash stream, thus improving carbon dioxide purity downstream in the final product carbon dioxide-ultra-rich product stream. The process enables advancing regeneration gas stream to a vessel through an opened valve, thus preventing fluid communication of the compressed carbon dioxide-rich flash stream to the vessel by a closed valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a system for removing acid gas from syngas.    Gas absorbers (12, 14)    Carbon dioxide-rich solvent stream (24)    Carbon dioxide-rich flash streams (54, 64, 74)    Carbon dioxide-ultra-rich product stream (150)    Residual gas stream (152)
NOVELTY - The present invention relates to a continuous system and method for producing biodiesel, wherein the continuous method for producing biodiesel includes the following steps: (a) performing continuous pressing-extraction using a continuous pressing-extraction module, wherein the continuous pressing-extraction module has multiple pressing-extraction devices, and at least one of the pressing-extraction devices is used for receiving liquid alcohol, and the pressing-extraction is performed with the lipid source within the pressing-extraction device to obtain a pressing-extracted liquid; (b) performing transesterification for the pressing-extracted liquid to obtain a transesterification product; and (c) separating the transesterification product to obtain biodiesel. The continuous system and method for producing biodiesel according to the present invention utilizes the continuous pressing-extraction module and method to perform pressing-extraction and then perform alcohol transesterification. The pressing-extraction and transesterification are continuous processes to simplify the process, save labor forces and cost, and reduce energy consumption.
NOVELTY - A self-contained processing unit (100) consists of a reactor vessel (220) arranged to receive a material to be pyrolyzed, a source of microwave radiation, and a processing-unit controller. The unit is operable by the controller to irradiate material contained within the reactor vessel with microwave radiation to heat the material to evolve hydrocarbon compounds. The unit is operable to provide a flow of evolved hydrocarbons from pyrolyzed material to a storage unit.    USE - Self-contained processing unit is used for pyrolyzing hydrocarbon-containing material and extracting hydrocarbons from hydrocarbon-containing material e.g. plastic materials, rubber, food waste and peelings, paper, boards, garden waste, carpets, polymers, and synthetic fabrics, in domestic buildings (all claimed). Can also be used in hospitals, restaurants, hotels, schools, factories, and food processing facilities, and to generate diesel fuel for use in domestic or industrial vehicles.    ADVANTAGE - The self-contained processing unit uses microwave which efficiently heats the material to be pyrolyzed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction of hydrocarbons from hydrocarbon-containing material by pyrolysis using the self-contained processing unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolysis unit or module.    Self-contained processing unit (100)    Casing (101)    Display (105)    Door (110)    Reactor vessel (220)
NOVELTY - A hydrogen separation membrane has a surface catalyst layer comprising a palladium alloy, or a surface layer comprising palladium alloy including metal(s) chosen from group 5A and group 6A. The content of palladium is 0.01-10 mol%.    USE - Hydrogen separation membrane is used for hydrogen separator (claimed) for hydrogen production apparatus for producing hydrogen used as fuel for fuel cell.    ADVANTAGE - The hydrogen separation membrane has excellent durability with reduced occurrence of Kirkendall voids regardless of the adherence of extrinsic airborne particles.
NOVELTY - The method involves preparing several composites (20) each formed by sandwiching an interconnector (22) between a lower insulating layer (24) and an upper insulating layer (26). A trench is formed on the upper and lower surfaces of the insulating layers. An electrolyte film (102) is formed in the space between adjacent two composites. The trench is divided by spraying a conductive material obliquely with respect to a direction approaching to the insulating layer of the trench.    USE - Manufacturing method of fuel cell (claimed) for portable device. Uses include but are not limited mobile telephone, notebook-type personal computer, personal digital assistant, MPEGaudio layer-3 (MP3) player, a digital camera, electronic dictionary and electronic book.    ADVANTAGE - The manufacturing process of the fuel cell is made simple. The productive time and the manufacturing cost of the fuel cell are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic views illustrating the fuel cell manufacturing process.    Composite (20)    Interconnector (22)    Lower insulating layer (24)    Upper insulating layer (26)    Electrolyte film (102)
NOVELTY - Temperature and pressure of a mixture containing aliphatic compound produced by algae and hydrocarbon solvent maintained in supercritical state with critical temperature of 90 degrees C or more are adjusted such that solubility of aliphatic compound with respect to 100 g of solvent is 15 g or less. The soluble portion of aliphatic compound in solvent is recovered and hydrogenated using a catalyst. Thus, hydrocarbon fuel is manufactured.    USE - Manufacture of hydrocarbon fuel.    ADVANTAGE - The hydrocarbon fuel having high quality is stably manufactured.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of manufacturing apparatus of hydrocarbon fuel.    Aliphatic compound extraction separation tank (1)    Solvent separation tank (2)    Hydrogenation reactor (3)    Mixing apparatus (12)    Heating apparatus (13)    Intermediate tank (18)
NOVELTY - A biomass catalytic cracking catalyst is produced by a) modifying a phyllosilicate to produce a modified phyllosilicate having improved yield when used in a biomass pyrolysis reaction, where the modifying step involves leaching phyllosilicate to form a leached phyllosilicate preparation, calcining leached phyllosilicate preparation to form a treated phyllosilicate that contacting with a suspension comprising metal ions to form a modified phyllosilicate; b) mixing modified phyllosilicate with inorganic materials to form a mixture; and c) shaping the mixture into fluidizable microspheres.    USE - In biomass pyrolysis (claimed) or in gasification of solid biomass material.    ADVANTAGE - Use of the biomass catalytic cracking catalyst in the biomass pyrolysis provides reduced coke yield, reduced oxygenated product and improved bio-oil yield.
NOVELTY - A low temperature fluidity improver contains carboxylate derivative (I).    USE - Low temperature fluidity improver for fatty acid methyl ester composition and biodiesel fuel composition (all claimed) use in winter or cold region.    ADVANTAGE - The fluidity improver improves the pour point of the fatty acid methyl ester and has low filtration-clogging temperature.    DETAILED DESCRIPTION - A low temperature fluidity improver contains carboxylate derivative of formula: H((CH(-C16H33)-CH2)m(CH(-C(=O)-OR1)-CH(-C(=O)-OR2))n)p-H (I).    R1,R2=H or 1-30C aliphatic hydrocarbyl;    m,n=1-50;    p=1-5000;and    m/n=0.4-4.    80 mol% or more of the sum total of R1,R2 is 1-30C aliphatic hydrocarbyl. INDEPENDENT CLAIMS are included for the following:    (1) low temperature fluidity improver composition, which contains the low temperature fluidity improver, and polymer chosen from ethylene vinyl acetate copolymer, styrene (meth)acrylic acid ester copolymer, (meth)acrylic acid ester polymer and vinyl acetate polymer;    (2) fatty acid ester composition, which contains 0.01-5 %mass of the fluidity improver;    (3) biodiesel fuel composition, which contains 0.0002-5 %mass of the fluidity improver; and    (4) manufacture of the low temperature fluidity improver, which involves esterifying 1-30C aliphatic monohydric alcohol, and polymerize-reacting with ( alpha )-octadecene and maleic anhydride.
NOVELTY - The fermentation tank (11) has a fermentation section (17) that stores the fermented liquor (B) which consists of waste materials (A), and generates methane gas. An upper chamber (18) stores the process liquid (D) generated in the fermentation section in a scum in separate state. An exhaust passage (28) provided in the high liquid level portion of the fermentation section discharges the scum outside.    USE - Methane fermentation tank used in fermentation process system for processing organic refuse discarded from home, agriculture, stock raising industry, and fishery.    ADVANTAGE - The scum separated from the fermented liquor which consists of waste materials stored in the fermentation section of the methane fermentation tank can be discharged to the exterior easily through exhaust passage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the fermentation process system.    Methane fermentation tank (11)    Fermentation section (17)    Upper chamber (18)    Exhaust passage (28)    Waste material (A)    Fermented liquor (B)    Process liquid (D)
NOVELTY - An in-situ microbe scene synergistic sewage treatment comprises sampling sewage at spot; carrying out analysis to water sample contaminants and bacteria; screening the strain; configuring to fit advantage strain the culture base and test culture condition; screening out according to scene condition and culture condition and design set with special culture device, setting and debugging and operation parameter; scene culture advantage effective bacteria; and adding bacteria, and carrying out biochemical treatment to the sewage.    USE - An in-situ microbe scene synergistic sewage treatment.    ADVANTAGE - The method has reduced investment, short construction period, and low operation cost.
NOVELTY - Generating livestock manure marsh gas comprises removing sand of the livestock manure, removing the livestock excrement after sand produce marsh gas by fermenting, carrying out desulfurization, dedusting and dehydrating the marsh gas and then generating electricity. The waste heat is set by waste heat recycle device for hydrolyzing and heating the fermentation device.    USE - Method for generating livestock manure marsh gas (claimed).    ADVANTAGE - The method can make the livestock manure marsh gas power generation engineering smoothly operated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a livestock manure marsh gas power generating system comprising a stirring pool, hydrolyzing pool, anaerobic fermentation tank, marsh gas biological desulfurization tower, air storage cabinet, biogas preprocessing system, and marsh gas power generation set.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for generating livestock manure marsh gas (Drawing includes non-English language text).
NOVELTY - Fermentation groove comprises transmission belt, where the transmission belt is connected with a transmission belt seal and the active sealing shed which is arch in shape of cylindrical sealing cavity.    USE - The fermentation groove is useful for producing bioorganic fertilizer.    ADVANTAGE - The groove occupies less space, has simple structure, is suitable for industrial production and environmentally-friendly, can create a sealed negative pressure environment, provides complete fermentation, and emits no malodorous gas as material.
NOVELTY - Briquette comprises lignocellulosic compressed structure comprising (a) grass stem debris (60-90 wt.%) and (b) beaten lignocellulosic binder (10-40 wt.%) having beating degree of 38-75 degrees Schopper-Riegler (SR), preferably 45-70 degrees SR, where the percentages are expressed by dry weight relative to the dry weight of the sum of (a) and (b) and of a fuel that is liquid at room temperature having a flash point of 30-150 degrees C, impregnating the lignocellulosic compressed structure, and the briquette has an essentially cylindrical shape and comprising a central chimney with a star-shaped cross-section.    USE - The briquette is used as fuel in torches, firelighter or for heat production, preferably for cooking or reheating food (claimed).    ADVANTAGE - The briquette is compact, lightweight and safe to use, as it does not contain gaseous fuel, can be carried by children and individual in crowd, exhibits steady combustion with same flame power throughout the duration of combustion, and produces less smoke and fly ash.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process for manufacturing briquettes, which involves (a) mixing an aqueous suspension of a lignocellulosic binder with grass stem debris in proportions such that the ratio by dry weight of the lignocellulosic binder to the grass stem debris is 10/90-40/60, (b) molding the mixture obtained in a suitable mold/countermold assembly at a temperature of 40-120 degrees C under a pressure of 3-12 bar applied for a duration of 5-120 seconds, (c) demolding the compressed structure obtained, and (d) impregnating the demolded compressed structure with a fuel, which is liquid at room temperature having a flash point of 30-150 degrees C.
NOVELTY - The insecticidal composition comprises spinosad and cyantraniliprole amide according to a weight ratio of 100:1-1:100.    USE - The insecticidal composition is useful: for preventing louse and thrips, where the thrips are melon thrips, onion thrips and rice thrips; and crop including cucumber, cotton, rice and hairy gourd (all claimed).    ADVANTAGE - The environmentally friendly insecticidal composition has improved pest drug resistance and long service life.
NOVELTY - Multi-stage anaerobic reactor comprises main portion connected with first reactor tank, second reactor tank and third reactor tank, where first reactor tank is useful for stirring components, second reactor tank and third reactor are useful for filling components in reactor.    USE - The multi-stage anaerobic reactor and method are useful for producing methane gas (all claimed).    ADVANTAGE - The multi-stage anaerobic reactor improves efficiency of methane gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing methane gas using the above-mentioned multi-stage anaerobic reactor, which involves adding raw materials to the first reactor tank and uniformly stirring the components, where the components enters into second reactor tank, and processed product enters into third reactor tank, and finally methane gas is discharged from the third reactor tank.
NOVELTY - A closed circuit circulating technique for treating fermented biogas of pig farm wastewater comprises putting biogas slurry wastewater to adjusting pool, heat flocculating-filtering to remove wastewater biogas fermentation bacteria to obtain mycoprotein; removing bacteria mother solution and concentrating; sending crystal slurry to centrifugal separation, spray part of crystallized mother liquid for producing organic fertilizer and returning remaining crystallization mother solution to the pig biogas liquid.    USE - A closed circuit circulating technique for treating fermented biogas of pig farm wastewater.    ADVANTAGE - The method solves the problem of the pig farm wastewater; at the same time, obtains the thalli protein, crystalline salt, organic compound fertilizer and other products. The evaporated cooled water can be used as the production water for use.    DETAILED DESCRIPTION - A closed circuit circulating technique for treating fermented biogas of pig farm wastewater comprises:    (A) putting biogas slurry wastewater to adjusting pool, adding water for reflux crystallization mother liquid, heat flocculating-filtering to remove wastewater biogas fermentation bacteria to obtain the mycoprotein and sterilizing;    (B) removing bacteria mother solution and concentrating to obtain condensed water and crystal slurry;    (C) sending the crystal slurry to centrifugal separation, obtaining the crystal salt and crystallized mother liquid; and    (D) taking out part of crystallized mother liquid, spray drying for producing organic fertilizer and returning remaining crystallization mother solution to the pig biogas liquid with high concentration wastewater.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram illustrating the closed circuit circulating technique for treating fermented biogas of pig farm wastewater (Drawing includes non-English language text).
NOVELTY - The method comprises pre-processing sludge in an ultrasonic processor for 1-10 minutes, introducing the sludge into a pool for hydrolysis acidification for 24-72 hours to obtain fermentation solution, entering the sludge into a methane tank to perform methane fermentation, and subsequently ultrasonic pre-processing the sludge for acidification pre-process for 14-16 hours. The hydrolysis fermentation liquid has a reflux quantity of 50-90%. The solid content of the sludge in the acidification pre-process is 2-4%. An ultrasound energy density of the ultrasonic pretreatment is 0.65-0.8 kW/m3.    USE - The method is useful for pre-treating sludge.    ADVANTAGE - The method is capable of effectively and rapidly pre-treating the sludge with reduced energy consumption.    DETAILED DESCRIPTION - The method comprises pre-processing sludge in an ultrasonic processor for 1-10 minutes, introducing the sludge into a pool for hydrolysis acidification for 24-72 hours to obtain fermentation solution, entering the sludge into a methane tank to perform methane fermentation, and subsequently ultrasonic pre-processing the sludge for acidification pre-process for 14-16 hours. The hydrolysis fermentation liquid has a reflux quantity of 50-90%. The solid content of the sludge in the acidification pre-process is 2-4%. An ultrasound energy density of the ultrasonic pretreatment is 0.65-0.8 kW/m3. The ultrasonic processor is a probe. The ultrasonic frequency is 18-30 kHz. The probe has a diameter of 20-30 mm.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for pre-treating sludge (Drawing includes non-English language text).
NOVELTY - Ferrate oxidation sewage treatment is carried out using a system consisting of a biochemical treatment unit, a deposition unit, a ferrate oxidation processing unit, and a sludge dewatering unit. The biochemical treatment unit removes organic pollutants using microorganisms. The sewage is settled to obtain settled sludge and clear water. 2/3 of settled sludge is returned to the biochemical treatment unit. 1/3 of sludge is sent to sludge reaction tank and ferrate is added and reacted. The surplus sludge is then filtered or centrifugally dewatered.    USE - Ferrate oxidation treatment of sewage e.g. industrial sewage and city sewage.    ADVANTAGE - The method reduces residual sludge output to 35-45%. The device used has a simple structure, and can be operated conveniently with easy and economical management.    DETAILED DESCRIPTION - Ferrate oxidation sewage treatment is carried out using a biochemical treatment system consisting of a biochemical treatment unit, a deposition unit, a ferrate oxidation processing unit, and a sludge dewatering unit. The biochemical treatment unit removes organic pollutants using microorganisms, and organic pollutants are converted into small molecular substances. The sewage is settled in the deposition unit to obtain settled sludge and clear water. 2/3 of settled sludge is returned to the biochemical treatment unit. 1/3 of sludge is sent to sludge reaction tank and ferrate (0.2 g/kg sludge solid) is added and reacted for 10-30 minutes in the ferrate oxidation processing unit. The mass ratio of ferrate and surplus sludge is 0.2:1. The surplus sludge is then filtered or centrifugally dewatered in the dewatering unit.
NOVELTY - The dryer has a cylinder (1) whose inlet and outlet ends are connected with guide plates (4). A roller wall is provided with secondary guide turning mud plates (5) that are arranged around an axial rod. A fence bar (10) and the cylinder are arranged on an inner wall of a flange (18). The fence bar is connected with the cylinder. A conveyor and a smoke inlet pipe are connected with the cylinder that is connected to a drying sludge discharging machine and a smoke outlet pipe. A fan is connected with the smoke inlet pipe.    USE - Efficient energy-saving environment-friendly sludge dryer.    ADVANTAGE - The dryer changes wastage into valuable, thus improving drying effect and high yield. The dryer is reasonable in structure, inexpensive and reliable to use. The dryer avoids erosion, difficult adhesion and blocking effect and ensures safety. The drier has prolonged service life and high automation degree.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an efficient energy-saving environment-friendly sludge dryer.    Cylinder (1)    Guide plates (4)    Secondary guide turning mud plates (5)    Fence bar (10)    Flange (18)
NOVELTY - Active soil fertilizer comprises (in kg): animal manure (15-50), pond sludge (4.5-15), plant straw powder (9-30), deodorizing agent (0.5-2), and fermentation decomposition ripening agent (1.5-5). The deodorizing agent is ferrous sulfate, and magnesium sulfate having weight ratio of 2:3. The fermentation decomposition ripening agent is 923 complex cobacterial composition. The fertilizer has a diameter of 1.5-4.5 mm, and has a shape of mung bean grain.    USE - The active soil fertilizer is useful for promoting growth of crops in soil.    ADVANTAGE - The fertilizer can improve soil effectively, yield and quality of crops, enhances soil fertility, has improved permeability and decomposing ability with respect to soil, prolonged fertilizer effect, and high utilization ratio, and is abundant in nutrient substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing organic biofertilizer, which involves obtaining animal manure, pond sludge, plant rice powder, and deodorizing agent, stirring obtained materials for 2-3 minutes, adding fermenting decomposition ripening agent to the stirred materials, stirring the materials evenly, and stacking the materials having piling height of 1.5 m, performing aerobic fermentation for 10-21 days, crushing the fermented materials, pelleting the crushed materials, polishing the pellet, drying the pellet, and packaging the dried material, where the polishing is performed by mixing root powder (1.5-3), and amino acid brightener (2-2.5) to obtain mixed slurry, and polishing film coating for polishing the surface of the fertilizer particle after granulation at 5-35 degrees C.
NOVELTY - The device has main structure that is provided with a reverse tapered vertical tank. A fluidized gas system is connected to lower portion of the main structure. A fluidization enveloping system and negative pressure pumping system are connected to middle portion and upper portion of the main structure respectively.    USE - Coat film device used in production of slow release fertilizer, used for manufacture of coated particle fertilizer (claimed).    ADVANTAGE - The coating of the fertilizer is made uniform and dust pollution is reduced such that environmental pollution is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the coat film device used in production of slow release fertilizer.    Gas exhaust pipe (1)    Draught fan (2)    Screen (3)    Feeding port (4)    Coating injector (6)
NOVELTY - Garbage microwave cracking treatment comprises pre-treating organic solid waste material; continuously feeding garbage in a microwave cracking device, carrying out microwave irradiation at 2450 plus minus 50 MHz, increasing garbage temperature to 350-650 degrees C to crack, and controlling the microwave cracking device at not greater than 1.6 MPa; and condensing liquid with spray water to the condensed cracking gas into a steam-water separator, separating liquid part and gas part, and processing by oil-water separator; and cracking solid product composition for cracking carbon and inorganic ash.    USE - Method for garbage microwave cracking treatment (claimed).    ADVANTAGE - The method has low energy consumption and is inexpensive, has high resource utilization rate, simple operation, and has improved garbage volume reduction rate.    DETAILED DESCRIPTION - Garbage microwave cracking treatment comprises:    (A) pre-treating organic solid waste material, oil, and residue obtained by fermenting organic matter, where the organic matter has a water content after dehydrating and crushing of less than 13% and grain size of less than structured garbage is suitable for splitting garbage with microwave to 100 mm;    (B) continuously feeding garbage in a microwave cracking device, carrying out microwave irradiation at 2450 plus minus 50 MHz, increasing garbage temperature to 350-650 degrees C to crack, and controlling the microwave cracking device at not greater than 1.6 MPa; and    (C) condensing liquid with spray water to the condensed cracking gas into a steam-water separator, separating liquid part and gas part, where the liquid part comprises tar and water, and processing by oil-water separator; and cracking solid product composition for cracking carbon and inorganic ash.
NOVELTY - The method involves arranging a macro-molecular organic substance on a biological oil depolymerization part under condition of a visible light catalyst. The visible light catalyst is provided with a load-type catalyst or doped catalyst. A load transition element and the load-type catalyst are made of iron, ruthenium, cobalt, rhodium, nickel, platinum, palladium, silver, gold or zinc. The doped catalyst is made of nitrogen, sulfur, halogen or carbon and transition metal ion e.g. ferric, molybdenum ion, ruthenium ion, osmium ion, vanadium ion or rhodium ion.    USE - Method for refining biological oil in an organic macro-molecular fuel component.    ADVANTAGE - The method ensures better absorption catalyst function of wavelength light. The method enables providing a light catalytic activated lignin oligomer with high energy obtained in a small molecule product. The method enables avoiding a complex structure of the light catalytic activated lignin oligomer. The method enables simplifying a structure of a small molecule organic matter. The method enables depolymerizing biological oil in an organic macro-molecular fuel component to improve a biological oil rate in an effective manner.    DETAILED DESCRIPTION - The visible light catalyst of a carrier is titanium dioxide granule, titanium dioxide film, silicon dioxide-titanium dioxide film, antimony doped titanium dioxide thin film, cadmium sulfide, cadmium sulfide-titanium dioxide, zinc oxide or tungsten trioxide. The load-type catalyst is platinum-ruthenium/cadmium sulfide titanium dioxide.
NOVELTY - The system has a control unit that is connected to an air storage pool, to control program during operation state. An electric burner burns gas in node unit by carrying out heat preservation treatment for bioreactor, to ensure the system operation within the reliable temperature range. The nutrition supply unit is provided with hydrogen sulfide and carbon dioxide. The nutrition supply of bio-reactor is controlled by node unit. A collecting unit is arranged for collecting the methane and hydrogen in the bioreactor.    USE - Distributed energy, bio-energy linkage of gas supply system.    ADVANTAGE - The efficiency, operability, reliability and usability of the distributed energy, bio-energy linkage of gas supply system can be improved.    DETAILED DESCRIPTION - A light energy collector and biological reaction tank are arranged in the bioreactor. The control center controls bioreactor top node according to parameter change of gas and liquid phase in the energy system. The gas collecting center collects methane gas and carbon dioxide gas in each node.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the distributed energy, bio-energy linkage of gas supply system. (Drawing includes non-English language text)
NOVELTY - Method for manufacturing round strip type polymerizing fuel coal, involves (a) drying and crushing fuel, red mud, iron or tailings, flue-gas desulfurization (FGD) gypsum, coke breeze, lignite, coal gangue and biomass, (b) carrying out polymerization by stirring fuel, red mud, coke breeze, lignite, coal gangue, and biomass with binder and water, and (c) adding the above mixture to a roller annular strip type extrusion forming machine.    USE - The method is useful for manufacturing round strip type polymerizing fuel coal.    ADVANTAGE - The method manufactures round strip type polymerizing fuel coal with high quality, and polymerizing fuel coal reduces emission and saves energy, increases economic value, and is environmentally-friendly and cost-effective.    DETAILED DESCRIPTION - Method for manufacturing round strip type polymerizing fuel coal, involves (a) drying and crushing fuel, red mud, iron or tailings, flue-gas desulfurization (FGD) gypsum, coke breeze, lignite, coal gangue and biomass to a particle size of 60-200 meshes, (b) carrying out polymerization by stirring (in wt.%) fuel (5-20), red mud (10-80), coke breeze (10-30), lignite (5-12), coal gangue (5-10), biomass (5-30), binder (2) and water (suitable amount), (c) adding the above mixture to a roller annular strip type extrusion forming machine, (d) adjusting the ratio of fuel, coal, coke, lignite and biomass so that the annular strip type polymerizing fuel coal generates 3000-6000 kcal/kg of heat, and (e) adjusting the ratio of fuel, coal, coke, lignite and biomass so that the annular strip type polymerizing fuel coal has a volatile content of 10-30%.
NOVELTY - Preparing 2-(benzyl acrylolyl amino)acetic acid benzyl ester comprises: reacting acrylic acid with the alkyl chloro formate (I) in the presence of suitable base and an organic solvent to give 2-benzylacrylic(alkyl carbonic) anhydride (II) which is optionally isolated; and reacting (II) with glycine benzyl ester or its salt.    USE - The process is useful for preparing 2-(benzyl acrylolyl amino)acetic acid benzyl ester.    ADVANTAGE - The process: is simple, cost effective, eco-friendly, reproducible, robust and is well suited on commercial scale; and provides the intermediates with higher yields and purities of final product with at least 99 area % by HPLC.    DETAILED DESCRIPTION - Preparing 2-(benzyl acrylolyl amino)acetic acid benzyl ester comprises: reacting acrylic acid with the alkyl chloro formate of formula (Cl-C(=O)-O-R) (I) in the presence of suitable base and an organic solvent to give 2-benzylacrylic(alkyl carbonic) anhydride of formula (II) which is optionally isolated; and reacting (II) with glycine benzyl ester or its salt of formula (glycine benzyl ester.HX).    R = 1-6C alkyl or aryl; and    HX = acid addition salts such as those made with hydrochloric, hydrobromic, hydroiodic, methylsulfonic, perchloric, sulfuric, nitric, phosphoric, acetic, propionic, glycolic, lactic pyruvic, malonic, succinic, maleic, fumaric, tartaric, citric, benzoic, carbonic cinnamic, mandelic, methanesulfonic, ethanesulfonic, benezenesulfonic, hydroxyethanesulfonic, p-toluene sulfonic, cyclohexanesulfamic, salicyclic, p-aminosalicylic, 2-phenoxybenzoic or 2-acetoxy benzoic acid.    An INDEPENDENT CLAIM is also included for racecadotril having a purity of at least 98 area % by HPLC and having less than 0.1 area % of individual impurity and 0.5 area % of total impurities by HPLC.
NOVELTY - The integration method comprises adding livestock manure into farm manure, primarily separating urine of livestock manure and auxiliary material for pre-mixing and for furfural residue or other fungi and corn flour and then fermenting, mixing the livestock manure to ferment into fermentation and then drying by dryer, fermenting the mixture and then baking by heat boiler composed of a garbage discharging high temperature steam, and putting the fermented organic matter into drying and then granulating to prepare organic fertilizer.    USE - The integration method is useful for livestock excrement as fertilizer.    DETAILED DESCRIPTION - The integration method comprises adding livestock manure into farm manure, primarily separating urine of livestock manure and auxiliary material for pre-mixing and for furfural residue or other fungi and corn flour and then fermenting, mixing the livestock manure to ferment into fermentation and then drying by dryer, fermenting the mixture and then baking by heat boiler composed of a garbage discharging high temperature steam, and putting the fermented organic matter into drying and then granulating to prepare organic fertilizer. The pre-mixing and livestock manure fermentation time period adopts totally enclosed automatic operation.
NOVELTY - The compost composition comprises 20-30 parts by weight (pbw) of bamboo fungus, 20-30 pbw of wood chips, sawdust or roots of other trees, 20-30 pbw of bagasses, 10-20 pbw of husks and inorganic compounds comprising potassium salt, magnesium salt and calcium salt, 1-3 pbw of urea, 5-10 pbw of ammonia carbonate, 0.3-0.5 pbw of monopotassium phosphate, 0.2-0.3 pbw of magnesium sulfate, and 1.0-1.2 pbw of calcium carbonate. The composition is replaced by 20-30 pbw of corncobs, 5-10 pbw of corn powder or 5-10 pbw of thin rice bran.    USE - The compost composition is useful for: improving amino acid contents in bamboo fungus sporocarps; treating neurasthenia, hypertension and gastrointestinal diseases; calming mind; improving immunity; relieving cough; protecting liver; and reducing accumulation of abdominal fat.    ADVANTAGE - The composition has high nutritional value and delicious taste, reduces pollutant discharge in pig breeding process, and ensures recycling and re-usage of pig manure residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of cultivating compost composition.
NOVELTY - The system has a cooling dust remover, an indirect cooler and a gas-water separator, where an inlet of the dust remover is connected with a gasification furnace. An outlet end of the dust remover and the indirect cooler are connected with an outlet end of the separator. The indirect cooler is connected with a shell side circulating water pump that is connected with the outlet end of the separator through an absorption tower, where an inlet end of a static focus follower is connected with an air storage tank.    USE - Large biomass gasification, destructive distillation gas engineering purification system for use in a gas station.    ADVANTAGE - The purification system solves the circulation water secondary pollution problem, improves the purifying efficiency, controls gas coke and dust content to be below 10 milligram per cubic meter, avoids trouble during changing of a filter, reduces operation cost, capable of realizing large scale gasification or carbonization and increases safety and stability of the gas station.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a large biomass gasification, destructive distillation gas engineering purification system.
NOVELTY - Method for producing bio-oil, involves inoculating Rhodobacter sphaeroides into a culture medium comprising carbon source chosen from acetic acid, butyric acid, lactic acid, maleic acid and succinic acid, and ammonium sulfate as nitrogen source, and culturing the R.sphaeroides in the presence of light under aerobic or anaerobic conditions.    USE - The method is useful for producing bio-oil for producing biodiesel (claimed).    ADVANTAGE - The method produces bio-oil with high quality and increased fatty acid content including vaccenic acid, stearic acid and palmitic acid.
NOVELTY - Method (M1) for preparing complex microorganisms culture medium, involves mixing brown sugar, Salicornia herbacea, cornstalk, wheat bran, sawdust, rice hulls, rice straw, starch, seaweeds, and fish product, fermenting the obtained product and irradiating the obtained product.    USE - The method (M1) is useful for preparing complex microorganism's culture medium which is useful for culturing microorganisms used in agricultural fertilizer (claimed).    ADVANTAGE - The complex microorganisms culture medium is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for preparing molasses replacement medium, which involves using the complex microorganism's culture.
NOVELTY - Hydrocarbon processing comprises: providing a fluid hydrocarbon feedstock comprising an oxygenate; contacting the feedstock with a catalyst comprising platinum loaded tungsten oxide/zirconium dioxide in the presence of hydrogen; and reacting the feedstock, hydrogen and catalyst at a temperature and a pressure for a period of time sufficient to allow both hydrodeoxygenation and hydrocarbon isomerization of the oxygenate.    USE - The method is useful for hydrocarbon processing, preferably hydrodeoxygenation and hydrocarbon isomerization of alditol (all claimed).    ADVANTAGE - The method: utilizes the catalyst which is substantially free of sulfide so it does not require a Claus unit; is a one-step hydrodeoxygenation and isomerization process; does not require continuous injection of a sulfiding agent to maintain catalytic activity; and is simpler and cheaper method for reforming and upgrading biomass-derived oxygenates and eliminates the separate upgrading and reforming steps, thus it saves time, money, effort and energy compared to previous methods.
NOVELTY - A fuel pellet manufacturing method involves utilizing (in wt.%) timber. Sawdust with moisture content (20-25) is mixed with rice bran to obtain expanded sawdust. The expanded sawdust is extruded and cooled to obtain expanded sawdust pellet. The sawdust pellet is maintained by injecting vapor at 100-200 degrees C. The pellet is extruded and mixed with rice bran and sawdust having moisture content (20-40). An expanded sawdust pellet and pellet powder generated in the extrusion process are separated. The pellet powder is cooled and extruded through a device to obtain fuel pellet.    USE - Method for manufacturing fuel pellet.    ADVANTAGE - The method enables manufacturing fuel pellet with improved effectiveness and better stability in an inexpensive and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for manufacturing fuel pellet.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing fuel pellet.'(Drawing includes non-English language text)'
NOVELTY - A sewage sludge carbonized adsorbent preparation method involves drying sewage sludge in an oven at 100 degrees C for 1 hour, and plasticizing the sludge in a kiln at 550 degrees C, followed by heating at 700 degrees C under nitrogen atmosphere for 2 hours and subjecting to carbonization in steam activating device at 800 degrees C for 1 hour to get sewage sludge carbonized adsorbent.    USE - Method for preparing sewage sludge carbonized adsorbent.    ADVANTAGE - The method enables preparing sewage sludge carbonized adsorbent in a non-odorable manner due to carbonization.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for preparing sewage sludge carbonized adsorbent.'(Drawing includes non-English language text)'
NOVELTY - The complex has service module for producing hydrogen and oxygen gases from water in a chamber during heating the water by an electric heater. A sensor detects temperature of overheated vapor, and is connected to a side of regulator, where the regulator regulates the hydrogen and oxygen gases in the chamber. A micro-controller is connected with the chamber, where the micro-controller is connected to a generating device for generating high voltage. The generating device is connected with a main distributive electrical panel.    USE - Mobile complex for utilizing biomass of a burnt wood.
NOVELTY - Preparation of bromhexine hydrochloride comprises reacting acetic anhydride and boric acid to produce triethyl borate; reacting 2-amino-3,5-dibromobenzyl alcohol and triethyl borate to generate 2-amino-3,5-dibromobenzyl alcohol boron chelate; reacting 2-amino-3,5-dibromobenzyl alcohol boron chelate with N-methylcyclohexyl amine to generate N-(2-amino-3,5-dibromobenzyl)-N-methylcyclohexyl amine (i.e. bromhexine base); reacting base with hydrogen chloride to generate bromhexine hydrochloride coarse product; and refining coarse product to obtain refined product of bromhexine hydrochloride.    USE - Preparation of bromhexine hydrochloride used for patients with bronchitis and respiratory diseases, particularly patients having hard to cough out sputum.    ADVANTAGE - The method has simple technique, mild reaction condition, high reaction quality, convenient operation, high yield, stable, low cost, and environment-friendly.
NOVELTY - The device has a body whose base is coaxially provided with chambers. Positive grids are provided with slots. Transmitters are arranged tangential to an exhaust part of a side wall. A cylindrical part is equipped with a closing flap. Openings are formed in a chamber to discharge dry biomass to an outlet of a reservoir. The chamber is arranged in a conical top part and provided with a sluice. A conical portion is located above a divider. A splitter is moved by an actuator through a slider in contact with a guide. Actuators are driven by tendons. The chamber is provided with a rack.    USE - Biomass torrefaction device.
NOVELTY - The device has a closed tank comprising a heating element. A discharge nozzle discharges biofuel and glycerol. A socket connects a vacuum line to a vacuum pump. A nozzle gas flow line supplies inert gas from a reservoir to a main reactor tank. The main reactor tank is equipped with a heater that is located in a space occupied by a mixture of raw materials and catalysts. An upper part of the main reactor tank is connected with a pump via a line.    USE - Biofuel producing device.
NOVELTY - The method involves feeding 10 to 20 percent of sewage sludge and 80 to 90 percent of distillery waste into an anaerobic reactor for producing biogas.    USE - Method for producing biogas from sewage sludge by a methane fermentation process.
NOVELTY - Preparing 2,3-dihydro-thieno(3,4-b)(1,4)dioxine-5,7-dicarboxylic acid dimethyl ester comprises adding 3,4-dihydroxy-thiophene-2,5-dicarboxylic acid dimethyl ester and ethylene glycol into a reactor under protection of nitrogen, feeding aluminum-phosphorus-titanium-silicon-oxygen as a catalyst at 0.1-2 ml/hour, and reacting the mixture at 250-500 degrees C to obtain product. A mass ratio of 3,4-dihydroxy-thiophene-2,5-dicarboxylic acid dimethyl ester to ethylene glycol is 1:1-1:20. A granularity of the catalyst is 20-80 meshes. The reactor is normal pressure fixed bed reactor.    USE - The method is useful for preparing 2,3-dihydro-thieno(3,4-b)(1,4)dioxine-5,7-dicarboxylic acid dimethyl ester (claimed).    ADVANTAGE - The method is capable of simply, rapidly and economically preparing the 2,3-dihydro-thieno(3,4-b)(1,4)dioxine-5,7-dicarboxylic acid dimethyl ester in an environmentally friendly manner.
NOVELTY - The reactor has a tank arranged with a cover. Surfaces of the tank and the cover are covered with a thermal insulation layer and a vertical drive. The cover of the tank is arranged with an open channel utilized to feed organic material. A shaft is arranged with a screw and connected to two rolls of a rotating cage. An ultrasonic generator is arranged with the rotating cage, where the rotating cage rotates around the axis of the tank in the range of 0.2 to 6 rpm.    USE - Reactor for use during methane fermentation process.
NOVELTY - Biological diesel oil raw material pre-processing device comprises a raw material storage tank, an additive storage tank, a reaction kettle, a sedimentation tank, a three-way valve, a decoloring tank and an air compressor. The upper part of the raw material storage tank and the additive storage tank are connected with the reaction kettle through a pipeline. The reaction kettle is provided with a stirrer, a heater and a thermometer. The outlet of the reaction kettle is connected with the inlet of the sedimentation tank. The outlet of the sedimentation tank is connected with a sewage outlet.    USE - Used as a biological diesel oil raw material pre-processing device.    ADVANTAGE - The device can achieve pre-processing of bio-diesel raw material, and provides quality assurance of the raw material source for the bio-diesel industry.    DETAILED DESCRIPTION - Biological diesel oil raw material pre-processing device comprises a raw material storage tank, an additive storage tank, a reaction kettle, a sedimentation tank, a three-way valve, a decoloring tank and an air compressor. The upper part of the raw material storage tank and the additive storage tank are connected with the reaction kettle through a pipeline. The reaction kettle is provided with a stirrer, a heater and a thermometer. The outlet of the reaction kettle is connected with the inlet of the sedimentation tank through the pipeline. The outlet of the sedimentation tank is connected with a sewage outlet and the three-way valve inlet through the pipeline. The three-way valve is connected with the reaction kettle through the pipeline. The second outlet of the three-way valve is connected with the first inlet of the decoloring tank through the pipe. The second inlet of the decoloring tank is connected with the outlet of the air compressor through the pipeline.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the biological diesel oil raw material pre-processing device.
NOVELTY - Separation and purification of chitosan comprises pre-processing Aspergillus niger zymotic fluid to obtain Aspergillus niger mycelium powder, soaking in sodium hydroxide-ethanol mixture at room temperature with ultrasonic extract solution, neutralizing, processing acid extraction and neutralization sedimentation, and vacuum drying to obtain chitosan.    USE - Method of separation and purification of chitosan (claimed) used in medicine, food, agriculture, feed additive and environmental protection field.    ADVANTAGE - The chitosan separated and purified has purity of more than 98%, deacetylation of more than 90%, and the yield of the product of more than 16%.
NOVELTY - Improving efficiency of degrading lignocelluloses comprises washing lignocellulose after processing buffer solution of actual cellulose, supplementing water to 40 g, and adjusting pH to 4.5-5.5; adding Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate) or polyethylene glycol (PEG)-6000 and bovine serum, albumin and reducing invalid lignin absorbed in cellulase; adding sodium thiosulfate and beta -glucosidase, xylanase, pectin enzyme, and cellulase; and performing enzymolysis, where lignocellulose is wheat straw, corn straw, sorghum straw, reed, straw, wooden meal or bamboo powder.    USE - Method for improving efficiency of degrading lignocelluloses (claimed).    ADVANTAGE - The method solves problem that the traditional enzymolysis technique has low enzymolysis efficiency, low sugar, cellulose and high glucose conversion. Wood enzymolysis is improved by 46%.    DETAILED DESCRIPTION - Improving efficiency of degrading lignocelluloses comprises: (A) washing lignocellulose after processing buffer solution of actual cellulose, where adding amount is 1-6% of total system, buffer solution is 4.5 citric acid or sodium citrate buffer solution, and pH is 5.5, supplementing water to 40 g, and adjusting pH to 4.5-5.5; (B) adding Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate) (0.025-500%) (v/w) or polyethylene glycol (PEG)-6000 (0.010-300%) (w/w), and bovine serum albumin (0.010-200%) and reducing invalid lignin absorbed in cellulase; (C) after 1-2 hours, adding (per 1 g of cellulose) sodium thiosulfate (0.025-0.500%) (w/w), and adding beta -glucosidase (0.5-500 international units (IU)), xylanase (5-100 IU), pectin enzyme (0.010-2 IU), and cellulase (1-100 FPU); and (D) performing enzymolysis at 45-55 degrees C, where lignocellulose is selected from wheat straw, corn straw, sorghum straw, reed, straw, wooden meal or bamboo powder.
NOVELTY - A S-3-hydroxy tetrahydrofuran is produced by mixing S-4-chloro-3-hydroxy-butyric acid ethyl ester, an alkylating agent, a solvent and a catalyst; adding metal borohydride and reducing agent to the obtained product; reacting; adding reagent and solvent to the obtained product; and subjecting mixture to alkylation reaction in the presence of an alkali.    USE - Method of producing S-3-hydroxy tetrahydrofuran.    ADVANTAGE - The method is simple and environment-friendly, has high yield, produces product having high purity, and can be applied to industrial production.
NOVELTY - Preparation of halo ethoxy acetic acid and its ester (I) comprises taking 2-(2-haloethoxy) ethanol as raw material; oxidizing in the presence of first catalyst and oxidant at 10-50 degrees C to prepare 2-(2-halo ethoxy)acetic acid; and esterifying 2-(2-haloethoxy)acetic acid with target alcohol of target ester in the presence of second catalyst to obtain 2-(2-halo ethoxy)acetate.    USE - Preparation of halo ethoxy acetic acid and its ester (I).    ADVANTAGE - The method uses one-pot process for performing two-step reaction, thus simplifying operation. It is safe, environment friendly, and provides high yield.    DETAILED DESCRIPTION - Preparation of halo ethoxy acetic acid and its ester of formula (X-CH2-CH2-O-CH2C(=O)-OR) (I) comprises taking 2-(2-haloethoxy)ethanol as raw material; oxidizing in the presence of first catalyst and oxidant at 10-50 degrees C to prepare 2-(2-halo ethoxy)acetic acid; and esterifying 2-(2-haloethoxy)acetic acid with target alcohol of target ester in the presence of second catalyst to obtain 2-(2-halo ethoxy)acetate. The first catalyst is selected from 2,2,6,6-(tetramethylpiperidin-1-yl)oxyl substances. The oxidizer is perhalite, halite, subhalite or hypohalite. The seconds catalyst is selected from concentrated sulfuric acid, hydrochloric acid, thionyl chloride or 001x 4 type resin. The alcohol is selected from methanol, ethanol, n-propanol, 2-propanol, n-butanol, 2-butanol, 2-methyl-1-propanol, or tert-butanol.    X=F, Cl, Br, or I; and    R=H, Me, Et, n-propyl, 2-propyl, n-butanol, 2-butyl, 2-methyl-1-propyl, or tert-butyl.    Provided that when R is H, esterifying step is not performed.
NOVELTY - A 6.6-dimethyl-3-oxa-bicyclo(3.1.0)ethane-2.4-diketone is synthesized by adding a phase transfer catalyst into water, adding ethyl chrysanthemumate, mixing, adding potassium permanganate, oxidizing the mixture, adding an acid medium and sodium pyrosulfite, subjecting to reducing reaction, dewatering; and closing loop in acetic anhydride.    USE - Method of synthesizing 6.6-dimethyl-3-oxa-bicyclo(3.1.0)ethane-2.4-diketone.    ADVANTAGE - The method is simple to operate and environment-friendly, reduces solvent consumption thus reducing synthesis cost, reduces acid consumption, and has high yield.
NOVELTY - Synthesis of aromatic amine and aromatic methanol comprises synthesizing with aromatic aldehyde having amine or formamide at mol ratio of 5:1-1:5 for 0.5-5 hours at 20-100 degrees C, and synthesizing aromatic amine and aromatic methanol in synthesizing reactor and in water or organic solvent with presence of inorganic or organic base.    USE - Method for synthesizing aromatic amine and aromatic methanol (claimed) used for medicament, pesticide, spice and dye industries.    ADVANTAGE - The method is simple, temperate condition, produces high yield, and environment-friendly.    DETAILED DESCRIPTION - Synthesis of aromatic amine and aromatic methanol comprises synthesizing with aromatic aldehyde of formula Ar'-C(=O)-H having amine or formamide of formula R1-N(R2)-R3 at mol ratio of 5:1-1:5 for 0.5-5 hours at 20-100 degrees C, and synthesizing aromatic amine of formula Ar'C(=O)-N(R1)-R2 and aromatic methanol of formula Ar'-CH2OH in synthesizing reactor and in water or organic solvent with presence of inorganic or organic base.    Ar'=aryl or styryl (both optionally substituted by F, Cl, Br, Me, Et, Pr, i-Pr, t-Bu, chloromethyl, OH, nitro, hydroxymethyl, hydroxyethyl or dimethylamino), where aryl is phenyl, pyridinyl, furanyl, pyridinyl or thiophenyl (sic);    R1, R2=Me, Et, i-Pr and t-Br, alkyl, less than or equal to 8C aryl, H, or 5-6 ring amine including tetrahydropyrrole, hexahydropyridines, tetrahydro imidazole, oxazole alkanol, 1,4-oxygen and nitrogen miscellaneous cyclohexane or piperazine;and    R3=H or formoxyl.
NOVELTY - Preparing N,N-disubstituted sulfonamide compound (I) comprises mixing sulfonamide compound (III) with ether compound (II); reacting for 1-48 hours at 30-200 degrees C in solvent with the protonic acid catalyst; and after reaction, carrying out post-processing for reaction liquid to obtain the compound (I).    USE - Method for preparing N,N-disubstituted sulfonamide compound (claimed) for synthesizing a medical intermediate, agricultural chemical and chemical products.    ADVANTAGE - The method has mild reaction condition, convenient operation and high yield, and uses protonic acid which is environment-friendly as catalyst.    DETAILED DESCRIPTION - Preparing N,N-disubstituted sulfonamide compound of formula R1-SO2-N(R2)(R3) (I) comprises:    (A) mixing sulfonamide compound of formula R1-SO2-NH2 (III) with ether compound of formula R2OR3 (II);    (B) reacting for 1-48 hours at 30-200 degrees C in solvent with the protonic acid catalyst; and    (C) after reaction, carrying out post-processing for reaction liquid to obtain the compound (I).    The protonic acid catalyst is trifluoromethanesulfonic acid, sulfuric acid, trifluoroacetic acid, p-toluenesulfonic acid or methanesulfonic acid. Where R2, R3 and O in compound (II) are connected to ring to form furan, pyran, morpholine or 2-methyl tetrahydrofuran; and R2, R3 and N in compound (I) are connected to ring to form pyrrolidine, hexahydropyridine, piperazine or 2-methyl tetrahydrofuran.    R1=Me, Ph, para-methyl phenyl, parachlorobenzyl, parabromo phenyl, para-amino phenyl or para-iodo phenyl; and    R2, R3=Ph.
NOVELTY - Sulfonamide chalcone derivatives are new class of compounds having antioxidant, antihypertensive, antiallergic, antimalarial, antileishmanial, antiinflammatory, insecticidal, antimicrobial and antitubercular activity and effectively inhibit glucosidase which is the major targets in the treatment of type 2 diabetes and HIV infection. Novel sulfonamide chalcone derivatives prepared by easy and simple greener method is disclosed. The obtained sulfonamide chalcone derivatives are tested for antifungal activity against Aspergillus niger (MTCC 1789), Trichoderma viride (MTCC 167), Penicillium chrysogenum (MTCC 160), Aspergillus flavus (MTCC 2510), Candida albicans (MTCC 183) and Fusarium moniliforme (MTCC 156). Results showed that the compound exhibit antifungal activity. Image 0/0
NOVELTY - Disclosed is an improved cost-effective process for preparing simvastatin from lovastatin using environmentally-friendly reagents resulting in pharmaceutically acceptable grade simvastatin. Preferably disclosed is route of synthesis from lovastatin to lovastatin cyclohexylamine phenylboronate and then to simvastatin, where the deprotection of simvastatin cyclohexylamine is carried out using oxidizing agent which decomposes into water, and resulting into cost-effective synthesis of simvastatin. Image 0/0
NOVELTY - A single-section pressure swing adsorption and carbon rich gas recycling device has a feed gas unit, a pressure swing adsorption unit, a product gas unit, a discharging unit and an analyzing unit that are connected together through a pipeline.    USE - Single-section pressure swing adsorption and carbon rich gas recycling device.    ADVANTAGE - The device enables absorption of hydrogen with high concentration and synthetic purge gas with high purity as product gas at same time, and enables desorption process of high purity carbon-enriched gas from methanol, which is returned to a methanol system. The device discharges fuel gas with low-concentration to an air exchange fuel pipe network as fuel gas by carrying out adsorption process, average pressure reducing process, replacing process, vacuumizing process, pressure lifting process and final punching process in a sequence manner. The device improves total yield of product recovering hydrogen, so that hydrogen recovery rate can be improved, and carbon rich gas with high purity can be obtained as desorbed gas at same time. The device requires less investment and small floor area, and has excellent economic benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a single-section pressure swing adsorption and carbon rich gas recycling device.'(Drawing includes non-English language text)'
NOVELTY - Making biofuels, comprises: dewatering intact algal cells to make algal biomass; extracting neutral lipids from algal biomass; esterifying neutral lipids with a catalyst in presence of an alcohol; separating water soluble fraction comprising glycerin from water insoluble fraction comprising fuel esters; distilling fuel esters under vacuum to obtain a 16C or shorter fuel esters fraction, a 16C or longer fuel ester fraction, and residue comprising carotenoids and omega -3 fatty acids; and hydrogenating and deoxygenating at least one of the 16C or shorter fuel esters and 16C or longer fuel esters.    USE - The method is useful for making biofuels.    ADVANTAGE - The method: recycles the residue comprising carotenoids and omega -3 fatty acids into an animal feed, a human food or a nutraceutical product; requires less energy; and involves the step of heating the biomass at a temperature below the boiling point of solvent, thus generating enough vapors to enhance the extraction, reducing expense, and increasing the effectiveness of the extraction.    DETAILED DESCRIPTION - Making biofuels, comprises: dewatering intact algal cells to make an algal biomass; extracting neutral lipids from the algal biomass; esterifying the neutral lipids with a catalyst in the presence of an alcohol; separating a water soluble fraction comprising glycerin from a water insoluble fraction comprising fuel esters; distilling the fuel esters under vacuum to obtain a 16C or shorter fuel esters fraction, a 16C or longer fuel ester fraction, and a residue comprising carotenoids and omega -3 fatty acids; and hydrogenating and deoxygenating at least one of the 16C or shorter fuel esters to obtain a jet fuel blend stock and the 16C or longer fuel esters to obtain a diesel blend stock.
NOVELTY - Catalytic thermolysis of cellulosic biomass, comprises heating the cellulosic biomass to a conversion temperature in presence of a catalyst system comprising a mixed metal oxide (I).    USE - The process is useful for catalytic thermolysis of cellulosic biomass (claimed) to produce a fuel, feedstock, specialty chemical, valuable liquid products including jet fuels, diesel and heating oil, and valuable gases including ethane, propane and butane.    ADVANTAGE - The process utilizes catalysts which lead to an increase in the yield of organic compounds and a reduction of the yield of undesirable products such as coke, tar and unconverted biomass.    DETAILED DESCRIPTION - Catalytic thermolysis of cellulosic biomass, comprises heating the cellulosic biomass to a conversion temperature in presence of a catalyst system comprising a mixed metal oxide of formula (X1O)(X2O)a(X3Y1bO4) (I).    X1-X3 = alkaline earth elements comprising Mg, Ca, Be and/or Ba;    Y1 = Al, Mn, Fe, Co, Ni, Cr, Ga, B, La, P, Ti and/or Zn;    a = 0 or 1; and    b = 0-2.
NOVELTY - The method involves char producing a solid heat carrier during pyrolysis process, where the solid heat carrier is of desired size and shape or density. The solid heat carrier is heated to appropriate temperature useful for pyrolysis of pyrolyzable material using microwave, infrared, hot fluid, air and electric heater. The solid heat carrier is introduced to a main reactor tube (MRT) shell (310) of a MRT (80) in which the pyrolyzable material and the solid heat carrier are mixed in proportion to cause pyrolysis of the pyrolyzable material.    USE - Method for supplying heat for auger pyrolysis process in an MRT shell to produce a liquid product i.e. pyrolysis oil or bio-oil, by a solid heat carrier.    ADVANTAGE - The method enables a feeding device to effectively deliver feedstock to the MRT. The method enables the carrier to maintain the shape and to effectively transfer heat to a feedstock, thus reaching pyrolysis temperature. The method enables vapor residence time to be varied less than 0.2 second for effective fast pyrolysis and vapors to be drawn from the MRT at port locations. The method enables ports to allow the vapors to be drawn from the MRT for transmission to a condenser train by a shortest path in shortest possible time, thus reducing vapor residence time to enhance bio-oil quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a MRT with a MRT auger and an internal auger.    MRTs (80, 340)    MRT auger (100)    MRT Shell (310)    Hollow shaft (320)    Internal auger (330)
NOVELTY - A gasification, pyrolysis, synthesis and/or related chemical process arrangement consists of a gasifier reactor arranged such that process energy is provided by renewable energy, particularly solar energy, and/or arranged directly in focal point of parabolic reflectors or parabolic troughs.    USE - Arrangement for gasification, pyrolysis, synthesis and/or related chemical processes of carbon (compounds) e.g. timber, coal, oil sand, bioresidual substance, and contaminated residual substance, and/or other chemicals to convert to higher energy chemicals (all claimed).    ADVANTAGE - The arrangement is compact and economical, and enhances yield of synthesis gas and other chemical products.
NOVELTY - A manganese peroxidase variant comprising (a) wild-type manganese peroxidase amino acid sequence in which amino acids at positions 230-250 are substituted such that the amino acids have more hydrophobicity than the wild-type sequence, or (b) a 359 amino acid sequence (SEQ ID NO: 1) fully defined in the specification or amino acid sequence of SEQ ID NO: 1 in which one or more amino acids are deleted, substituted or added.    USE - The manganese peroxidase variant is useful for pre-processing lignocellulosic biomass and isolating lignin from lignocellulosic biomass (claimed) e.g. wood, rice straw, bagasse, bamboo and pulp, and producing bioethanol.    ADVANTAGE - The manganese peroxidase variant has excellent heat resistance and hydrogen peroxide proof property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) recombinant protein comprising the above amino acid sequence of SEQ ID NO: 1 or amino acid sequence of SEQ ID NO: 1 in which one or more amino acids are deleted, substituted or added;    (2) gene encoding the above recombinant protein;    (3) recombinant vector comprising the above gene;    (4) transformant comprising the above recombinant vector; and    (5) method for pre-processing lignocellulosic biomass, involves adding manganese peroxidase variant or recombinant protein to lignin peroxidase.
NOVELTY - A hydrogen storage alloy is rare earth-magnesium-nickel group alloy containing mixed phase of A2B4 subunit and AB5 subunit.    USE - Hydrogen storage alloy is used for negative electrode element of alkaline storage battery (claimed) e.g. nickel hydride storage battery used as power supply for hybrid electric vehicles.    ADVANTAGE - The negative electrode element containing hydrogen storage alloy provides alkaline storage battery with high capacitance, durability, and charging and discharging characteristics.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of storage battery.    Alkaline storage battery (10)    Container (12)    Negative electrode (14)    Reference pole (16)    Positive electrode (18)
NOVELTY - A rural sewage comprehensive use treatment system comprises a biological anaerobic tank (1) and a biological wetland (2), and marsh gas pool (3) and sewer. The biogas slurry and the domestic sewage in the marsh gas pool enter into the anaerobic tank. The artificial wetland biological anaerobic pool is connected, and the sewage in the anaerobic pool enters into the artificial wetland.    USE - A rural sewage comprehensive use treatment system.    ADVANTAGE - The system can solve the problems that the rural sewage treatment has high investment, complex process, high cost and low processing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the rural sewage comprehensive use treatment system.    Biological anaerobic tank (1)    Biological wetland (2)    Marsh gas pool (3)    Methane collecting pipe (4)    Marsh gas purifying device (5)
NOVELTY - Application of zephyr lily in purifying livestock breeding marsh liquid, where it is in the environment for methane liquid pollution poultry carcass planting shallot.    USE - Application of zephyr lily purifying livestock breeding marsh liquid.    ADVANTAGE - The livestock breeding of marsh liquid pollution environment is planted with shallot and the shallot fully uses flange to absorb the ammonia-nitrogen, total nitrogen, total phosphorus, chemical oxygen demand determined by potassium dichromate method and pollution and the tenacious zephyr lily in livestock breeding biogas liquid can be directly planted and it does not need special management and the characters to solve the problem of the livestock breeding biogas liquid pollution. The application has little investment, low operating cost and good effect, has simple and easy operation, ensures the purifying effect at the same time and avoids secondary pollution. The harvested zephyr lily has a certain medical value and can be used for treating infantile convulsion air and vitiligo. The method provides environment protection and landscape construction, and combines economic construction. The ecological restoration, landscape construction and economic benefit are realized.
NOVELTY - Application of Dieffenbachia for purifying poultry breeding biogas liquid, where the environment for methane liquid pollution poultry carcass is used for planting flower leaf evergreen.    USE - Application of Dieffenbachia for purifying poultry breeding biogas liquid.    ADVANTAGE - The poultry breeding marsh liquid pollution environment is planted with flower leaf evergreen and it fully uses flower leaf evergreen for livestock breeding biogas liquid of ammonia ion-nitrogen, total nitrogen, total phosphorus, chemical oxygen demand determined by potassium dichromate method, and pollution material to absorb and flower leaf evergreen tenacious vitality and can be directly planted and it does not need special management. The application has little investment, low operating cost and simple and easy operation, and can ensure the artificial wetland system in purifying effect. The flower leaf harvesting evergreen can be used for treating traumatic injury, golden injury, sudden strain or contusion of a muscle strain, erysipelas, and carbuncle. The application uses flower leaf evergreen processing wastewater, thus realizing environmental protection and landscape construction and economic construction are combined. Sewage treatment and ecological restoration and landscape construction and economic benefit are also realized.
NOVELTY - Preparation of a particle fuel and charcoal comprises crushing a waste fungus culture medium, extruding in an extruding device at 5-100 tons, and molding; and crushing at 100-130 tons for 5-10 seconds under extrusion forming, extruding to obtain an extrusion blank, and placing the extruding blank in a carbonization furnace at 400-600 degrees C and a vacuum degree of 1x 10-1-1x 10-2 MPa.    USE - Method for the preparation of a particle fuel and charcoal (claimed).    ADVANTAGE - The method is environment-friendly, and is inexpensive.
NOVELTY - The method involves conducting a high pressure gaseous stream rich in carbon-di-oxide through an adsorbent bed to remove hydrocarbons from the bed. A purged adsorbent bed is subjected to multiple successive blow-down steps, where pressure of the bed is reduced by a predetermined amount with each successive blow-down step. The adsorbent bed is subjected to successive equalization steps, where the pressure of the bed is increased by the predetermined amount with each successive step. The adsorbent bed is re-pressurized to feed pressure using feed.    USE - Cyclical swing adsorption method for removing contaminant e.g. carbon-di-oxide (claimed), from natural gas stream or gaseous feed stream. Can also be used for removing nitrogen, water, mercury, mercaptan, acid gas i.e. hydrogen sulfide, benzene, toluene, ethylbenzene and xylenes, carbonyl sulfide and hydrogen disulfide.    ADVANTAGE - The method enables re-pressurizing the adsorbent bed to the feed pressure using feed so as to remove the contaminants from the feed streams at high pressure. The method enables preventing fouling of a cryogenic heat exchanger by solid carbon-di-oxide when a purified product is converted to liquefied natural gas. The method enables synchronization requirements between the adsorbent beds to be relaxed, so that transfer of the gas between adsorbent vessels is eliminated due to use of equalization vessels. The method enables small volume of adsorbent and the vessels in a rapid-cycle pressure swing adsorption (RC-PSA) system enabling various purges conducted so as to improve recovery and product purity. The method enables a cycle time to be reduced so as to improve productivity of the RC-PSA system.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph representing a pressure versus time relationship for RC-PSA cycles.
NOVELTY - Integrated process for the production of bio-oil from sludge coming from a wastewater purification plant, comprises: (a) sending wastewater to the purification plant obtaining sludge; (b) subjecting the sludge to liquefaction obtaining a mixture comprising an oily phase consisting of bio-oil, a solid phase and an aqueous phase; and (c) sending the aqueous phase to the purification plant.    USE - The process is useful for the production of bio-oil from sludge coming from a wastewater purification plant, where the bio-oil for the production of biofuels, which is useful: in automotive fuels, combustible oil and coal; and for electric energy generation.    ADVANTAGE - The process: is efficient and simple management of the aqueous phase obtained from sludge liquefaction, directly in the civil and/or industrial wastewater purification plant, with no need to subject the aqueous phase to further treatments, with consequent reduction of both overall investment and operating costs; minimizes the amount of solid waste obtained in the wastewater purification process; is possible exploitation of the solid phase obtained from the liquefaction for the production of heat and/or electric energy which can be used to energetically supply the process with resulting energy savings; and increases bio-oil yield and zero setting of the disposal costs of the oils and/or fats.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bio-oil obtained through the integrated process.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of purification plant to implement the integrated process for the production of bio-oil from sludge.
NOVELTY - The sterilization composition comprises picoxystrobin, cymoxanil, auxiliary agent and filler. A mass ratio of picoxystrobin and cymoxanil is 1:10-10:1.    USE - The sterilization composition is useful for preventing and treating disease on a gramineous crop and a Cruciferae vegetable, where the disease includes leaf blight, leaf rust, glume blight, tan disease, leaf spot, powdery mildew, net blotch, blotch, frosty mildew, blight disease, gray mold and anthracnose (all claimed).    ADVANTAGE - The sterilization composition can be econo0mically produced with improved drug resistance and without environmental pollution.
NOVELTY - Use of 5-15C-alkanol (I) for improving the defoaming effect of a silicon containing antifoaming agents in fuel oils, which contain at least one additive having a detergent effect, is claimed.    USE - (I) is useful for improving the defoaming effect of silicon containing antifoaming agents in fuel oils.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an additive concentrate comprising (a) 0.1-10 wt.% of (I), (b) 0.5-80 wt.% of at least one aryl hydrocarbon or hydrocarbon mixture having a boiling point or a predominant boiling range of 100-250 degrees C and/or at least one 5-12C-alkylnitrate, where the amount of (b) is at least five times the amount (I), (c) 0.01-2 wt.% of the silicon containing anitfoaming agent, (d) 1-30 wt.% of the additive with detergent effect and (e) 0-5 wt.% of at least a commercial dehazer, where the sum of (a) to (e) is 100 wt.% with the proviso that the additive concentrate additionally meets at least one of the following criteria: the amount of (d) is at least ten times the amount of (c) and the amount of (a) is at least three times the amount of (c); and    (2) additized fuel oil comprising a major amount of base-fuel oil containing 0.1-100 wt.% of at least one biofuel oil based on fatty acid ester and 0-99.9 wt.% of average distillates from fossil origin or plant and/or animal origin, preferably hydrocarbon mixture, where the distillate is free of fatty acid esters, and a small amount of the additive concentrate.
NOVELTY - The temozolomide pharmaceutical composition comprises 5-20% of temozolomide, 5-30% of a solubilizer, 30-50% of lyophilizing protectants, 5-20% of a first buffering agent, and 5-15% of a second buffering agent.    USE - The temozolomide pharmaceutical composition is useful for treating brain tumor and radiotherapy for lung cancer brain metastasis.    ADVANTAGE - The temozolomide pharmaceutical composition permeates blood-brain barrier and provides brain metastasis objective release rate thus ensuring effective treatment of the patient and prolonging the life span of patient, and can be simply, rapidly and economically prepared with high quality in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing temozolomide pharmaceutical composition.
NOVELTY - The method comprises discharging industrial waste including non-ferrous metal and black metal waste, and crushing the waste by a crusher and then mixing and stirring into organic garbage and city sludge.    USE - The method is useful for manufacturing fertilizer by industrial waste.    ADVANTAGE - The method is capable of simply manufacturing the fertilizer with less energy consumption and without pollution.
NOVELTY - The apparatus has mixing portion that is installed at wet sludge storage to mix dry sludge and wet sludge with certain amount of water. The dry sludge storage is installed at downstream of exhausting unit for storing dry sludge. The dry sludge is pulverized by screening device and is ejected to the return unit. The dry sludge is separated according to the fixed range of the particle size. The transport unit is made to transfer the dry sludge for mixing with wet sludge.    USE - Sludge fuel recycling apparatus.    ADVANTAGE - The sludge can be recycled effectively at low cost, to prepare effective fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge fuel making method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sludge fuel recycling apparatus. (Drawing includes non-English language text)
NOVELTY - The biogas apparatus has a gas channel (19) which connects a methane fermentation tank (11) and gas-engine generators (61-63). A pressure detection apparatus (13) detects pressure of biogas in gas channel. A water sealed valve (25) discharges biogas when pressure of the biogas in the gas channel exceeds constant value. A backflow prevention water tank (26) is provided in gas channel for retaining water which flows backward from the water sealed valve.    USE - Biogas apparatus for generating biogas using organic waste such as foodstuff residue, sewage sludge, organic waste water, garbage, and excrement, used in electric power generation application.    ADVANTAGE - Since the rapid pressure change occurs in the gas channel according to gas suction force generated at the time of drive of gas engine generator, the continuous operation of the gas engine generator is possible even if backward flow water enters in gas channel.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the biogas apparatus.    Methane fermentation tank (11)    Pressure detection apparatus (13)    Gas channel (19)    Water sealed valve (25)    Backflow prevention water tank (26)    Gas-engine generators (61-63)
NOVELTY - The equipment (1) has flow meter (29,31) which measures influent volume in bio-reaction tank (10). An air flow calculation and valve control apparatus (33) and air blower control apparatus ascertain actual condition of process condition of reaction tanks (11-14) based on measured values of ammonia nitrogen meter (15-18). The valve control apparatus separately controls air volume controlling valve of each reaction tank, so that air flow to diffuser corresponding to present nitrification condition between each ammonia nitrogen meter blast pressure force is maintained in constant state.    USE - Activated sludge processing equipment of sewage.    ADVANTAGE - The air flow to each reaction tank can be automatically controlled separately, so that required air quantity according to the process condition for every reaction tank can be separately ventilated without excess and deficiency, and an excessive air flow can be reduced efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation-control apparatus for controlling operation of activated sludge processing equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the activated sludge processing equipment. (Drawing includes non-English language text)    Activated sludge processing equipment (1)    Bio-reaction tank (10)    Reaction tanks (11-14)    Ammonia nitrogen meter (15-18)    Flow meter (29,31)    Air flow calculation and valve control apparatus (33)
NOVELTY - Gas or liquid process body comprises container (2) accommodating molding (1) of treatment material which processes gas or liquid, inflow port (3) where gas or liquid from outside flows in, and outflow port (4). All the opening parts provided in the inflow port and the outflow port are made into a shape that does not allow the molding to pass. The molding has convex curve.    USE - Gas or liquid process body for fuel cell system (claimed).    ADVANTAGE - The container can be filled with large amounts of molding, without considering the position of the opening parts. Processing capacity of the gas or liquid process body is high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional diagram of a fuel generating body. (Drawing includes non-English language text).    Molding (1)    Container (2)    Inflow port (3)    Outflow port (4)
NOVELTY - Method for preparing fertilizer, involves crushing (ST3) raw material containing shellfish as main component, mixing (ST4) wood chip with the crushed material, and fermenting (ST5) the mixture for one month or more, where mixing ratio of the raw material and wood chip is 2:1.    USE - The method is useful for preparing fertilizer.    ADVANTAGE - The method is cost-effective and environmentally-friendly, and does not produce any offensive odor and toxic substances.    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart illustrating method for preparing fertilizer.    Landing process (ST1)    Storage process (ST2)    Crushing process (ST3)    Mixing process (ST4)    Fermentation process (ST5)
NOVELTY - The fuel cell (100) includes an oxidant gas flow channel (50) which is divided into a first flow path (52) and a second flow path (54). The thermal expansion coefficient of the first flow path is made greater than the thermal expansion coefficient of the second flow path.    USE - Fuel cell for generating electric power.    ADVANTAGE - Enables continuation of electric power generation when the operating temperature of the fuel cell becomes high, even if a non-humidification fuel gas is supplied.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional views of a fuel cell. (Drawing includes non-English language text).    Membrane electrode assembly (10)    Oxidant gas flow channel (50)    First flow path (52)    Second flow path (54)    Fuel cell (100)
NOVELTY - Producing self-supporting composite material involves either: i) providing substrate of raw material composed of discrete particles of agricultural byproduct; ii) adding plant oil emulsion to substrate in amount and for a time to inhibit microbial growth on substrate and form mixture; ii) adding inoculum including preselected fungus to the mixture; and iv) allowing fungus to grow hyphae and to allow the hyphae to form network of interconnected mycelia cells through and around discrete particles; hence bonding the particles; or step (i); step (iii); step (iv); and step (ii).    USE - For producing self-supporting composite material (claimed).    ADVANTAGE - The process is disinfection process for raw materials used in producing composite material using fungal tissue; reduces costs of manufacturing composite materials; and reduce time required to produce sterilized composite material using fungal tissue. The emulsion can also be reused number of times without loss of efficacy of the emulsion's disinfection characteristics. The process provides a simple and economical technique for disinfecting bulk materials that can later be inoculated with filamentous fungus for composite materials production or cultivation of food (mushrooms).    DESCRIPTION OF DRAWING(S) - The figure shows schematic of process for producing self-supporting composite material.
NOVELTY - Preparing 5-aminotetrazole, involves: (1) adding inorganic acid in hydrazine hydrate aqueous solution to make most of hydrazine hydrate into salt; (2) adding cyanamide aqueous solution in step 1), reacting with silicate of hydrazine hydrate to produce aminoguanidine salt; (3) adding inorganic acid in reacting solution in step 2) to provide acidity environment, then adding nitrite aqueous solution to diazotize; (4) after diazotizing, quickly adding alkali material in reacting solution to adjust pH 4-6, heating to cyclize, adjusting pH 3.5-4.5, then filtering/washing/separating out crystal.    USE - For preparing 5-aminotetrazole (claimed) used as the propellant and explosive, medicine, herbicide and safety air bag of vehicle for agent, and is suitable for industrial production.    ADVANTAGE - The method is simple, free of hydrazoic acid, little in the environment pollution, obtains product in one pot, and is concise; optimizes and selects the process condition; and provides finished product yield of 86%, and purity of 99.6% detected by the high performance liquid chromatography.
NOVELTY - An organic matrix comprises needle mushroom culture residue, cow dung, and furnace slag at volume ratio of 6:3:1.    USE - Organic matrix used in vegetable production.    ADVANTAGE - The organic matrix can fully utilize needle mushroom residue to increase fertilizer effect and increase organic matter content, thus improving quality and yield of vegetables, and organic nutrients and inorganic nutrients content in vegetable production.
NOVELTY - A coal gas is transformed to obtain transformation gas. The transformation gas is condensed and separated to obtain condensed liquid. The condensed liquid is desulfurized and decarburized to obtain purified transformation gas. The purified transformation gas is subjected to methanation treatment to obtain mixed gas. The mixed gas is cryogenically separated. The hydrogen is combined with nitrogen to obtain synthesis gas with predetermined hydrogen-nitrogen ratio, and the synthesis gas is supplied to synthesis ammonia process to obtain ammonia.    USE - Co-production method of liquefied natural gas and ammonia.    ADVANTAGE - The method enables efficient co-production method of liquefied natural gas and ammonia, without environmental pollution.    DETAILED DESCRIPTION - A coal gas is transformed to obtain transformation gas. The transformation gas is condensed and separated to obtain condensed liquid. The condensed liquid is desulfurized and decarburized to obtain purified transformation gas. The purified transformation gas is subjected to methanation treatment to obtain mixed gas containing hydrogen and methane. The mixed gas is cryogenically separated, to obtain liquefied natural gas and hydrogen. The hydrogen is combined with nitrogen to obtain synthesis gas with predetermined hydrogen-nitrogen ratio, and the synthesis gas is supplied to synthesis ammonia process to obtain ammonia. An INDEPENDENT CLAIM is included for device of co-production process of liquefied natural gas and ammonia, which has gasification unit, airflow bed coal gasification bed, gasification unit, transformation unit, desulphurization/decarburization unit, methanation unit, cryogenic separation unit, nitrogen washing tower, and ammonia synthesis unit.
NOVELTY - Bacillus subtilis (I) under a preservation number of CGMCC No. 5280, is new.    USE - (I) is useful for removing light yellow phosphorus in a sewage in an aerobic condition at low-temperature (8-12 degrees C) (claimed)    ADVANTAGE - (I) is capable of efficiently removing phosphorus in the sewage at low temperature, preferably 8-12 degrees C. (I) improves phosphorus rate by 10% than the standard water level A (the water temperature is 12 degrees C and the control index of the first level A standard is 0.5 mg/l).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing (I).
NOVELTY - A method for converting a hydrocarbon feedstock into methanol, involves: (a) reacting a hydrocarbon feedstock with molecular halogen so as to form alkyl halides; (b) contacting at least a portion of the alkyl halides with an alkali so as to form methanol and a halide salt; and (c) photoelectrocatalytically converting at least a portion of the halide salt into molecular halogen.    USE - For converting hydrocarbon feedstock comprising natural gas or methane derived from a biomass or coal into methanol (Claimed).    ADVANTAGE - The present method combines the thermal (non-electrochemical) reactivity of halogens (preferably bromine) with hydrocarbons to produce hydrogen halide (preferably HBr) and reactive alkyl halides or other carbon-containing intermediates that may be converted to subsequent products, more readily than the original hydrocarbon, with the facile electrolysis of hydrogen halides or halide salts to create an overall process with significantly higher efficiency. The use of halogens prevents the total oxidation of the hydrocarbon to carbon dioxide and allows subsequent production of partial oxidation products. The molecular halogen is recovered by electrolysis using a non-hydrogen producing cathode, e.g., an oxygen depolarized cathode, which significantly reduces the power consumption by producing water instead of hydrogen.
NOVELTY - The electrode has a positive electrode plate (1) comprising 15-30 weight percentage of graphite, 12-35 weight percentage of carbon powder, 20-50 weight percentage of manganese oxide, 9-25 weight percentage of curing agent and a metal net, and a negative electrode plate (2) comprising a rare earth element, 0.5-5.3 weight percentage of bismuth, tin, 0.21-3.2 weight percentage of gallium, 0.6-4.5 weight percentage of magnesium, zinc and 64.30-96.46 weight percentage of aluminum. The carbon powder is chosen from acetylene carbon powder or charcoal carbon powder.    USE - Solid electrode for a self consumption fuel generating device.    DETAILED DESCRIPTION - The curing agent is combination of polyethylene, polyfluortetraethylene or LD0020. The rare earth element is praseodymium, lanthanum or cerium.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solid electrode for a self consumption fuel generating device.    Positive electrode plate (1)    Negative electrode plate (2)
NOVELTY - Sludges are collected, coal is mixed with collected sludge and compressed. The dwelling coal is mixed to the fixed thickness, molded, heated and dried, to obtain substitution fuel.    USE - Manufacture of substitution fuel.    ADVANTAGE - The substitution fuel is efficiently manufactured.
NOVELTY - Preparation of ferrous glycinate involves preparing raw material containing glycine and ferrous sulfate heptahydrate; exposing the raw material in air for a time, an air humidity is ( gamma 70%, time is 214 hours); fully mixing and grinding the materials, grinding to size at 4r/ 200 meshes; placing it for a time for 2-12 hours; and drying the two raw materials at constant temperature of 60 degrees C. The the mol ratio of glycine to ferrous sulfate heptahydrate is 1:1.    USE - The ferrous glycinate is useful in amino acid chelated mineral element.    ADVANTAGE - The process is capable of easily and energy efficiently preparing ferrous glycinate with high yield in an industrial and environmentally friendly manner.
NOVELTY - A biological pesticide comprises (wt.%): abamectin mixture (2-80, preferably 15), ammonium sulfate (0.5-36, preferably 5), monoammonium phosphate (0.5-16, preferably 5), potassium sulfate (2-48, preferably 10), borax (2-10, preferably 4), zinc sulfate (2-15, preferably 8), ferrous sulfate (2-20, preferably 10), calcium powder (2-10, preferably 5), rooting reagent (2-5, preferably 3), chicken manure (2-20, preferably 10), pepper powder (2-45, preferably 10), and peanut cake or castor cake (2-20, preferably 15).    USE - For killing various crop parasitic injurious insects, e.g. nematodes and whitefly.    ADVANTAGE - The biological pesticide promotes growth of the crop and increase the yield, and effectively inhibit growth of the nematode with special effect for whitefly. The present pesticide not only has insecticide efficiency, but also has fertilizer effect with good utility value.
NOVELTY - The system has distillation column (H) to distill oil from storage tank to recover heavy oil, diesel, or petrol by ports (I,J,K). The sludge is transferred to screw press (O) from catalytic decomposition reactor (D) by valve (R). The liquid is re-circulated into reactor by pump (S). The heat generated from incinerator (M) is recovered by heat exchanger (Y) to convert into electrical energy. The gas generated from incinerator is transferred to catalytic oxidation column (L) to decompose into carbon dioxide and water. The residual catalyst is recovered by catalyst recovery unit (N).    USE - System for producing oil from wood composite hydrocarbon, corn stem, coconut tree, palm tree, canola, waste plastic, and organic waste.    ADVANTAGE - The high-quality oil can be obtained with high edibility, without consuming more energy and resources. The contamination of environment can be prevented during oil production.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the oil production system.    Catalytic decomposition reactor (D)    Distillation column (H)    Ports (I,J,K)    Catalytic oxidation column (L)    Incinerator (M)    Catalyst recovery unit (N)    Screw press (O)    Valve (R)    Pump (S)    Heat exchanger (Y)
NOVELTY - Warm water is added to mixed-alum byproduct essentially containing potassium alum and ammonium alum, and dissolved to obtain a solution. Ammonia is added to the resultant solution to obtain aluminum hydroxide precipitate and solution containing potassium sulfate and ammonium sulfate. The aluminum hydroxide precipitate is filtered, washed and dried, to obtain aluminum hydroxide powder. The filtrate is concentrated, cooled, crystallized, obtained crystals are filtered and dried to obtain a mixture of potassium sulfate and ammonium sulfate (fertilizer).    USE - Preparation of nitrogen-potassium compound fertilizer and aluminum hydroxide.    ADVANTAGE - The method economically and efficiently provides nitrogen-potassium compound fertilizer and aluminum hydroxide from mixed-alum byproduct. The method reduces discharge of waste and prevents environmental pollution by recycling the filtrate.    DETAILED DESCRIPTION - Mixed-alum byproduct essentially containing potassium alum and ammonium alum, is obtained during extraction of lithium from lithium ore. Warm water is added to byproduct, dissolved to obtain a solution, and insoluble impurities are filtered. Ammonia is added to the resultant solution to obtain aluminum hydroxide precipitate and solution containing potassium sulfate and ammonium sulfate. The aluminum hydroxide precipitate is filtered from the solution, washed and dried, to obtain aluminum hydroxide powder. The wash liquid is heated and further used to dissolve mixed-alum byproduct. The filtrate remaining after filtration of aluminum hydroxide precipitate, is concentrated, cooled, and crystallized. The obtained crystals are filtered and dried to obtain a mixture of potassium sulfate and ammonium sulfate (fertilizer). The concentrated mother liquor and filtrate are recycled to obtain mixture of potassium sulfate and ammonium sulfate.
NOVELTY - A round-leaved youthwort herb is crushed, added to carbon dioxide supercritical extractor and extracted in presence of ethanol to obtain extract. The extract is added to a polyamide chromatography column in which mixed solvent of dichloromethane and methanol is used as eluent to elute the extract, and a powder is collected on polyamide film. The solvent is recovered, added to macroporous adsorption resin column, eluted by ethanol, eluent is collected, ethanol is recovered and concentrated, acetic acid crystal is added, separated, washed and dried, to obtain droserone.    USE - Method for extracting droserone from round-leaved youthwort.    ADVANTAGE - The method efficiently extracts high purity droserone by simple process, with reduced environmental pollution and energy consumption.    DETAILED DESCRIPTION - A round-leaved youthwort herb is crushed, added to carbon dioxide supercritical extractor, extracted in presence of ethanol as entrainer at 10-30 MPa and 40-50 degrees C for 150-170 minutes, to obtain extract. The flow rate of carbon dioxide is 1-3 ml/g.minute. The content of entrainer is 1-3 vol.% of total extraction solvent. The extract is added to a polyamide chromatography column in which mixed solvent of dichloromethane and methanol in volume ratio of 8:1 is used as eluent to elute the extract, and a powder with Rf value of 4-4.5 is collected on the polyamide film. The solvent is recovered, added to D101 macroporous adsorption resin column, eluted by 30% ethanol, 5 times the amount of column volume of eluent is collected, ethanol is recovered and concentrated under reduced pressure, acetic acid crystal is added, separated, washed and dried, to obtain droserone.
NOVELTY - A biodiesel preparing method involves mixing transition metal sulfate with oil and alcohol.    USE - Method for preparing biodiesel.    ADVANTAGE - The method ensures simple technical flow and biodiesel yield.
NOVELTY - A magnetic solid alkali catalyst preparation method involves mixing magnetic substance raw material and active component raw material with titanium dioxide, and roasting mixture for 3-6 hours at 300-500 degrees C. The mixture is cooled to room temperature, and ground to 120 meshes sieve. The mixture is roasted for 5-12 hours at a temperature of 900-1200 degrees C. The mixture is cooled to room temperature to obtain magnetic solid alkali catalyst, where the magnetic substance raw material is magnetite, hematite, nickel oxide, cobalt oxide and manganese oxide.    USE - Method for preparing magnetic solid alkali catalyst used for synthesizing bio-diesel.    ADVANTAGE - The method enables preparing catalyst with simple preparation process and better catalyzing effect.    DETAILED DESCRIPTION - A magnetic solid alkali catalyst preparation method involves mixing magnetic substance raw material and active component raw material with titanium dioxide, and roasting mixture for 3-6 hours at 300-500 degrees C. The mixture is cooled to room temperature, and ground to 120 meshes sieve. The mixture is roasted for 5-12 hours at a temperature of 900-1200 degrees C. The mixture is cooled to room temperature to obtain magnetic solid alkali catalyst, where the magnetic substance raw material is magnetite, hematite, nickel oxide, cobalt oxide and manganese oxide. The active component is lithium, sodium, potassium, rubidium, cesium, hydroxide, fluoride salt, carbonate, nitrate or acetate, where mass percent of the magnetic substance raw material in the solid alkali catalyst is 27.2-77.5 wt.%, content of active component raw material in the solid alkali catalyst is 15.2-40.1wt.% and content of metal oxide in solid alkali catalyst is 7.3-37.7wt.%.
NOVELTY - The device has a carbon paper electrode that is loaded with hydrogen evolution catalyst and oxygen evolution catalyst. A transparent end plate is provided with a water inlet and a water outlet. A metal end plate and conductive metal screens are connected with cathode of direct current power supply. An anode is connected with end plate. The metal end plate is provided with irradiation light end plate of the light source.    USE - Device for decomposing water to produce hydrogen in photo-electrolysis pond.    ADVANTAGE - The zero distance between the electrodes and the membrane can be ensured. The electrolytic efficiency of the decomposing device can be improved. The energy consumption of the decomposing device can be reduced. The stability of the decomposing device can be improved.
NOVELTY - The compact, containerized, elegant garbage composter which is a feasible decentralized community solid waste management system consists of a shredder which shreds the loaded solid waste and discharges it into a well ventilated composter. The shredded waste entering the composter is blended with a microbial culture, which is a rich and diverse consortium of microbes, brown waste like garden waste and saw dust. The composter vessel is rotated for an hour in a day by a robust geared motor. The system is designed, such that the compost moves gradually forward along the axis as the composting process takes place simultaneously. At the furthest end of the vessel there is a built in circular sieve. The compost gets sieved and drops into a tray kept below the composting drum. The end product is nutrient rich compost. Image 0/0
NOVELTY - Waste leaves obtained from the beedi industry are used for preparation of compost which is prepared using earthworms. The waste leaves of the Diospyros melanoxylon contains high amount of tannin, lignins, naphthoquinones and cellulose which cannot be easily degraded by natural process and takes longer time for degradation by natural process and equally harmful for earthworms. To avoid the problem which arises due to presence of higher concentration of the tannin, lignins, naphthaquinones and cellulose the litter leaves of the Diospyros melanoxylon subjected for the partial decomposition using Aspergillus, Penicillium, Trichoderma, Paecilomyces and Chaetomium over 90 days. Partially decomposed leaves are further subjected to undergo vermicomposting process using earthworms Eudrilus eugeniae for 30 days until the leaves litter is completely degraded and converted into vermicompost with carbon and nitrogen of below 30:1. Disclosed is a vermicompost used for the cultivation of onion in farms which results in cost saving on the manuring and increases crop production, and therefore provides an interesting cost saving tool from the waste leaves of Diospyros melanoxylon. Image 0/0
NOVELTY - The assembly has a housing (1) designed as a stand pipe, where upper and lower front surfaces (2, 3) of the stand pipe stay in free contact with the environment. Catalytic element arrangements (4, 5) are arranged in a lower part of the housing along a height axis of the housing. The housing has a round cross-section in an area equipped with the catalytic element arrangements, where the cross-section decreases successively from one of the arrangements to another arrangement in the direction of gas flow, where the arrangements are shielded by metal meshes.    USE - Passive auto-catalytic recombination assembly for recombination of fire-and explosion endangered hydrogen and oxygen in a hydrogen storage, nuclear waste disposal site and atomic power plant, and during high-temperature corrosion process.    ADVANTAGE - The housing has the round cross-section in the area equipped with the catalytic element arrangements, and the cross-section decreases successively from one of the arrangements to another arrangement in the direction of gas flow, thus increasing efficiency of the hydrogen recombination in the entire surface of catalytic coating, and increasing critical hydrogen concentration through the intensification of the heat discharge from a catalytic converter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a passive auto-catalytic recombination assembly.'(Drawing includes non-English language text)'    Heights of catalytic element arrangements (H-1, H-2)    Housing (1)    Upper front surface of stand pipe (2)    Lower front surface of stand pipe (3)    Catalytic element arrangements (4, 5)
NOVELTY - Primary treatment of organic sewage flowing into household septic tank, involves irradiating the inside of the household septic tank with light through immersion type transparent cylinder, putting microbial material, and maintaining the facultative anaerobic environment in the household septic tank without transferring sludge formed in the septic tank to avoid changes in the treating environment.    USE - The method is useful for primary treatment of organic sewage flowing into household septic tank.    ADVANTAGE - The method prevents formation of scum and emission of offensive smell, controls sedimentation of organic matters flowing into the septic tank, and increases degradation speed of the organic matters and the removal ratio of the organic matters.    DETAILED DESCRIPTION - Method for primary treatment of organic sewage flowing into a household septic tank, involves irradiating the inside of the household septic tank with light through immersion type transparent cylinder, which is provided within the household septic tank, to treat the organic sewage under normal facultative anaerobic conditions, putting a microbial material, where microbial material comprises facultative anaerobes as the main component, into the household septic tank, while irradiating the inside of the household septic tank with light via the immersion type transparent cylinder, and maintaining the facultative anaerobic environment in the household septic tank without transferring sludge formed in the septic tank to avoid changes in the treating environment while irradiating the inside of the household septic tank with light through the immersion type transparent cylinder.
NOVELTY - The enhancing arrangement has a non-isolating pre-regulator (122) which provides part of the fuel cells (103) with voltage and current to facilitate an electrolysis mode of operation producing hydrogen. A feedback arrangement (109) circulates fuel through the anode sides (100) of the cells to supply part of the hydrogen to the cells. The pre-regulator and feedback arrangement release requirements on a heating source (138) by minimizing amount of fuel feed-in and by minimizing amount of internal reforming required to draw current from the fuel cells during start-up of fuel cell device.    USE - Enhancing arrangement for start-up heating of a high temperature fuel cell device.    ADVANTAGE - Cost savings are achieved because smaller and cheaper heating sources are enough to fulfill external heating demands, and the fuel cell system has a more compact size. The arrangement operates as an advanced interactive fuel cell system, and due to the internal circulation of power and hydrogen in the fuel cell circulation loop, the amount of fresh fuel feed required for driving current in the fuel cells is significantly reduced such that the amount of stack cooling by internal reforming can be significantly reduced. This enhances the heating of fuel cells and reduces the need and requirements for external heating source, e.g. electrical heaters, in the start-up process of the fuel cell device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an enhancing method for start-up heating of a high temperature fuel cell device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the enhancing arrangement for start-up heating of a high temperature fuel cell device.    Anode sides (100)    Fuel cells (103)    Feedback arrangement (109)    Non-isolating pre-regulator (122)    Heating source (138)
NOVELTY - Ion-permeable reinforced separator comprises at least one separator element and a substantially hollow by-pass channel contiguous with at least one separator element, where at least one separator element comprises a binder and a metal oxide or hydroxide dispersed in the element, and the separator element has a bubble point of at least 1 bar and a back-wash resistance of at least 1 bar.    USE - The ion-permeable reinforced separator is useful for electrochemical cells associated with a production or consumption of at least one gas. The electrochemical cells are high-pressure electrochemical cells, electrolytic cell including alkaline water electrolysis cell, or fuel cell including alkaline fuel cell (claimed).    ADVANTAGE - The separator reduces cross-contamination of hydrogen and oxygen produced in the electrochemical cells, and is geometrically stable with respect to changes in pressure i.e. it does not collapse or explode. Flow of electrolyte through the integrated hollow by-pass channel removes corrosion products thereby maintaining ionic conductivity of the cell, hence it enables a constant temperature to-be-maintained. The separator elements sufficiently resilient to follow contours of preelectrodes in catholyte anolyte compartments thereby it avoids gas bubbles between surface of the separators and respective pre-electrodes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electrochemical cell comprising above-mentioned separator; and    (2) method for producing hydrogen in an electrolytic cell.
NOVELTY - Use of biodiesel in pesticide microemulsion, is claimed, where the biodiesel is mixed with an organic solvent.    USE - The biodiesel is useful in pesticide microemulsion.    ADVANTAGE - The safe and clean biodiesel is non-toxic, and exhibits strong dissolving capacity, high flash point, good environment protection performance and high viscosity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the pesticide microemulsion with the biodiesel as a solvent.
NOVELTY - A catalyst composition containing alumina, alkaline-earth metal compound, cerium compound and platinum group metal compound is wet-ground, to obtain aqueous slurry. A surfactant is added to the obtained slurry, stirred and foamed, and coated on a honey-comb base material to form porous catalyst layer.    USE - Manufacture of steam reforming catalyst used for manufacturing hydrogen (claimed) used as raw material for fuel cell e.g. polymer electrolyte fuel cell or solid oxide fuel cell for household appliances.    ADVANTAGE - The method provides steam reforming catalyst having excellent durability and sulfur-poisoning proof property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen, which involves reforming hydrocarbon-type compound using steam reforming catalyst.
NOVELTY - A hydrogen-generating apparatus (100) comprises normal-temperature desulfurizer (11) from which sulfur compound in a raw material is removed at normal temperature, a hydrodesulfurization device (12) which removes the sulfur compound in the raw material at temperature higher than normal temperature, and a hydrogen generator (13) which generates hydrogen-containing gas using the raw material. The capacitance of the normal-temperature desulfurizer is changed based on the concentration of sulfur compound in the raw material.    USE - Hydrogen-generating apparatus is used for fuel cell system (claimed).    ADVANTAGE - The hydrogen-generating apparatus continues and performs desulfurization of sulfur compound contained in raw material without optimizing the heat balance even if the concentration of the sulfur compound contained in raw material is changed by area.    DETAILED DESCRIPTION - A hydrogen-generating apparatus comprises normal-temperature desulfurizer from which sulfur compound in a raw material is removed at normal temperature, a hydrodesulfurization device which removes the sulfur compound in the raw material at temperature higher than normal temperature, and a hydrogen generator which generates hydrogen-containing gas using the raw material. The capacitance of the normal-temperature desulfurizer is changed based on the concentration of sulfur compound in the raw material. The hydrodesulfurization device does not depend on the concentration of the sulfur compound in the raw material. INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) manufacture of hydrogen-generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of hydrogen-generating apparatus. (Drawing includes non-English language text)    Normal-temperature desulfurizer (11)    Hydrodesulfurization device (12)    Hydrogen generator (13)    Heat-insulating material (15)    Hydrogen-generating appartaus (100)
NOVELTY - The method involves applying a liquid electrode precursor containing an organometallic compound on the electrolyte layer (30) of a solid oxide type, and irradiating energy light of an ultraviolet region to the electrode precursor.    USE - Manufacturing method of fuel cell.    ADVANTAGE - Enables manufacture of highly active electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a fuel cell.    Metal support body (10)    Holes (11)    Electrode (20)    Electrolyte layer (30)    Fuel cell (100)
NOVELTY - An alkali-free-glass-type sealing material comprises glass composition containing (in weight%) barium oxide (50-85), silica (4-20), alumina (1-15), boron oxide (0-20) and titanium oxide (0-30) as an essential component.    USE - Alkali-free-glass-type sealing material is used for stainless steel and separator for manufacturing solid oxide fuel cell (all claimed).    ADVANTAGE - The solid oxide fuel cell manufactured using alkali-free-glass-type sealing material has excellent chemical stability-proof property, adhesiveness, gas permeability and flexibility, and improved durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) solid oxide fuel cell; and    (2) manufacture of solid oxide fuel cell.
NOVELTY - A refrigerant contains carbon dioxide, isobutane, and propane.    USE - A refrigerant for refrigerators (claimed).    ADVANTAGE - Energy is saved, and problems relating to global warming and odor are addressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for household ultra-low temperature freezer of refrigerator with refrigerant for cooling to ultra-low temperature which has freeze-preserving chamber and freezer main body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the external appearance of the household ultra-low temperature freezer.    Household ultra-low temperature freezer (1)    Freezer main body (2)    Freeze-preserving chamber (3)    Temperature regulator (13)    Display part (15)
NOVELTY - An acid compound (II) or (III) is cyclized in the presence of aluminosilicate as catalyst at 80 degrees C, to obtain a lactone compound of formula (I).    USE - Manufacture of lactone compound e.g. gamma -hexano lactone and gamma -heptano lactone. Uses include but are not limited to pharmaceuticals, agrochemicals, flavor compounds, and intermediate for solvent, cosmetics, foodstuffs, lacquers and varnishes.    ADVANTAGE - The method efficiently and economically provides lactone compound without causing pollution to environment.    DETAILED DESCRIPTION - An acid compound of formula: R1-CH=CH-CH2-C(=O)-OH (II) or R2-CH=CH-CH2-C(=O)-OH (III) is cyclized in the presence of aluminosilicate as catalyst at 80 degrees C, to obtain a lactone compound of formula (I).    R1=alkyl of formula: CnH2n+1;    R2=alkene of formula: CnH2n-1;and    n=2-8.
NOVELTY - The method involves delivering an ethanol for combustion in the engine (106). A diesel is delivered for combustion in the engine, where the diesel is different than the ethanol. The ethanol is delivered as a reductant for the exhaust gas treatment system (166). The ethanol is delivered to cylinders (108) of the engine by direct injection during an intake stroke of an engine cycle. The ethanol is delivered as a reductant, when nitrogen oxide conversion efficiency decreases below threshold value.    USE - Method for emission control of engine e.g. internal combustion engine used in vehicle system such as rail vehicle. Can also be used in stationary engine in power-plant application, or engine in ship propulsion system, compression ignition engines, diesel engines and spark ignition engines.    ADVANTAGE - The efficiency of the engine can be increased and emissions can be reduced. The ethanol may further serve as reductant for the exhaust gas treatment device, thus the need for providing separate system for the reductant can be avoided and also overall size of the engine and exhaust gas treatment system can be reduced. The amount of space occupied by the engine and exhaust gas treatment system can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of rail vehicle with dual fuel engine.    Internal combustion engine (106)    Cylinders (108)    Controller (112)    Intake passage (132)    Gas treatment system (166)
NOVELTY - The system has a collection vessel (18) that is positioned above the electrodes (20,22). A gas conduit bundle assembly is connected to the gas generating assembly. The gas generating assembly is positioned at depth for immersing the electrodes within the polar molecular fluid. An electrical potential is generated between the electrodes for enabling an electrolytic breakdown of the polar molecular fluid. The pressure of the gas components is set above an atmospheric pressure that depends upon the depth of gas generating assembly.    USE - System for producing pressurized gas such as oxygen gas and hydrogen gas from polar molecular fluid.    ADVANTAGE - The use of complex and expensive equipment to pressurize the gas is eliminated. The energy consumption required for compressing the gas is reduced. The production efficiency of the system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the electrode bell pressurized gas generator apparatus.    Electrolysis system (10)    Collection vessel (18)    Electrodes (20,22)    Central aperture (24)    Valve (44)
NOVELTY - Method of manufacturing a fertilizer comprises creating a thixotropic paste from a composition containing biosolids, adding an oxidizing agent to the paste, adding an alkaline agent to the paste to produce a pH of 10 or higher, exposing the paste to ammonia at a concentration of at least 1000 ppm, adding an acid to the paste to produce heat and a pH of 7 or less, adding a granulating agent to the paste, extruding or granulating the paste, and drying the extruded or granulated paste to a dryness of 90% or more of solids.    USE - The method is useful: for manufacturing the fertilizer (claimed); for converting organic containing materials into nutrient fertilizers; and to increase the plant nutrient content in the organic containing product, preferably nitrogen, phosphorus and/or potassium and iron. No biological data given.    ADVANTAGE - The method: provides the fertilizer in a safe and an economical manner; improves an odorant quality of the biosolids; destroys a pathogen in sludges; increases nitrogen, phosphorus, iron or other plant nutrients e.g. potassium and/or sulfur.
NOVELTY - The system has a photovoltaic unit and/or wind turbine (1), a control device (2), a transformer, a rectifier, an inverter (3), an electrolysis device (4), a hydrogen storage device (5), an oxygen storage device (6), a generator or fuel cell (7), a counter for regional network (11), an alternating current (AC) power supply (12), a direct current (DC) power supply (13), a hydrogen network (14) and an oxygen network (15). The control device transmits DC current from photovoltaic unit to inverter which converts DC current into AC current and supplies to AC power supply.    USE - Autonomous power supply system for hydrogen-powered vehicle and household appliance (all claimed) and electric vehicle.    ADVANTAGE - The power can be made available also during night time, winter or cloudy conditions, and the efficiency of the autonomous power supply system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the autonomous power supply system.    Photovoltaic unit and/or wind turbine (1)    Control device (2)    Inverter (3)    Electrolysis device (4)    Hydrogen storage device (5)    Oxygen storage device (6)    Fuel cell (7)    Counter for regional network (11)    AC power supply (12)    DC power supply (13)    Hydrogen network (14)    Oxygen network (15)
NOVELTY - Pet house comprises a pet room and a fermentation box (1) installed below the pet room (2) for fermenting pet waste. The pet room and fermentation box are partially or completely connected with each other. The fermentation box is equipped with a stirring device.    USE - As pet house and for decomposing pet excreta. Can also be useful for processing household kitchen waste in small scale.    ADVANTAGE - The pet house is wash-free, eco-friendly, cost-effective and simple to operate, and provides worry-free way to enjoy the pleasure of keeping pets, and converts pet excreta into odorless organic matter.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of pet house.    Fermentation box (1)    Pet room (2)    Humidity sensor (8)    High pressure water pump (10)    Roller (16)
NOVELTY - The device has guiding channels (2, 3) comprising filter housings (4, 5) with a mineral filter element, and a microwave source (6) arranged at the filter housing. The microwave source radiates microwave to the filter element, and exhaust channels (9, 10) collect fluid exhaust material produced in the filter housing by the microwave radiation. A supply unit supplies additives e.g. water vapor, to the filter housing, and a plasma reactor (11) is arranged downstream of the collecting arrangement, where the reactor converts hydrocarbon-containing exhaust material into synthesis gas.    USE - Filter device for filtering fluid carrier material i.e. exhaust air of a ship engine.    ADVANTAGE - The microwave source radiates microwave to the filter element, and the exhaust channels collect fluid exhaust material produced in the filter housing by the microwave radiation, thus permitting energy recovery of loading material removed from the filter element.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a filter device.'(Drawing includes non-English language text)'    Guiding channels (2, 3)    Filter housings (4, 5)    Microwave source (6)    Exhaust channels (9, 10)    Plasma reactor (11)
NOVELTY - The purifying device has an air distributing plate (301) and a baffle plate that are provided with an air inlet (101) which is penetrated through a gas-guide tube (302). The gas guide tube is equipped with a gas conveying pipe (402) whose one end is connected with an upper portion of a washing chamber (3) and other end is set in a cleaning solvent (6). One end of the baffle plate is provided with a gas circulating port. The gas circulating ports of the upper and lower baffle plates are respectively set on the two sides of a gas-liquid separating chamber (4).    USE - Purifying device used in biomass waste resource pyrolysis gasification system.    ADVANTAGE - The purifying device is provided with several functions such as leaching, wash bath, separating the gas and liquid resistance, and filtering and is featured with simple structure, small occupied space accomplished through the simple structure. The liquid particles are separated from the gas by the shielding plate so as to prevent the damage to the subsequent device.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the purifying device used in biomass waste resource pyrolysis gasification system.    Washing chamber (3)    Gas-liquid separating chamber (4)    Cleaning solvent (6)    Air inlet (101)    Air distributing plate (301)    Gas-guide tube (302)    Gas conveying pipe (402)
NOVELTY - Fermentation tank comprises cylindrical tank (1), marsh gas outlet (3), gas collecting chamber (2) at the upper part of the fermentation tank, methane collecting port (4) connected to the marsh gas outlet, biogas slurry outlet (6) and biogas residue outlet (5) at the lower part of cylindrical surface from top to bottom.    USE - The fermentation tank is useful for treating excrement, particularly animal excrement.    ADVANTAGE - The fermentation tank enables rapid treatment, is convenient to use and environmentally-friendly, increases economic efficiency and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fermentation tank.    Cylindrical fermentation tank (1)    Gas collecting chamber (2)    Marsh gas outlet (3)    Methane collecting port (4)    Biogas residue outlet (5)    Biogas slurry outlet (6)
NOVELTY - Refluxing and treating sludge by acidized fermentation liquor involves hydrolyzing and acidizing the sludge, pre-acidizing the sludge by refluxing acid fermented liquid, hydrolyzing, acidizing and fermenting the pre-treated sludge.    USE - For refluxing and treating sludge by acidized fermentation liquor which is useful for producing methane (claimed).    ADVANTAGE - The method utilizes sludge fermentation liquor to pre-acidize sludge, which can shorten time of anaerobic digestion, increase gas production rate, and reduce operating cost. After pre-treatment, the total chemical oxygen demand (TCOD) of sludge liquid phrase can be increased 3000-1000 mg/l, moreover protein, polysaccharide and other material in liquid phrase can be increased significantly. The speed and efficiency of sludge hydrolytic acidification can be increased after pretreatment. The methane yield can be improved to 40% to 80% of the anaerobic digestion. The method can be used for the sewage treatment factory in sludge anaerobic digestion processing technology upgrading, and sludge digestion technology, it can improve digestion amount of methane and reduce sludge digestion time, and fully uses hydrolysis acidification phase to generate the organic acid and then to realize the sludge to generate obvious environmental benefit and economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing methane by refluxing and treating sludge by acidized fermentation liquor involving hydrolyzing and acidizing the sludge, pre-acidizing the sludge by refluxing acid fermented liquid, hydrolyzing, acidizing and fermenting the pre-treated sludge, and making use of product to produce methane.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the method for refluxing and treating sludge by acidized fermentation liquor.
NOVELTY - The method involves effectively diversifying the surface structure of the polymer electrolyte membrane. The electric discharge process of the fuel cell stack is performed with specific current density.    USE - Fuel cell stack activation method.    ADVANTAGE - The use amount of hydrogen for stack activation can be decreased and time required for stack activation can be reduced. The ion conductivity of the polymer electrolyte membrane can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the current density. (Drawing includes non-English language text)
NOVELTY - A methane fermentation tank has storage reservoir, having inclination part in the inner side, which accommodates wastewater which contains anaerobic organic substance, concrete partition wall, stirring apparatus, bottom sheet positioned at the bottom part, and gas impermeable cover sheet for awnings positioned at the inclination part of the storage reservoir, fixing tool, methane gas piping, and bottom sheet piece.    USE - A methane fermentation tank.    ADVANTAGE - Fracture or fault formation in the bottom sheet is prevented.    DETAILED DESCRIPTION - A methane fermentation tank has storage reservoir, having inclination part in the inner side, which accommodates wastewater which contains anaerobic organic substance, concrete partition wall which partitions off the storage reservoir, stirring apparatus spaced apart on both sides of the partition wall, can be moved vertically, and stirs wastewater in the storage reservoir, bottom sheet positioned at the bottom part, and gas impermeable cover sheet for awnings positioned at the inclination part of the storage reservoir, which stores methane gas emitted from wastewater, fixing tool which fixes the edge part of the bottom sheet and the cover sheet for awnings, methane gas piping positioned inside the cover sheet for awnings, and bottom sheet piece reaching from one bank part to other bank part opposing the storage reservoir, and is made from cut piece of raw material for bottom sheets extended from another bank part adjacent to bank part of bottom sheet piece, and raw material for bottom sheets of the corner part of storage reservoir. An INDEPENDENT CLAIM is included for construction method of bottom sheet.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the methane fermentation tank.    Storage reservoir (11)    Partition wall (12)    Organic waste water (14)    Fixing tool (24)    Bottom sheet (25)
NOVELTY - The method comprises mixing a nitrogen containing compound comprising ammonia or ammonia water and organic amine or ammonium salt with the crude biodiesel on weight ratio of 0.2-2:100 at normal temperature, adding methanol or ethanol into the mixture, heating and reacting the mixture at normal pressure to obtain a reacted mixed oil, conveying the reacted mixed oil into a fractionation tower and keeping the temperature on a top of the tower within 205 degrees C to extract out a light element to obtain primary product oil.    USE - The method is useful for refining internal combustion engine fuel from cracked biodiesel.    ADVANTAGE - The method is capable of economically refining the internal combustion engine fuel from cracked biodiesel with control corrosion resistant in an environmental friendly manner.    DETAILED DESCRIPTION - The method comprises mixing a nitrogen containing compound comprising ammonia or ammonia water and organic amine or ammonium salt with the crude biodiesel on weight ratio of 0.2-2:100 at normal temperature, adding methanol or ethanol into the mixture, heating and reacting the mixture at normal pressure to obtain reacted mixed oil, conveying the reacted mixed oil into a fractionation tower, keeping the temperature on a top of the tower within 205 degrees C to extract out a light element to obtain primary product oil, washing the primary product oil by alkali till the acidity is within 7 and obtaining the finished product of internal combustion engine fuel. The weight ratio of the methanol or the ethanol to the crude biodiesel is 0.2-0.5:100. The crude biodiesel is derived from the biodiesel obtained via catalytically cracking the animal and vegetable oil by alumina.
NOVELTY - The microorganism composite bacteria comprises strains comprising 10-35% of Cellulomonas fimi (ATCC 484), 15-28% of Bacillus cereus (ATCC 12480), 5-15% of Bacillus amyloliquefaciens (ATCC 23842), 8-25% of Clostridium papyrosolvens (ATCC 700395), 10-25% of Clostridium bifermentans (ATCC 17838), 5-15% of Clostridium glycolicum (ATCC 29797), and 6-15% of Clostridium butyricum (ATCC 13732).    USE - The microorganism composite bacteria is useful for producing methane by promoting anaerobic fermentation of traditional Chinese medicine dregs (claimed).    ADVANTAGE - The microorganism composite bacteria is capable of economically producing the methane with reduced energy consumption in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microorganism composite bacteria for producing methane by promoting anaerobic fermentation of traditional Chinese medicine dregs.
NOVELTY - The method involves initial homogenization of municipal waste stream by using a material classifying device. The waste stream is subjected to additional cleaning and mechanical homogenization to produce a mixture of refuse derived fuel (RDF) fuel with a calorific value of 16-22 MJ/kg, and a permeate fraction. Water content of the mixture of the RDF and the fraction is reduced to below 20 percentage by weight. The mixture is subjected to additional cleaning and mechanical homogenization to form solid recovered fuel (SRF) with a calorific value of 12-17 MJ/kg.    USE - Method for producing RDF and SRF from municipal waste.    ADVANTAGE - The method enables increasing efficiency of energy recovery from waste, and reducing capital and operating costs of fuel producing from waste by mechanical and biological treatment.
NOVELTY - Method for promoting complex enzyme catalytic degradation of rice straw using oxalic acid and manganese, involves (a) grinding the rice straw into straw powder and sieving the powder, (b) processing Phanerochaete chrysosporium under submerged culture to obtain complex enzyme solution, and (c) adding the complex enzyme solution into the straw powder, simultaneously adding oxalic acid, manganese solution, and hydrogen peroxide solution, processing the solution at heat preservation and moisture retention, and completing the catalytic degradation.    USE - The method is useful for promoting complex enzyme catalytic degradation of rice straw using oxalic acid and manganese.    ADVANTAGE - The method is simple, cost-effective, and environmentally-friendly and increases the speed of degradation and reduces the heat loss.
NOVELTY - The equipment has a buffer tank provided with lower drain connectors. An upper overflow outlet is fluidly connected to a filler neck of a cylindrical container. Another filler neck is fluidly connected to a filter plate. A conduit is connected to a hydraulic pump. A collecting duct is connected to a drain outlet and the cylindrical container. The filter plate is mounted on a tub tray in which a drain nozzle is in communication with the collecting duct.    USE - Equipment for producing agricultural biofuel.
NOVELTY - A kitchen garbage full biomass resource is used by removing impurities on collected kitchen waste; compressing sorted kitchen garbage to remove large amount of oil-water component, crushing solid material into uniform grain diameter and using for subsequent fermentation of fuel ethanol, and taking liquid material into oil-water separator for oil-water separation; separating fermentation liquid and residue after producing fuel ethanol, and drying and pelletizing solid product to prepare high protein feed; and processing the wastewater.    USE - Method for using kitchen garbage full biomass resource (claimed) to produce fuel ethanol, protein feed, and biodiesel.    ADVANTAGE - The method reduces kitchen waste processing cost and improves economic benefit. The operation process is mild, production energy consumption is low, and the process is green and environment-friendly.    DETAILED DESCRIPTION - Using kitchen garbage full biomass resources comprises:    (A) removing impurities on collected kitchen waste by magnetically separating metal impurities and other non-biomass component (sand, glass, and plastic);    (B) compressing sorted kitchen garbage to remove large amount of oil-water component, crushing solid material into uniform grain diameter and using for subsequent fermentation of fuel ethanol, and taking liquid material into oil-water separator for oil-water separation;    (C) oil-water separating the liquid, using waste grease for making biological diesel oil, and reusing organic wastewater after being treated;    (D) separating the fermentation liquid and residue after producing fuel ethanol which contain large amount of food waste protein and yeast cell protein by centrifuging, and drying and pelletizing solid product to prepare high protein feed; and    (E) processing the wastewater by comprehensively using immobilized biological activated carbon adsorption degradation technology and membrane separation technology.
NOVELTY - Ethylene-containing composition comprises 2C hydrocarbon compounds (75-99.9 vol.%); and ethylene, where the ratio of the quantity of ethylene to the total quantity of 2C hydrocarbon compounds is 97-99.5%.    USE - The composition is useful in the manufacture of ethylene derivative compound, ethylene dichloride, vinyl chloride and PVC (claimed).    ADVANTAGE - The composition: is obtained in a higher yield at a reduced cost; has purity inferior to that of polymerization grade ethylene and contains impurities of types and at levels that will not be prohibitive for its future use; and is obtained at a reduced heat duty compared to the one required to obtain polymerization grade ethylene.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) manufacturing the ethylene-containing composition comprising: (a) subjecting an effluent stream (E) containing ethylene and other constituents coming from an oxygenate-to-olefins process and having been submitted to a conventional treatment, to a pre-conditioning treatment to obtain a compressed effluent stream (E1); and (b) separating the compressed effluent stream E1 inside 1-3 distillation towers to obtain the ethylene-containing composition;    (2) manufacturing at least one ethylene derivative compound starting from the ethylene-containing composition; and    (3) manufacturing ethylene dichloride comprising subjecting the ethylene-containing composition to a chlorination and/or an oxychlorination.
NOVELTY - The device has a flue gas component detecting device (18) connected with an air outlet pipe (17). An upper part of a detecting head (21) of a rubbish fuel position detecting device is set on a combustion chamber (5). A side wall of the upper part of the head is set in middle of a cathode-side wall of a coke oven carbonization chamber. A fuel vaporizing device comprises an automatic control system. A feeding device, a discharging device, a blast device, the flue gas component detecting device, a temperature detecting device (19) and the head are connected with the automatic control system.    USE - Rubbish fuel vaporizing device.    ADVANTAGE - The device has convenient operation, simple operation and economic and social benefits, and can realize fully automatic control without pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a rubbish fuel vaporizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a rubbish fuel vaporizing device.    Combustion chamber (5)    Air outlet pipe (17)    Flue gas component detecting device (18)    Temperature detecting device (19)    Detecting head (21)
NOVELTY - The furnace has a burner provided with a fuel preprocessing system. A fuel crushing device is connected with a qualified fuel tank and an unqualified tank. The bottom part of a front furnace nozzle is connected to a furnace body through a vaporizing furnace synthesis gas exit that is arranged with a synthesis gas monitoring unit. Two microwave plasma generators are arranged in a gasification reaction section of the furnace body and 2 to 4 work gas interfaces.    USE - Microwave plasma biomass entrained flow bed gasification furnace.    ADVANTAGE - The furnace utilizes efficient biomass fuel without excessive crushing and without excessive feeding of the furnace. The furnace enables high biomass fuel combustion efficiency and high quality gasification, and can prepare synthesis gas as a biomass fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microwave plasma biomass entrained flow bed gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of microwave plasma biomass entrained flow bed gasification furnace.
NOVELTY - The furnace has a fuel inlet provided on a vertical furnace body, and a product gas outlet provided with a slag at bottom of the furnace body and arranged with a synthesis gas monitoring unit. A microwave plasma generating device is provided at an upper part of the furnace body. A section of the microwave plasma generating device comprises microwave plasma activated oxidant and fully chemical reaction, where reaction temperature is controlled at 700 degrees Celsius to 1600 degrees Celsius. Microwave power source of the generating device exhibits main frequency of 2.45 GHz.    USE - Microwave plasma biomass gasification furnace.    ADVANTAGE - The furnace performs biomass gasification process in a simple, reliable and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a microwave plasma biomass gasification furnace.
NOVELTY - Method (M1) for sequestering mycotoxin from material, comprising: providing material comprising mycotoxins, and molecularly imprinted polymer generated via polymerization of at least one monomer and crosslinker in presence of mycotoxin template including N-(2-hydroxy-3,5-dichlorobenzoyl)-L-phenylalanine, 5-chloro-6,7-dimethoxy-1-methylisatine, ethyl 3-hydroxy-6,7-dimethoxy-2-indolone-3-carboxylate, 6,7-dimethoxyisatine, or 6,7-dimethoxy-1-methylisatine; and contacting molecularly imprinted polymer with material under conditions that permit molecularly imprinted polymer to bind the mycotoxin.    USE - The method is useful for sequestering mycotoxin from material, where: the mycotoxin is ochratoxin A and sporidesmin; and the material is a beverage, a foodstuff, an animal feed, a pharmaceutical composition, a nutraceutical composition, a cosmetic composition or a substance necessary to sustain life, that is a medium for use in aquaculture or a gaseous sample comprising oxygen (all claimed).    ADVANTAGE - The method utilizes the molecularly imprinted polymer, which: is reusable and ecologically friendly; exhibits reduced or no toxicity, high water sorption and retention, enhanced shelf life and high affinity towards target mycotoxins; and minimizes hazardous waste, and can be produced in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for making the molecularly imprinted polymer, comprising: providing the mycotoxin template, and at least one monomer and at least one crosslinker; and contacting the mycotoxin template with the monomers and the crosslinkers under conditions that permit polymerization of the monomers and crosslinkers in the presence of the mycotoxin template.
NOVELTY - The apparatus has a conveyor (13) supplying biomass into a lower section of a vertical reactor (6). Crude gas is drawn-off in an upper section of the reactor. Another vertical reactor (5) is arranged in a lower section of the reactor. The latter reactor is provided with a tube, which is connected with the conveyor. The conveyor is arranged in enlarging upper sections (7, 8) of a gasification medium. A portion of the biomass is dried and subjected to partial pyrolysis at temperature of 130 to 350 degree Celsius. Another portion of the biomass is heated by a gasification medium.    USE - Apparatus for treating biomass in a vertical reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an apparatus for treating biomass in a vertical reactor.'(Drawing includes non-English language text)'    Vertical reactors (5, 6)    Enlarging upper sections of gasification medium (7, 8)    Conveyor (13)
NOVELTY - Fuel feed stock, comprises municipal solid waste (MSW), and a sorbent, where the MSW prior to thermal conversion, has a carbon content of 36.6-46%, a hydrogen content of 4.9-6%, an oxygen content of 35.4-43.3%, an ash content of 8.6-10.6%. The feed stock has a hydrogen/carbon ratio of 0.117-0.143, and an oxygen/carbon ratio of 0.85-1.04. The feed stock contains biodegradable and non-biodegradable materials, and no glass, metals, grit and non-combustibles.    USE - The fuel feed stock is useful: to mitigate the sulfur content of another fuel (claimed); for combustion or gasification applications; as loose material, densified cubes, briquettes, pellets, honeycomb and sheets; for co-firing with other waste fuel e.g. densified or loose refuse-derived fuels for both emission and corrosion control; and for the production of thermal energy, power, biofuels and petroleum.    ADVANTAGE - The fuel feed stock: are free of glass, metals, grit and non-combustibles; contains biodegradable and non-biodegradable materials; has a higher heating value of 5000-9000 BTU/lb, a volatile matter content of 40-80%, a sulfur content of less than 1 wt.%, a moisture content of 10-40 wt.% and a chlorine content of less than 1%; when converted produces less greenhouse gas (GHG) emissions as compared to the known level of GHG emitted from coal when converted; exhibit improved reaction kinetics, improved sorbent reactivity, improved pollutant removal efficiency, improved fuel conversion, improved corrosion control, reduced ash slagging, reduced operating temperature, and extend power generating facility lifetime; and avoid expensive retrofit costs and reduces operating and maintenance costs.
NOVELTY - Preparation of meropenem trihydrate comprises subjecting meropenem compound (I) to hydrogen extricated protective reaction in the presence of catalyst and under mixed solvent system consisting of water, water-soluble solvent and water-insoluble solvent to obtain meropenem trihydrate.    USE - Preparation of meropenem trihydrate.    ADVANTAGE - The method improves quality and yield coefficient of product. It is economical and environment friendly. It simplified production and shortens production cycle.    DETAILED DESCRIPTION - Preparation of meropenem trihydrate comprises subjecting meropenem compound of formula (I) to hydrogen extricated protective reaction in the presence of catalyst and under mixed solvent system consisting of water, water-soluble solvent and water-insoluble solvent to obtain meropenem trihydrate.    PNB=p-nitrobenzyl; and    PNZ=p-nitrobenzyl oxygroup carbonyl.
NOVELTY - A crude (S)-oxiracetam is purified by adding crude (S)-oxiracetam into water to dissolve, standing for 1-3 days at 0-18 degrees C to separate out colorless and transparent crystals, filtering, washing with ice water at 0-5 degrees C, and drying in vacuum.    USE - Method for purification of crude (S)-oxiracetam (claimed).    ADVANTAGE - The method provides (S)-oxiracetam with purity of 98-98.4%. It is simple, has gentle reaction condition, and has low production cost. It does not cause pollution caused by organic solvent, thus it is environment friendly, and is suitable for large-scale industrial production.
NOVELTY - Composition comprises 25-45 wt.% of cellulose decomposing bacteria, 9-15 wt.% of proteolytic bacteria, 8-15 wt.% of fat decomposing bacteria, 8-12 wt.% of hydrogen-generation acetic acid-generation bacteria, 18-31 wt.% of sulfate reducing bacteria and 2.5-9.5 wt.% of Methanogenic archaea.    USE - The composition is useful for dry fermentation of biogas.    ADVANTAGE - The composition ensures easy and economical dry fermentation of the biogas with high stability and reduced energy consumption.
NOVELTY - Producing ethanol with solid-liquid fermentation of plant straws, comprises crushing plant straws, drenching mycete-containing water, processing preliminary fermentation to degrade nutrient substances, e.g. saccharides and protein in the straw, solubilizing other nutrient substances and squeezingly washing the straws with water to remove insoluble cellulose to obtain a solution containing pentose, hexose and liquid protein, concentrating the liquid phase, fermenting and distilling Saccharomycetes to obtain ethanol, where the liquid waste combines with residues to obtain an organic fertilizer.    USE - The method is useful for producing ethanol with solid-liquid fermentation of plant straws.    ADVANTAGE - The method completely utilizes various straws and strains with high conversion efficiency, strong specificity and short growth cycle to improves the production efficiency, and shortens the production cycle.    DETAILED DESCRIPTION - Producing ethanol with solid-liquid fermentation of plant straws, comprises crushing plant straws, drenching mycete-containing water, processing preliminary fermentation to degrade nutrient substances, e.g. saccharides and protein in the straw, solubilizing other nutrient substances and squeezingly washing the straw with water to remove insoluble cellulose to obtain a solution containing pentose, hexose and liquid protein, concentrating the liquid phase, fermenting and distilling Saccharomycetes to obtain ethanol, where the liquid waste remained after the distillation combines with the residues remained after the washing to obtain an organic fertilizer.
NOVELTY - Nut shell biomass particulate fuel comprises (in wt.%) nut inner layer hard shell powder (5-10), nut outer layer soft shell slurry (60-65), wood shavings powder (15-20) and sawdust (10-15).    USE - Used as a nut shell biomass particulate fuel.    ADVANTAGE - The fuel has high calorific value and is tight granular structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the nut shell biomass particulate fuel, comprising (i) crushing the nut outer layer soft shell to slurry, and the nut inner layer hard shell into powder, and (ii) mixing the nut inner layer hard shell powder, the nut outer layer soft shell slurry, wood shavings powder and sawdust, and extruding into columnar grain.
NOVELTY - The system has a smoke processing device provided with first and second purifying chambers (29, 30). An upper part of the first purifying chamber is provided with a tube (19). A middle part of the first purifying chamber is provided with an air outlet pipe (32). The air outlet pipe is fixed with a bottom surface of a third purifying chamber (38). The third purifying chamber is connected with a fuel pipe (37) and provided with a water outlet (28). An automatic control system is linked to a feeding device, a discharging device (10), a blast device and a flue gas component detecting device (18).    USE - Rubbish e.g. sawdust, crop straw and solid organic wastage, fuel combustible gas furnace fuming system for a thermoelectric cogeneration system.    ADVANTAGE - The system is environmental-friendly, easy to control, inexpensive and convenient to operate, and has better combustion efficiency, high production efficiency and wide application range. The system can realize fully automatic control process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rubbish fuel fuming system control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a rubbish fuel combustible gas furnace fuming system.    Discharging device (10)    Flue gas component detecting device (18)    Tube (19)    Water outlet (28)    Purifying chambers (29, 30, 38)    Air outlet pipe (32)    Fuel pipe (37)
NOVELTY - An alkaline catalyst film comprises inert ceramic membrane as catalytic membrane as carrier. Second carrier is active alumina. Metal hydroxide or salt is alkaline center precursor. Inert ceramic film comprises separating film layer and coated support surface. The coated support surface is hydroxide, chloride, fluoride, nitrate, carbonate, and sulfate of lithium, sodium, potassium, magnesium, and calcium. The separating film layer is alpha -aluminum oxide, titanium oxide, zirconium oxide or silicon carbide.    USE - Alkaline catalyst film used for membrane reactor for producing biological diesel.    ADVANTAGE - The film realizes ester exchange reaction and product separation for green, fast speed, and high efficiency of producing biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the alkaline catalyst film which comprises providing aluminum sol-gel (2-5 mol/L) and preprocessing ceramic membrane carrier and dipping into aluminum sol-gel for 10-30 minutes; blowing residual liquid between pore, drying at 500-700 degrees C for 2 to 5 hours, and repeating step for 1-5 times; and soaking polysilazane film into metal hydride or salt water solution for 3-48 hours, and drying at 500-700 degrees C for 2-10 hours.
NOVELTY - Synthesizing heparin ester comprises taking sodium heparin powder and organic anhydride, pyridine as a catalyst, an inert gas as a protective agent, and performing esterification of heparin in an anhydrous reactor.    USE - The heparin ester is useful for preventing tumor and metastasis.    ADVANTAGE - The method increases the yield to about 80%; is simple, convenient, and easy to control which requires only controlling the dryness degree, reaction temperature and the reaction time; and recycles the filtrate after the reaction is complete; and is ecofriendly. The heparin ester has high anti-tumor and anti-metastasis activity in comparison with conventional medicines.
NOVELTY - Recycling biogas slurry to achieve resource utilization of biogas slurry comprises: (a) anaerobically fermenting fermentation extracted waste liquid to obtain biogas and biogas slurry; (b) performing micro-oxidation; (c) decoloring and performing solid-liquid separation to obtain a filtrate; (d) performing solid acid treatment on the filtrate; (e) mixing the biogas slurry with starch-based raw materials or starch hydrolyzed sugar, stewing, saccharifying, fermenting and extracting the fermentation liquid; and (f) performing biogas fermentation of the extracted waste liquid.    USE - The method is useful for recycling biogas slurry to achieve resource utilization of biogas slurry.    ADVANTAGE - The method infinitely recycles biogas slurry, eliminates wastewater pollution, saves valuable water resources, and reduces production cost.    DETAILED DESCRIPTION - Recycling biogas slurry to achieve resource utilization of biogas slurry comprises: (a) anaerobically fermenting fermentation extracted waste liquid to obtain biogas and biogas slurry; (b) performing micro-oxidation of the biogas slurry; (c) decoloring the biogas slurry and performing solid-liquid separation to obtain a filtrate; (d) performing solid acid treatment on the filtrate; (e) mixing the biogas slurry with starch-based raw materials or starch hydrolyzed sugar in a specific ratio and making up with tap water, stewing and saccharifying, or saccharifying and fermenting, separating and extracting the fermentation liquid to obtain fermentation products and extracted waste liquid; and (f) performing biogas fermentation of the extracted waste liquid in an anaerobic fermentation tank, and returning to the step (a) to form a cycle.
NOVELTY - Directly liquefying cellulose comprises providing raw material cellulose and ionic liquid as agents at normal pressure and 70-150 degrees C, and reacting for 0.5-24 hours; and performing vacuum filtering, drying to constant weight at 105 degrees C, cooling to room temperature, and weighing liquid.    USE - Method of directly liquefying cellulose (claimed) used as chemical industry raw material for producing petroleum.    ADVANTAGE - The method is simple, and has liquefied rate, low corrosiveness, and clean process as compared with traditional liquefying method. Liquefacient has simple structure and can be used repeatedly, and is good for environmental protection. The method has lower and mild condition, and short process time.
NOVELTY - Raw materials including (in parts weight) quaternary ammonium-type lignin (10-80), polyvinyl alcohol (20-90), distilled water (100-200) and crosslinking agent (0.05-50) are added into reactor, stirred, reacted, obtained product is filtered, resultant solid is washed using distilled water for 2-5 times, dried, and sieved using 60-100 mesh-sized screen, to obtain quaternary ammonium-type lignin/polyvinyl alcohol composite material. The crosslinking agent is glutaraldehyde aqueous solution, formaldehyde aqueous solution or epoxy chloropropane aqueous solution.    USE - Preparation of quaternary ammonium-type lignin/polyvinyl alcohol composite material used for wastewater treatment and absorption-separation of nitrogen-containing compound e.g. trinitrotoluene and nitro compounds in chemical industry, food industry, pharmaceutical industry and agrochemical industry.    ADVANTAGE - The environmentally-friendly quaternary ammonium-type lignin/polyvinyl alcohol composite material having has high selective absorption capacity with respect to nitrogen-containing compounds e.g. trinitrotoluene and nitro compounds is economically prepared by simple method.    DETAILED DESCRIPTION - Raw materials including (in parts weight) quaternary ammonium-type lignin (10-80), polyvinyl alcohol (20-90), distilled water (100-200) and crosslinking agent (0.05-50) are added into a reactor at 40-150 degrees C, pH of resultant product is maintained as 1-6, stirred at rate of 100-1000 rpm, reacted for 1-8 hours, obtained product is filtered, resultant solid is washed using distilled water for 2-5 times, dried at 25-80 degrees C for 4-24 hours, and sieved using 60-100 mesh-sized screen, to obtain quaternary ammonium-type lignin/polyvinyl alcohol composite material. The crosslinking agent is glutaraldehyde aqueous solution, formaldehyde aqueous solution or epoxy chloropropane aqueous solution, having concentration of 1-50 wt.%.
NOVELTY - A soil arsenic passivating agent comprises (wt.%) red mud (50-60), straw biomass char (30-40), and ferric chloride (5-18).    USE - A soil arsenic passivating agent for the reduction of soil arsenic crop effectiveness and toxicity, reduction of arsenic absorption of crop in soil, and passivation of arsenic in soil (claimed).    ADVANTAGE - The soil arsenic passivating agent can stabilize arsenic in soils and reduce arsenic toxicity to achieve the goal of reducing crop arsenic absorption. It reduces the environmental pollution caused by stacking large number of industrial and agricultural wastes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparation of soil arsenic passivating agent comprising mixing 70-80 kg semi-air dried red mud and 80-95 kg naturally dried crop stalks with the length of 20-30cm; adding water to 12-18 kg ferric chloride hexahydrate; adding the ferric chloride solution into the mixture; stirring; adding water; putting the mixed materials into a cement pool to stack, and covering with plastic film for 4-5 days; putting the materials stood in the cement pool to a carbonization furnace; heating at 350-400 degrees C for 1.5-2.5 hours; cooling the mixed materials; and grinding and screening with 0.5-1 mm sieve.
NOVELTY - A vehicle biological diesel oil comprises (wt.%) acid oil (60-70), commodity gasoline (29.6-29.7), and additive (0.3-0.4), which are conveyed to the synthesis tank according to the order, uniformly stirred, and filtered to obtain the product.    USE - A vehicle biological diesel oil.    ADVANTAGE - The diesel oil has low cost, can reach the national diesel standard, has small equipment investment, and can be directly used as diesel oil or mixed with common diesel oil. The equipment investment is small. The production process would not generate secondary pollution, and the obtained finished product diesel has low cost to replace the petroleum resource.
NOVELTY - Synthetic methanol diesel fuel comprises (in %mass): national standard diesel (40-80), methyl alcohol (10-35), waste animal or plant fat (5-20), biodiesel (5-20), solvent oil number 120 (1-20) and surfactant (10-30).    USE - The synthetic methanol diesel fuel is useful for motors.    ADVANTAGE - The diesel fuel is crystal clear, does not delaminates fuel tanks, and can be stored for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing diesel fuel, which involves (a) sequentially adding (in %mass): high alcohol (30-60), alkylphenol polyoxyethylene ether (10-30), isohexane (5-20), nitric acid ester (5-15), dimethyl carbonate (5-15), dicyclopentadienyl iron (1-10) and triethylamine (5-10) and blending the components in mixing tank for 30 minutes to obtain surfactant, and (b) sequentially adding methanol, surfactant, waste animal or plant fat, biodiesel, national standard diesel and solvent oil number 120 into tank containing mixture of step (a), and blending the mixture in circular motion for 20-40 minutes using special device including high efficiency static mixer and ultrasonic wave emulsifier to obtain methanol diesel fuel.
NOVELTY - Method for preparing molded coal bonding agent, involves using (in wt.%) fuel, preferably coal (7-15), livestock or animal blood meal (10) and organic waste water (4-6), where animal blood is preserved from coagulation by adding blood anticoagulant (0.48-2) and preservative (0.4-0.6), and the livestock or animal blood meal containing natural polymer material of organic wastewater acts as bonding agent.    USE - The method is useful for preparing molded coal bonding agent.
NOVELTY - The method involves adding a bed material to a fluidized bed. Wind speed control temperature of the fluidized bed is 2 degrees centigrade. Reaction temperature of the fluidized bed is 65-70 degrees centigrade. The fluidized bed is provided with a gasification furnace. A secondary discharging quantity bed is provided with a discharged water bed material. A water washing bed material part is utilized to enter into a dryer unit. A water content of a drying bed material is less than 5 percent. The gasification furnace is located through an external feeding device.    USE - Method for eliminating fluidized bed biomass gasification slag.    ADVANTAGE - The method improves reaction efficiency and avoids biomass ash due to molten slag.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fluidized bed biomass gasification slag eliminating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a fluidized bed biomass gasification slag eliminating method. adding bed material to fluidized bed.
NOVELTY - A polymeric combustion supporting additive comprises (pts.wt.) sodium chloride (11.5-15), calcium hydroxide (4-10), cement (45-55), and sulfate (24-38).    USE - A polymeric combustion supporting additive used for ecological energy-saving fuel (claimed).    ADVANTAGE - The fuel is easy to prepared, and achieves complete combustion. It is reduces pollution generated by the combustion of the coal slime.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an ecological energy-saving fuel, comprising (pts.wt.) coal slime (33-50), craw coal (9-18), and straw (15-27); auxiliary ingredients including calcium carbonate (7-12) and nickel soil (8-15); adhesives including starch (0.5-2), polypropylene (0.05-0.5), and sodium hydroxide (0.1-1); and polymeric combustion-supporting additive (0.01-0.04).
NOVELTY - Preparing ticarcillin disodium intermediate (A) comprises adding dimethyl sulfoxide to thiophene malonic acid and anhydride at 10-60 degrees C, adding acetone in the presence of inorganic acid and hydrolyzing in acidic condition.    USE - (A) is useful in medicine chemical engineering field.    ADVANTAGE - The process: is simple and convenient to operate; and provides less environmental pollution for preparing (A) with high yield (greater than 80%) and high purity (99.8%).
NOVELTY - Synthesis of (4-nitro-phenyl)-diphenyl-amine comprises reacting potassium carbonate, palladium acetate catalyst, diphenylamine, and 4-bromonitrobenzene, without anhydrous and anaerobic operating condition.    USE - Method for the synthesis of (4-nitro-phenyl)-diphenyl-amine (claimed) used for preparing charge transporting material, an electroluminescent material, organic dye, and a medical intermediate.    ADVANTAGE - The method is ligand-free, does not require protection of inert gas directly in air, has mild reaction condition, uses a low dosage of raw materials and catalyst, has high yield, and is inexpensive.
NOVELTY - A ramelteon key intermediate 2-(1,2,6,7-tetrahydro-8H-indeno(5,4-b)furan-8-yl)amine hydrochloride is prepared by dehydrating 1,2,6,7-tetrahydro-8H-indeno(5,4-b)furan-8-one and cyanoacetic acid in the presence of catalyst, solvent and organic acid or alkali, and condensing for decarboxylation reaction.    USE - Method of preparing a ramelteon key intermediate 2-(1,2,6,7-tetrahydro-8H-indeno(5,4-b)furan-8-yl)amine hydrochloride.    ADVANTAGE - The method is simple and low cost, utilizes cheap raw materials, has high yield, produces less pollution, and can be applied to industrial production.
NOVELTY - Synthesis of 3-(3-chloropropyl)-1,3,4,5-tetrahydro-7,8-dimethoxy-2H-3-benzoazepine-2-ketone (I) comprises processing oximation reaction and beckmann rearrangement with 6,7-dimethoxy-1,2,3,4-tetralin-2-ketone, obtaining 1,3,4,5-tetrahydro-7,8-dimethoxy-2H-3-benzoazepine-2-ketone (III), substituting with 1-bromo-3-chloropropane to obtain 3-(3-chloropropyl)-1,3,4,5-tetrahydro-7,8-dimethoxy-2H-3-benzoazepine-2-ketone.    USE - Method for synthesizing 3-(3-chloropropyl)-1,3,4,5-tetrahydro-7,8-dimethoxy-2H-3-benzoazepine-2-ketone (claimed).    ADVANTAGE - The product is separated easily; the post-treatment is simple; and the preparation is environment-friendly.
NOVELTY - The method involves heating biodiesel (4) at a sufficient temperature to achieve desired degree of refining, where impurities are separated from methyl or ethyl esters by adsorption on an adsorbent material (3). The adsorbent material is selected from an activated carbon with a surface area of 850 m2/g, a particle diameter of 0.8 mm and micro-porosity percentage of 80%. The adsorbent material is regenerated with an organic solvent, where retained impurities are eliminated from the adsorbent material.    USE - Method for refining biodiesel for use with diesel fuel for diesel combustion engines.    ADVANTAGE - The method provides biodiesel according European standard EN 14124 in a simple and safe manner without occurring problems.    DETAILED DESCRIPTION - The method involves heating biodiesel at a sufficient temperature to achieve desired degree of refining, where impurities are separated from methyl or ethyl esters by adsorption on an adsorbent material. The adsorbent material is selected from an activated carbon with a surface area of 850 m2/g, a particle diameter of 0.8 mm and micro-porosity percentage of 80%. The adsorbent material is regenerated with an organic solvent, where retained impurities are eliminated from the adsorbent material. A liquid fraction is obtained after the regeneration and subsequent removal of solvent, which is rich in glycerides, dyestuffs and natural antioxidants in the form of concentrated oily extract. The adsorbent material is reused to perform thermal regeneration of the material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of impurities extraction from the biodiesel.    Stirred tank (1)    Cooling or heating jacket (2)    Adsorbent (3)    Biodiesel (4)    Stirred mixture (5)
NOVELTY - Production of glucosamine hydrochloride comprises using citric acid waste residue as raw material; hydrolyzing; filtering; concentrating to obtain crude glucosamine hydrochloride; and refining by film separation method comprising adding deionized water in crude glucosamine hydrochloride, steam heating, adding active carbon to react, filtering the mother liquor, naturally cooling, centrifuging, and adding the semi-finished product into film separation system, where film is ultrafiltration membrane.    USE - Production of glucosamine hydrochloride (claimed) i.e. vegetarian glucosamine hydrochloride.    ADVANTAGE - The method is simple and environmentally friendly; achieves high product purity; and provides safe glucosamine hydrochloride product with no fishy smell and no heavy metal pollution. The glucosamine hydrochloride product meets the quality index of Europe, United States, and other developed countries.    DETAILED DESCRIPTION - Production of glucosamine hydrochloride comprises using citric acid waste residue as raw material; hydrolyzing; filtering; concentrating to obtain crude glucosamine hydrochloride; and refining by film separation method. Refining specifically comprises adding deionized water in crude glucosamine hydrochloride; steam heating at 80-95 degrees C; adding active carbon to react for 0.5-1.5 hour; filtering the mother liquor; transferring in cooling kettle; naturally cooling at 25-35 degrees C; centrifuging to obtain glucosamine hydrochloride semi-finished product, where weight ratio of crude glucosamine hydrochloride, deionized water, and active carbon is 1:1:0.1; and adding the semi-finished product into film separation system, where film is ultrafiltration membrane.
NOVELTY - An ammonium sulfate is prepared by adding catalyst and active carbon to wastewater at 10-95 degrees C, aerated and stirred for 10-720 minutes by using air or pure oxygen so that oil is absorbed by the active carbon; reacting sulfide ion with oxygen gas to obtain sulfite ion; adding sulfite or thiosulfate ion with oxygen gas to react to obtain sulfate ion, and reacting thiocyanate ion with oxygen gas to obtain sulfate ion, nitrogen and carbon dioxide gas.    USE - Method for the production of ammonium sulfate (claimed).    ADVANTAGE - The method solves environmental pollution problem of high ammonia nitrogen sulfur-contained high-salinity wastewater, and obtains a high purity ammonium sulfate product.    DETAILED DESCRIPTION - Preparation of ammonium sulfate comprises:    (A) adding catalyst and active carbon to wastewater at 10-95 degrees C, aerating and stirring for 10-720 minutes by using air or pure oxygen so that oil is absorbed by the active carbon; reacting sulfide ion with oxygen gas to obtain sulfite ion; adding sulfite or thiosulfate ion with oxygen gas to obtain sulfate ion; and reacting thiocyanate ion with oxygen gas to obtain sulfate ion, nitrogen and carbon dioxide gas;    (B) performing solid-liquid separation in the mixture reacted; introducing air at 200-900 degrees C and heating for 20-600 minutes to obtain a mixture of active carbon and catalyst, where adsorptive capacity of active carbon and catalytic activity of catalyst are restored, which can be recycled for use;    (C) evaporating the liquid obtained by performing solid-liquid separation for the mixture using centrifugal machine, and crystallizing for 80%;    (D) returning the liquid obtained for catalytic oxidization treatment; and    (E) drying solid obtained to obtain an ammonium sulfate product.
NOVELTY - Preparing 2-(benzyl acrylamide)benzyl acetate involves reacting 2-benzyl acrylamide halide with glycinate in the presence of an acid scavenger to prepare 2-(benzyl acrylamide)acetic acid; and performing catalytic esterification of 2-(benzyl acrylamide)acetic acid and benzyl alcohol to prepare 2-(benzyl acrylamide)benzyl acetate, where reaction of 2-benzyl acrylamide halide and glycinate is carried out in a mixed phase of an organic solvent and a water phase, where molar ratio of 2-(benzyl acrylamide)acetic acid to benzyl alcohol in esterification is 1:1.5-2.    USE - For preparing 2-(benzyl acrylamide)benzyl acetate used as racecadotril intermediate (claimed).    ADVANTAGE - The method reduces preparation cost; reduces environmental pollution; and provides yield of greater than 91.7%.    DETAILED DESCRIPTION - Preparing 2-(benzyl acrylamide)benzyl acetate involves reacting 2-benzyl acrylamide halide with glycinate in the presence of an acid scavenger to prepare 2-(benzyl acrylamide)acetic acid; and performing catalytic esterification of 2-(benzyl acrylamide)acetic acid and benzyl alcohol to prepare 2-(benzyl acrylamide)benzyl acetate, where reaction of 2-benzyl acrylamide halide and glycinate is carried out in a mixed phase of an organic solvent and a water phase. The organic solvent is any one of dichloromethane, chloroform, methylbenzene or acetonitrile. The molar ratio of 2-(benzyl acrylamide)acetic acid to benzyl alcohol in esterification is 1:1.5-2. The catalyst is sodium methylbenzenesulfonate or N,N-dimethylamino pyridine. The quantity is 1-2% of the molar quantity of 2-(benzyl acrylamide)acetic acid. The acid scavenger is sodium hydroxide.
NOVELTY - A sustainable chemical process of green reduction of nitro compounds (R-NO2) or nitroso compounds (R-NO) into corresponding amino compounds (R-NH2), that produces greener R-NH2 in good yields and selectivity with large number of recycle of mother liquor, is disclosed. The process creates sustainable and closed loop of water allowing inherent recycles of all liquid streams generated in the process. Proprietary chemical agents are used in a novel manner which makes the process feasible. The liquid streams generated during the process are inherently recycled completely, making the process a zero liquid discharge process which is green and sustainable. Image 0/0
NOVELTY - An oxygen-enriched fuel comprises acetylene and methanol, where acetylene is utilized as master liquid, and methanol is utilized as a carrier addition engine oil by replacing petrol.    USE - Oxygen-enriched fuel.    ADVANTAGE - The fuel improves the combustion heat value, increases the burning speed, vaporization potential, leaning ability, and avoids gas resistance. The fuel has good antiknock performance, and is simple to produce, inexpensive, easy to apply on a petrol engine generator and safe to use.
NOVELTY - A mesoporous catalyst comprises a carrier i.e. mesoporous aluminum oxide, and an active component, where average particle size of the carrier is 5 to 25 nanometer, volume fraction of the carrier with the average particle size of less than 5 nanometer is greater than 80 percent, and specific surface area of the carrier is greater than 230 square meter per gram. The active component is metal or oxide of rhenium, molybdenum or tungsten, where weight content of the active component is 1-30 percent.    USE - Mesoporous catalyst for disproportionating low-carbon olefin.    ADVANTAGE - The catalyst disproportionates the lowcarbon olefin with improved transform rate, and has prolonged service life.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing mesoporous catalyst    (2) a low-carbon olefin disproportionation reaction method.
NOVELTY - A HHO (two portions of hydrogen and one portion of oxygen)-type hydrogen generator (10) having a reaction cell (12) comprising at least one anode plate (14) and at least one cathode plate (16) in which electric current is passed through a distilled water-electrolyte solution is prepared. The concentration of electrolyte in distilled water-electrolyte solution is increased until the testing by antifreeze tester confirms that the distilled water-electrolyte solution does not freeze at predetermined temperature.    USE - Preparation of hydrogen generator used in winter.    ADVANTAGE - The damage of interior of reaction cell in the hydrogen generator is prevented. The output stream from reaction cell is bubbled through solution of neutralizing chemical to neutralize electrolyte residue in the output stream, without using bubble tubes.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen generator.    Hydrogen generator (10)    Reaction cell (12)    Anode plate (14)    Cathode plate (16)    Water outlet (28)
NOVELTY - A membrane separation activated-sludge system (10) comprises a biological reactor which biologically treats to-be-processed water with an activated sludge, a membrane module which enclosed the side surface of the several flat films arranged in parallel by the casing is immersed, and a membrane separation tank separated into solid and liquid while producing the upward flow of the to-be-processed water from the biological reactor between the films of a several flat film.    USE - Membrane separation activated-sludge system e.g. membrane bioreactor is used for treating to-be-processed water e.g. sewage and industrial wastewater.    ADVANTAGE - The membrane separation activated-sludge system has high cleaning effect and prevents clogging.    DETAILED DESCRIPTION - A membrane separation activated-sludge system comprises a biological reactor which biologically treats to-be-processed water with an activated sludge, a membrane module which enclosed the side surface of the several flat films arranged in parallel by the casing is immersed, and a membrane separation tank separated into solid and liquid while producing the upward flow of the to-be-processed water from the biological reactor between the films of a several flat film. The activated-sludge concentration of the biological reactor is more than the concentration in nitrification reaction. The flow of sludge inside the membrane separation tank is enabled with the upward flow. A support whose density is more then the water is added to the membrane separation tank. An INDEPENDENT CLAIM is included for membrane separation activated-sludge method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of membrane separation activated-sludge system. (Drawing includes non-English language text)    Membrane separation activated-sludge system (10)    Pipings (16b,18a)    Strainer (19)
NOVELTY - A hydrogen-production apparatus consists of a reaction chamber (2), a belt-shaped hydrogen-production substance supplier (7), and a movement unit. A solution (4) for reaction for producing hydrogen by contacting with a hydrogen-production substance (18) is stored in the reaction chamber. A hydrogen-production substance is supplied by the supplier. The hydrogen-production substance is immersed in the solution in the movement unit by moving the hydrogen-production substance supplier in the longitudinal direction.    USE - Hydrogen-production apparatus is used for fuel cell systems (claimed) used in industrial applications.    ADVANTAGE - The hydrogen-production apparatus enables easy control of generation amount of hydrogen by contacting only the required amount of hydrogen-production substance with solution for reaction.    DETAILED DESCRIPTION - A hydrogen-production apparatus consists of a reaction chamber, a belt-shaped hydrogen-production substance supplier, and a movement unit. A solution for reaction for producing hydrogen by contacting with a hydrogen-production substance is stored in the reaction chamber. A preset amount of hydrogen-production substance is supplied by the supplier which is provided into two or more numbers in the longitudinal direction and arranged inside the reaction chamber. The hydrogen-production substance is immersed in the solution in the movement unit by moving the hydrogen-production substance supplier in the longitudinal direction. INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the principal portion of hydrogen-production apparatus.    Reaction chamber (2)    Solution for reaction (4)    Belt-shaped hydrogen-production substance supplier (7)    Conversion roll (16)    Hydrogen-production substance (18)
NOVELTY - A hydrogen-producing apparatus (1) comprises substance part provided with substance accommodating part which accommodates hydrogen-producing substance which reacts with solution for reaction and produces hydrogen, liquid storage part which stores solution for reaction, supporting part which holds substance part, external-force provision part which provides external force with respect to substance part and makes solution for reaction contact hydrogen-producing substance, and movement part to which substance part is made to provide external force to by moving supporting part.    USE - A hydrogen-producing apparatus for fuel cell system (claimed).    ADVANTAGE - Required amount of hydrogen can be produced exactly without requiring large-scale mechanism.    DETAILED DESCRIPTION - A hydrogen-producing apparatus (1) comprises substance part provided with substance accommodating part which accommodates hydrogen-producing substance which reacts with solution for reaction and produces hydrogen, liquid storage part which stores solution for reaction, supporting part which holds substance part, external-force provision part which provides external force with respect to substance part and makes solution for reaction contact hydrogen-producing substance, and movement part to which substance part is made to provide external force to by moving supporting part with respect to external-force provision part. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hydrogen- producing apparatus. (Drawing includes non-English language text).    Hydrogen-producing apparatus (1)    Reaction chamber (2)    Reaction container (3)    Hydrogen-producing part (4)    Feeding-out roll (5)
NOVELTY - A hydrogen gas filling apparatus comprises filling nozzle (6) which can be connected on vehicle-mounted hydrogen filling tank at the front-end of the hydrogen supply line (7) led-out from the liquid hydrogen storage container (1) in which the hydrogen supply line is mounted with booster pump (2), heat exchanger (3), flow regulating valve and flowmeter in order from the liquid hydrogen storage container side, and bypass line for hydrogen supply which is formed in the state which bypasses heat exchangers and flow regulating valve.    USE - Hydrogen gas filling apparatus for fuels used for vehicles such as fuel cell electric vehicle and hydrogen fueled engine motor vehicle.    ADVANTAGE - The apparatus can fill hydrogen gas to vehicle mounted hydrogen filling tank in a short time.    DETAILED DESCRIPTION - The hydrogen gas filling apparatus comprises filling nozzle (6) which can be connected on vehicle-mounted hydrogen filling tank at the front-end of the hydrogen supply line (7) led-out from the liquid hydrogen storage container (1) in which the hydrogen supply line is mounted with booster pump (2), heat exchanger (3), flow regulating valve and flowmeter in order from the liquid hydrogen storage container side, and bypass line for hydrogen supply which is formed in the state which bypasses heat exchangers and flow regulating valve. The bypass line for hydrogen supply is mounted with flow regulating valve and for cold fluids. An INDEPENDENT CLAIM is included for a hydrogen gas filling process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen station. (Drawing includes non-English language text.)    Liquid hydrogen storage container (1)    Booster pump (2)    Heat exchanger (3)    Filling nozzle (6)    Hydrogen supply line (7)
NOVELTY - The method involves providing processing chamber (2) in which material which is to be gasified is received. The processing chamber is provided with an inlet (5) and an outlet (6). A flow of hot gas (30) is received through the inlet. The hot gas is exhausted from processing chamber outlet. The velocity increasing units (20,21) are provided for temporarily increasing the velocity of the hot gas. The velocity of hot gas is increased temporarily which flows into the inlet from one velocity to another higher velocity.    USE - Method for gasifying and pyrolysing organic matter such as waste material containing organic content such as municipal or industrial waste, and other material containing organic matter.    ADVANTAGE - The efficiency of gasification and pyrolysis is increased. Improved agitation of material during a gasification process is obtained. The chamber and piston are provided for increasing the hot gas flow velocity through the holes in the inlet panel of the processing chamber, thus the gasification process is enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for gasifying and pyrolysing organic material.    DESCRIPTION OF DRAWING(S) - The drawing shows an isometric view of the gasification and pyrolysis apparatus.    Processing chamber (2)    Inlet of processing chamber (5)    Outlet of processing chamber (6)    Velocity increasing units (20,21)    Flow of hot gas (30)
NOVELTY - The method involves stirring and mixing carbon particles (10) and the resin material (20) of the powdered state having water-repellent property to make a supercritical fluid or a sub critical fluid. The mixed material of the carbon particle and resin material is coated on a base material while removing the supercritical fluid or sub critical fluid. The powder of the PTFE resin is used as a resin material of the powdered state.    USE - Method for manufacturing diffused layer used for manufacturing fuel cell (claimed) such as polymer electrolyte fuel cell mounted in motor vehicle.    ADVANTAGE - The diffused layer with excellent water repellent property can be achieved. The electric power generation performance of the fuel cell can be improved effectively. The gas diffusion property can be improved effectively. The gas permeability or the waste water property can be reduced effectively. The structure of the fuel cell is simple, so that manufacturing cost of the fuel cell can be reduced effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the manufacturing method of fuel cell.    Carbon particle (10)    Resin material (20)    Hole (23)    Element electrode assembly (50)    Catalyst layer (56)
NOVELTY - The method involves assembling sealing portion (50) to one surface of fuel cells (40), in temporary assembly process. The assembled sealing portion is laminated, in lamination process. The temporary-assembled sealing portion is positioned by space narrower than width (D2) of sealing portion, by pair of convex portion (44d1,44d2). The sealing portion is provided with shape to fit between convex portions in separator (44). The sealing portion is curved, and peripheral portion (50e) of sealing portion is fitted between convex portions, in temporary assembly process.    USE - Manufacturing method of fuel cell stack.    ADVANTAGE - Since the peripheral portion of the sealing portion can be fitted between the pair of convex portions, the sealing portion can be positioned precisely. Since the components required for the laminate can be decreased, the productivity of the fuel cell stack can be improved. The positional offset of the sealing portion in the lamination process can be prevented, as the separator is contacted with several seal convex portions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) separator;    (2) sealing portion; and    (3) fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic views illustrating the manufacturing process of the fuel cell stack. (Drawing includes non-English language text)    Fuel cell (40)    Separator (44)    Convex portions (44d1,44d2)    Sealing portion (50)    Peripheral portion (50e)    Width (D2)
NOVELTY - The fuel cell (28) equipped in the fuel cell stack (10) is heated. When the electromotive force produced from the fuel cell due to heating reaches the minimum electromotive force, and the temperature of the fuel cell stack reaches the rated-operation temperature after starting electric power generation of the fuel cell, heating of the fuel cell is stopped.    USE - Control method of fuel cell stack such as solid oxide fuel cell (SOFC) for fuel cell system used as portable power supply.    ADVANTAGE - The electric power generation efficiency of the fuel cell stack at the rated-operation temperature after starting electric power generation of the fuel cell is improved, and deterioration of an electrolyte-electrode assembly is prevented as much as possible, by stop heating the fuel cell if the electromotive force produced from the fuel cell reaches minimum value, and the temperature of the fuel cell stack reaches rated-operation temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic explanatory view of the mechanical-system circuit of the fuel cell system. (Drawing includes non-English language text)    Fuel cell stack (10)    Fuel cell module (11)    Fuel cell system (12)    Control apparatus (21)    Fuel cell (28)
NOVELTY - The cell has gas diffusion sheets (12, 14) diffusing hydrogen-containing-gas to an anode catalyst layer through a separator (20). Corrugation is formed in a separator surface. A hydrogen-containing-gas flow path is formed in a recessed part (22a). A coolant flow path is formed as a convex part (24). Carbon with low-crystallization degree is added to an electric power generation surface of the gas diffusion layer. Sacrificial oxidation area of the gas diffusion layer is formed such that a fixed angle is formed in extension direction of the hydrogen containing-gas flow path.    USE - Polymer electrolyte fuel cell.    ADVANTAGE - The cell suppresses carbon oxidation of the anode catalyst layer and strength reduction of the gas diffusion layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a polymer electrolyte fuel cell.    Gas diffusion sheets (12, 14)    Separator (20)    Recessed part (22a)    Convex part (24)    Porous body layer (34)
NOVELTY - The photovoltaic-, wind- and hydrogen power distribution system of a BRD, is claimed, where a conversion of natural gas in hydrogen for industrial requirement and uneconomical conversion of hydrogen in natural gas obtained form an excess solar energy are stopped. An imported natural gas is stored in summer so that it is available for power generation in winter, and is waived on a high-voltage network across the BRD. A number of required storage power plants is reduced. An excess voltaic energy is used to produce hydrogen for industrial requirements in summer.    USE - Used as a photovoltaic-, wind- and hydrogen power distribution system.    DETAILED DESCRIPTION - The photovoltaic-, wind- and hydrogen power distribution system of a BRD, is claimed, where a conversion of natural gas in hydrogen for industrial requirement and a uneconomical conversion of hydrogen in natural gas obtained form an excess solar energy are stopped. An imported natural gas is stored in summer so that it is available for power generation in winter, and is waived on a high-voltage network across the BRD. A number of required storage power plants is reduced. An excess voltaic energy is used to produce hydrogen for industrial requirements in summer. The stored natural gas in gas-fired power plants is used to generate electricity in winter. Another imported natural gas in the winter is converted in an industrial-hydrogen.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a photovoltaic-, wind- and hydrogen power distribution system of a BRD (Drawing includes non-English language text).
NOVELTY - Hydrothermal carbonization of solid or liquid biomass, comprises a pre-treatment of the biomass including providing a discrete amount of biomass in a closed pre-heating tank (30) within the first pre-treatment, carrying out a carbonation reaction by introducing resulting slurry into a closed reaction tank, and a post-treatment of the biomass including triggering the carbonation reaction of discrete amount of biomass present in the slurry contained in the reaction tank.    USE - The method is useful for hydrothermal carbonization of solid or liquid biomass.    ADVANTAGE - The method is a multi-batch process, in which all steps are carried out parallel to each other in separate tanks, thus it is simple and highly efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for hydrothermal carbonization of solid or liquid biomass comprising at least one installation for preheating, a reactor, and an apparatus for post-treatment, where a separate, closed pre-heating tank is provided for preheating, which is connected to at least a separate, self-contained reaction tank serving as a reactor, which is emptied into at least a separate, sealed buffer tank for subsequent treatment slurry resulting from the biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic perspective view of the device for hydrothermal carbonization of solid or liquid biomass.    Feed tank (10)    Feed pump (12)    Feed hopper (20)    Screw conveyor (21)    Pre-heating tank (30)
NOVELTY - The alcohol ether fuel comprises 88 wt.% of methanol, 7-8 wt.% of ether or dimethyl ether, 0.1-0.6 wt.% of isopropyl alcohol, 0.4-0.9 wt.% of n-butyl alcohol or isobutyl alcohol, 0.35-0.9 wt.% of carbonate, 0.3-0.6 wt.% of ethyl acetate, and 0.4-1 wt.% of methyl tertiary butyl ether.    USE - The alcohol ether fuel is useful as a raw material for coal and natural gas.    ADVANTAGE - The economical alcohol ether fuel exhibits excellent dynamic performance and strong water resistance, can be conveniently stored, and reduces the emission of harmful gas in the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing alcohol ether fuel.
NOVELTY - Anhydrous Linezolid crystalline Form-II having water content of less than 0.5 wt.%, is new.    USE - As anhydrous Linezolid crystalline Form-II (claimed), used as antibacterial agent.    ADVANTAGE - The method is reliable, convenient and easily reproducible on industrial scale and gives identical anhydrous crystalline form-II of Linezolid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing anhydrous Linezolid crystalline Form-II.
NOVELTY - Method for sanitizing waste product involves (a) subjecting waste to biological treatment under aerobic conditions that results in increase in temperature to produce treated and heated product, and (b) adjusting pH of treated and heated product to alkaline pH and incubating the product for sufficient period of time to eliminate or reduce concentration of pathogens in the waste.    USE - The method is useful for sanitizing waste product, where the sanitized product is used as fertilizers. The waste product is human excrements, animal excrements, sludge, greywater or biowaste (all claimed). The sanitized product is useful in agriculture and/or landscapes, and as soil conditioner.    ADVANTAGE - The method improves economical value, protects environment, conserves water, recycles recovered nutrients and organic matter, prevents diseases and promotes health, as it reuses waste product, reduces cost of importing fertilizers.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for sanitization of waste product and reuse of nutrients, comprising at least one aerobic reactor and optionally sanitization reactor, where the product is passed from at least one reactor into the sanitization reactor when the temperature exceeds 30 degrees C, and sanitization step is performed in sanitization reactor by adjusting the pH in sanitization reactor to at least 8, preferably 9, and most preferably 9; and    (2) use of sanitization reactor in the above system.
NOVELTY - The apparatus has transport unit which is equipped with membrane electrode assembly (10), which contains gas diffusion layer. The gas diffusion layer is assembled in the upper and lower part of the membrane electrode assembly. An electrode separator (40a,40b) and another transport unit is equipped with the fuel anode separator.    USE - Apparatus for manufacturing fuel cell.    ADVANTAGE - The apparatus has transport unit which is equipped with membrane electrode assembly, which contains gas diffusion layer, where gas diffusion layer is assembled in upper and lower part the membrane electrode assembly, and thus the apparatus is simple and improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus.    Membrane electrode assembly (10)    Folder (22a)    Electrode separator (40a,40b)    Support (110)    Decoupling-type laminate support (112)
NOVELTY - Potentiating enzymatic saccharification of a cellulosic biomass using a microbial enzyme cocktail comprises combining the microbial enzyme cocktail with at least one cellulase enzyme.    USE - The methods are used for potentiating enzymatic saccharification of a cellulosic biomass, and for producing fermentable sugars (all claimed).    ADVANTAGE - The use of the advantageous genetic of the transgenic plants and seeds can further be made in plant breeding. Depending on the desired properties, different breeding measures are taken. The transgenic seeds and plants can be used for the breeding of improved plant lines that, for example, increase the effectiveness of conventional methods of biomass processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of producing fermentable sugars.
NOVELTY - Method of burning raw material including biomass-based and waste-based raw material (3) in combustion reactor involves feeding raw material to firebox of combustion reactor, adding calcium carbonate (4) to firebox partially or completely, adjusting temperature and partial pressure of carbon dioxide during combustion such that calcination of calcium carbonate is hindered, maintaining content of calcium carbonate during combustion such that calcium carbonate forms reactive bonding with alkali metal-based substance, and removing unwanted alkali metal-based substance (7) from firebox.    USE - Method of burning raw material including biomass-based and waste-based raw material in combustion reactor.    ADVANTAGE - The method efficiently and economically burns raw material including biomass-based and waste-based raw material in combustion reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for raw material-burning apparatus, which comprises a combustion reactor (1) and feeding unit (2) for feeding the raw material to the firebox of the combustion reactor, feeding unit for feeding calcium carbonate to the firebox, adjusting unit (5), and unit (6) for conveying the unwanted alkali metal based substances out from the firebox by calcium carbonate.    DESCRIPTION OF DRAWING(S) - The drawing shows the structure of raw material-burning apparatus.    Combustion reactor (1)    Feeding unit (2)    Raw material (3)    Calcium carbonate (4)    Adjusting unit (5)    Unit for conveying the unwanted alkali metal-based substance (6)    Unwanted alkali metal-based substance (7)
NOVELTY - The apparatus (45) has photoelectric conversion unit (2) which is provided with light-receiving surface and a rear surface. The electrodes (4,5) are arranged on the rear surface side of the photoelectric conversion unit, when the sunlight is incident on the light-receiving surface of the photoelectric conversion unit. An electromotive force is utilized to electrolyze the electrolyte, such that hydrogen and oxygen are generated. The engagement unit is configured to adjust the orientation of the light-receiving surface of the photoelectric conversion unit toward sunlight.    USE - Hydrogen production apparatus used as water electrolysis apparatus.    ADVANTAGE - Since the electrodes are provided in the back surface side of the photoelectric conversion unit, the light can be entered in the light-receiving surface of the photoelectric conversion unit without the usage of the electrolyte solution, so that the absorption of incident light and scattering of incident light by electrolyte solution can be prevented. Hence, the quantity and the optical efficiency of the hydrogen production apparatus are improved. The installation place of the hydrogen production apparatus can be changed easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen production apparatus.    Translucent substrate (1)    Photoelectric conversion unit (2)    Electrodes (4,5)    Control unit (12)    Hydrogen production apparatus (45)
NOVELTY - Non-naturally occurring polyketide synthase (PKS) capable of synthesizing a trimethylpentanoic acid, is new.    USE - The non-naturally occurring polyketide synthase is useful in recombinant nucleic acid for synthesizing trimethylpentanoic acid, which is reduced to produce trimethylpentanol or isooctane (all claimed), where the isooctane are used as a fuel.    ADVANTAGE - The non-naturally occurring polyketide synthase reduces the dependence on oil for producing certain chemicals, and serves as a means for capturing and sequestrating carbon from the atmosphere.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a recombinant nucleic acid encoding the PKS;    (2) a replicon comprising the recombinant nucleic acid, where the replicon is capable of stable maintenance in a host cell;    (3) a host cell comprising the recombinant nucleic acid; and    (4) producing the trimethylpentanoic acid, comprising providing the host cell, and culturing the host cell in a suitable culture medium.
NOVELTY - The system (10) has two plates (20a, 20b) arranged within a reservoir tank (12), where a portion of each plate is in contact with a solution (14) of water and electrolyte in the reservoir tank. The plates are in electrical communication with an electrical power source (24), where the plates create electrical current in the solution to produce gas including oxygen and hydrogen. A filter system (70) is in fluid communication with the reservoir tank. A conduit (58) is in fluid communication with the filter system and utilized for delivering the gas to an internal combustion engine.    USE - Electrolysis system for supplementing supply of petroleum fuel of an internal combustion engine in a vehicle.    ADVANTAGE - The filter system captures electrolyte particles so as to reduce overall consumption of the electrolyte during utilization, thus reducing utilization of raw materials, reducing harmful gas emission and improving fuel combustion.    DETAILED DESCRIPTION - The electrolyte is potassium hydroxide. The filter is a glass-bonded silica air diffuser. An INDEPENDENT CLAIM is also included for a method for supplying hydrogen and oxygen to an internal combustion engine to supplement the engine's petroleum fuel supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a front elevational view of an electrolysis system.    Electrolysis system (10)    Reservoir tank (12)    Solution of water and electrolyte (14)    Plates (20a, 20b)    Electrical power source (24)    Conduit (58)    Filter system (70)
NOVELTY - The device (10) has an anode (14) and a cathode (16). An applied magnetic field is existed between anode and cathode. A divider (12) is provided to separate the anode from the cathode. A magnet is attached to the cathode. The magnetic material is selected from one of neodymium (Nd), iron (Fe), nickel (Ni), copper (Cu), chromium (Cr), gadolinium (Gd), yttrium (Y), lanthanum (La) or cobalt (Co). A low energy source is selected from one of the solar cell, wind turbine or a battery.    USE - Electrochemical device for generating hydrogen fuel gas, used in household appliances, toy and car. Can also be used in unmanned aircraft vehicle (UAV).    ADVANTAGE - The hydrogen fuel gas can be generated effectively, since applied magnetic field is existed between anode and cathode. The occurrence of contamination on hydrogen fuel gas can be prevented efficiently.    DETAILED DESCRIPTION - The device has anodes and cathodes that are arranged parallel to each other. The nano-particle layer and partial layer of anode are formed over the resurfaced surface. The electrolyte solution is selected from the group of sodium chloride, sodium hydroxide, sodium nitrate, potassium chloride, potassium hydroxide, sodium acetate, acetic acid or hydrogen peroxide. The negative polarity of magnetic field is arranged opposite to the anode. A positive polarity of magnetic field is arranged away from general direction of anode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas generating device.    Electrochemical device (10)    Chamber (11)    Divider (12)    Anode (14)    Cathode (16)
NOVELTY - Ferment, is claimed.    USE - The ferment is useful for strengthening plants, and for fermenting municipal sewage sludge.    ADVANTAGE - The ferment has a high antioxidant factor suitable for regenerating contaminated biomass, and reduces pollutants, preferably heavy metals, and radioactive contamination.
NOVELTY - Methane fermentation system comprises dissolution tank for producing a solution for decomposing organic waste using aerobic microbe, acid production tank, methane fermentation tank, safety valve, desulfurizing apparatus, connecting pipe and a cover container.    USE - The methane fermentation system is useful for converting waste food material into biogas.    ADVANTAGE - The system does not produce any odor and causes no malfunction.    DETAILED DESCRIPTION - Methane fermentation system (1) comprises dissolution tank (3) for producing a solution for decomposing organic waste using aerobic microbe, and dissolving organic substance, acid production tank (4) which decomposes the organic substance which is dissolved in the solution from the dissolution tank by acid production bacteria, and produces organic acid, methane fermentation tank (9) which ferments the organic acid from the acid production tank using methanogenic bacteria, and produces methane gas, safety valve (94) which is connected within the methane fermentation tank, and is operated when the internal pressure of the methane fermentation tank rises to a reference pressure, and internal pressure is reduced, desulfurizing apparatus (97), connecting pipe (96) which removes hydrogen sulfide contained in the methane gas which blew off from methane fermentation tank, and a cover container (95) for scattering prevention which seals and covers the outer side space of the safety valve.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of methane formation system.    Methane formation system (1)    Dissolution tank (3)    Acid production tank (4)    Supply tank (6)    Methane fermentation tank (9)    Safety valve (94)    Cover container (95)    Connecting pipe (96)    Desulfurization apparatus (97)
NOVELTY - The invention relates to an improved method for utilizing spent mushroom compost (so called "bulk bag") of white rot fungi to produce and purify ligninolytic enzymes. The invention further provides a use of the ligninolytic enzymes produced by the method of the invention for eliminating organic toxic organic compounds. The invention comprises steps of depositing cultured medium below 4 degrees Celsius to retain enzyme activity after gathering white rot fungi entities; performing vibration extraction for three hours to one day at 4 to 20 degrees Celsius through the medium and sodium acetate-acetic acid buffer in which buffer ratio is 1:5 to 1:25; and imposing centrifugal force for 15 minutes at 8000 rpm to obtain supernatant fluid, thereby acquiring enzyme extraction fluid.
NOVELTY - The method involves utilizing a flowing gas mixture with solids having predefined size distribution. Gas concentration in the flowing gas mixture is measured using an optical spectrometer (2) i.e. laser spectrometer, and a measurement beam of the optical spectrometer is guided by a measurement channel (3) during measurement. The solids comprising flame-hydrolyzed silica particles and concentration of oxygen in the flowing gas mixture are determined, and a gas-permeable material is selected from a group consisting of polymers, sintered ceramics, sintered metal and PTFE.    USE - Method for determining gas concentration in a flowing gas mixture i.e. solid-containing gas mixture, in an industrial plant (all claimed) in e.g. chemical industry and automobile industry.    ADVANTAGE - The method enables determining gas concentration in the flowing gas mixture in an effective manner and avoiding formation of ignitable gas mixtures.    DETAILED DESCRIPTION - The flowing gas mixture comprises gas that is selected from a group consisting of anhydrous ammonia, hydrogen chloride, chlorine, hydrogen fluoride, hydrogen sulfide, oxygen, carbon monooxide, carbon dioxide, nitric oxide, nitrogen oxides, nitrous oxide and methane. An INDEPENDENT CLAIM is also included for a device for determining gas concentration of a solid-containing gas mixture of an industrial plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for determining a gas concentration in a flowing gas mixture in an industrial plant.    Gas concentration determining device (1)    Optical spectrometer (2)    Measurement channel (3)    Filter tube (4)    Spectrometer accommodation (21)
NOVELTY - The method involves separating a hydrocarbon component mixed in water. The water is heated to generate water steam, such that the generated water steam is mixed with the hydrocarbon component to form a hydrocarbon vapor mixture. The mixture is heated to form hydrogen-containing gaseous fuel at particular temperature. The water stream is directed to a return path for ignition in a flame torch.    USE - Multi-stage method for obtaining hydrogen-containing gaseous fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas production device.
NOVELTY - The organic-inorganic mixed fertilizer comprises chicken manure peat mixture compost (55.5-64.5 wt.%) and inorganic fertilizer (35.5-44.5 wt.%). The inorganic fertilizer comprises carbamide (46.5 wt.%), ammonium dihydrogen phosphate (10 wt.%), potassium sulfate (52 wt.%), and phosphorus pentoxide (46 wt.%). A dry material weight ratio of the chicken manure and the peat is 2.7-2.8:1.    USE - The organic-inorganic mixed fertilizer is useful for tea tree.    ADVANTAGE - The organic-inorganic mixed fertilizer can be simply and economically prepared with high quality in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic-inorganic mixed fertilizer.
NOVELTY - A self-heating straw carbonization furnace comprises carbonization room with feeding hole and discharging hole. An inside of the carbonization room has an internal furnace and it is surrounded by external furnace. Smoke vents are between carbonization room and internal furnace and between carbonization room and external furnace. Air intake and air outlet are arranged in both internal and external furnaces. The internal or external furnace is combined with startup heater for providing start-up heat.    USE - A self-heating straw carbonization furnace.    ADVANTAGE - The furnace burns combustible gas that comes out of the carbonization process and lowers fuel consumption. Hot air exhaust is used as transfer gas to preheat the materials so that energy lost is lowered. By heating from both internal and external furnaces, the furnace improves the efficiency of energy utilization.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a self-heating straw carbonization furnace.
NOVELTY - A high temperature anaerobic cellulose decomposing strain Thermoanaerobacterium sp. L-D deposited as CCTCC NO. M208166, is new.    USE - The high temperature anaerobic cellulose decomposing strain Thermoanaerobacterium sp. L-D is useful for degrading rice straw and the degradation product is useful for culturing sulfate reducing bacteria. The method (M1) is useful for enriching and separating culture of anaerobic cellulose decomposing bacterial strain (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for enriching and separating culture of anaerobic cellulose decomposing bacterial strain; and    (2) method (M2) for degrading rice straw using cellulose decomposing microorganisms.
NOVELTY - System for mass culturing lipid oil using both Heterotrophic and Autotrophic techniques, thus reducing the land mass presently adopted, such as using ponds for commercial cultivation.    USE - The system is useful for mass culturing lipid oil using both Heterotrophic and Autotrophic techniques.    ADVANTAGE - The mass cultivation system will provide oil for the production of Bio fuels such as Biodiesel and Butanol and the ability to clean waste water reuse thus substantially reducing pollution of waterways in industry e. g. dairy farming. It does not have the problems that plague traditional systems, such as cross contamination, species bullying or variations of seasonal temperatures and daylight hours.
NOVELTY - Method of processing tall oil fatty acid stream comprising a first level of sulfur, comprises (a) esterifying the tall oil fatty acid stream with an alcohol to produce a tall oil fatty acid ester stream with a second level of sulfur less than the first level of sulfur, (b) distilling the tall oil fatty acid stream to recover a distillate stream having a third level of sulfur less than the second level of sulfur, and (c) saponifying and acidizing the distillate stream to provide a final tall oil fatty acid stream with a final level of sulfur less than the second level of sulfur.    USE - The method is useful for producing tall oil fatty acid or its derivative, which is useful as lubricity additives for ultra-low sulfur diesel (ULSD), and for the production of PVC additives or biodiesel.    ADVANTAGE - The method provides tall oil fatty acid or its derivative with low unsaponifiable tall oil species, low tall oil rosin content, and low sulfur content in an economical manner. The tall oil fatty acid provides lubricity additives with improved lubricity and low temperature properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for a fuel additive comprising: either a tall oil fatty acid and sulfur compound; or a hydrocarbon component, tall oil fatty acid methyl ester and sulfur compound, where the sulfur compound comprise fuel additive (15 ppm, 14 ppm, 13 ppm, 12 ppm, 11 ppm, 10 ppm, 9 ppm, 8 ppm, 7 ppm, 6 ppm, 5 ppm, 4 ppm, 3 ppm, 2 ppm, 1 ppm, 0.1 ppm and/or 0.01 ppm).
NOVELTY - Preparing a catalyst comprises spraying a slurry containing a particulate catalyst compound comprising catalytic metals including nickel, copper, platinum, palladium, rhodium, ruthenium or gold, on to the surface of a shaped support in a pan coater to form a coated shaped support material having the catalytic metal in a surface layer, drying and optionally calcining the coated shaped support material to form a catalyst precursor, and optionally reducing the metal or metals in the catalyst precursor to a lower oxidation state to form the catalyst.    USE - The method is useful for preparing a catalyst, which is useful in a steam reforming process including steam reforming a hydrocarbon such as natural gas, naphtha, a liquid fuel or a gasifier effluent (all claimed), coal- or biomass-gasifier effluents to reform methane and higher hydrocarbons, including tars into gas streams.    ADVANTAGE - The method provides catalyst in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the catalyst obtainable by the method; and    (2) performing a steam reforming reaction using the catalyst.
NOVELTY - A supply of whole stillage is obtained (202) from an ethanol production facility after extracting ethanol. The whole stillage is pretreated (204) to convert hemicellulose portions of whole stillage into sugars. Enzymes are added (206) to the whole stillage to convert cellulose portions of the whole stillage to sugars. The whole stillage is fermented (208) to create a beer mixture and the beer mixture is distilled (210) to separate ethanol.    USE - Manufacture of ethanol used as gasoline additive or straight liquid fuel.    ADVANTAGE - The ethanol is economically manufactured.
NOVELTY - The chamber (100) has an oxidation and reduction region (142) which is provided below pre-heating region (140). Oxidation and reduction region has steam plasma torches (126) coupled to annular ring distributor (128). Gas outlet region (143) has half annular ring distributor (135) which is coupled to air plasma torch (134). Gas outlet region (143) has half annular ring collector (136) having apertures and gas outlet port for removing combustible gasses produced inside enclosed volume. Solids offloading zone (144) is provided below unloading region, for removing ash and slag.    USE - Top-loading plasma pyrolysis chamber for extracting combustible gasses from heterogeneous organic materials such as wood chip, municipal refuse, biomass, agriculture waste, wood chip, forest product processing waste, hazardous waste, petroleum coke, coal and oil shale.    ADVANTAGE - As the solids offloading zone is provided below unloading region for removing ash and slag, the improved pyrolysis chamber with increased internal operating temperature and resultant efficiency without the use of oxygen enriched air can be provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for extracting combustible gasses from fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the plasma pyrolysis chamber.    Pyrolysis chamber (100)    Steam plasma torches (126)    Annular ring distributor (128)    Air plasma torch (134)    Half annular ring distributor (135)    Half annular ring collector (136)    Pre-heating region (140)    Oxidation and reduction region (142)    Gas outlet region (143)    Solids offloading zone (144)
NOVELTY - The biological liquid organic fertilizer comprises 38-44% of biogas slurry, 40-54% of biogas residue and 6-12% of beneficial microflora. The biogas slurry is animal dung and straw. The beneficial microflora is Lactobacillus, Bacillus and saccharomycetes.    USE - Used as a biological liquid organic fertilizer.    ADVANTAGE - The economical biological liquid organic fertilizer reduces alkalinity of the soil, improves air permeability, makes the crops to grow uniform and vigorous, increases yield and quality and ensures safety of the food.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a biological liquid organic fertilizer.
NOVELTY - Preparation of high-efficiency compound biological probiotics comprises screening single probiotic strain, subjecting single probiotic strains to slope activation and shake flask liquid propagating, and obtaining single probiotic strains; and adjusting proportion of every single probiotic strain, mixing to obtain probiotic flora, and obtaining compound primary strain, and obtaining high-efficiency compound biological probiotics.    USE - Method of preparation of high-efficiency compound biological probiotics used for treating livestock breeding waste material (claimed), and for producing fertilizer and treating domestic garbage.    ADVANTAGE - The probiotics is safe, and has strong environmental adaptation, strong bioactivity, and anti-interference ability.
NOVELTY - A straw compressed fuel is formed by pressing straw and starch glue at a pressing pressure of 1-1.5 MPa.    USE - A straw compressed fuel for a fuel-saving furnace.    ADVANTAGE - The fuel is environment-friendly, increases burning time, is toxic-free and flavorless, improves burning efficiency, and does not scatter.
NOVELTY - Improving biological oil quality comprises mixing biological oil with acetic anhydride and solid alkali, heating and refluxing to obtain biological oil after catalyzing and extracting, and performing normal pressure distilling of catalyzed and extracted biological oil, removing the cut fraction less than 120 degrees C, and gathering 120-250 degrees C cut fraction to obtain the refined biological oil.    USE - Method for improving biological oil quality (claimed).    ADVANTAGE - The alcohol is unnecessary to be added in large amount; but little carboxylic acid glycoside is added so that the biological oil is extracted by catalyzing; and the biological oil stability is improved after refining.
NOVELTY - Method for fermenting solid waste and producing biogas involves air drying solid waste until its water content reaches 1% or less and crushing the air dried solid waste, mixing the pre-treated solid waste with biogas slurry and obtaining mixture, where mass of the solid waste to the added biogas slurry is 15-90%, stirring the mixture uniformly, adjusting pH of mixture to 6.8-7.4, fermenting the mixture containing water content of 10-40% at -2.5 to 2.5 V and 10-55 degrees C, and collecting biogas.    USE - The method is useful for fermenting solid waste chosen from solid waste collected from city, animal manure, crop straw and their mixtures, and producing gas (claimed).    ADVANTAGE - The method is simple, enable to biodegrade lignocellulose and carry out fermentation at low temperature. The method produces biogas continuously.
NOVELTY - Use of Iris tectorum in purifying animal breeding biogas slurry, where the Iris tectorum is planted in the animal breeding biogas slurry polluted environment, is claimed.    USE - The Iris tectorum is useful in purifying animal breeding biogas slurry, and treating waste water.    ADVANTAGE - The Iris tectorum prevents secondary pollution, and ensures simple and feasible operation with low operation cost.
NOVELTY - The device has a kiln tail smoke chamber (1) that is mounted at side end of a cement kiln (2). A cooler (4) is arranged at other side end of the cement kiln. A triple-air pipeline (3) is arranged between cooler and kiln tail smoke chamber. A mixing chamber (5) is mounted at side end of the kiln tail smoke chamber. A cold air draught fan (11) is mounted at upper end of the mixing chamber through a connection pipeline.    USE - Device for producing cement and kiln ash potassium fertilizer.    ADVANTAGE - The cement and kiln ash potassium fertilizer can be manufactured effectively. The production efficiency of kiln ash potassium fertilizer can be improved. The working efficiency of cement producing device can be improved. The utilization ratio of cement and kiln ash potassium fertilizer can be improved. The cement producing device is environment-friendly. The production cost of cement and kiln ash potassium fertilizer can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing cement and kiln ash potassium fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing cement and kiln ash potassium fertilizer.    Kiln tail smoke chamber (1)    Cement kiln (2)    Triple-air pipeline (3)    Cooler (4)    Mixing chamber (5)    Cold air draught fan (11)
NOVELTY - Ecological liquid raw material comprises (pts.wt.) plant ash (43-68), bean dregs (19-25), human urine (30-40), waste saw dust (50-60), halogen alkali (22-26), and dry moss (rolled into powder) (16-20) based on 200 pts.wt. proportion.    USE - Ecological liquid raw material used for landscape restoration.    ADVANTAGE - The ecological liquid raw material provides surface wettability via natural precipitation, thus rock mass generates green moss and plants.
NOVELTY - The system has a solar photo-thermal integrated component (1) which comprises a solar heat collector located at the back and front face of the solar energy battery. A hot water storage tank (4b) is provided with the solar energy photo-thermal integrated component. The solar heat collector is provided for collecting heat energy. The fuel cell electric energy generated by the photo-thermal integrated component is stored in the storage system (6). The water storage tanks (4a,4b) are selectively connected with evaporating and condensing ends of the heat pump (5).    USE - Solar combined heat power system.    ADVANTAGE - The usage of the electricity can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the solar combined heat power system. (Drawing includes non-English language text)    Solar photo-thermal integrated component (1)    Heat terminal (2)    Hot water storage tank (4a,4b)    Heat pump (5)    Storage system (6)
NOVELTY - The stove has an ash chamber connected with a lower furnace core and a furnace core. An ash room is arranged on a side by a fire stove head, and a bin body comprises an upper opening and lower opening. A stove core comprises a throat opening connected below a storage bin body, and the throat opening is provided with a surrounding gathering air nozzle. The air nozzle includes a side provided with an air inlet. A water tank is provided with a spiral fin and a furnace core. The ash room is provided with a waste heat furnace.    USE - Household biomass energy saving stove.    ADVANTAGE - The stove has high practical value, convenient usage, energy-saving and environment-friendly property, and avoids secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a household biomass energy saving stove.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a household biomass energy saving stove.
NOVELTY - The furnace has a furnace body provided with a main body (2), a heating inner container (5) and a biomass semi-gasification combustion furnace (9). The heating inner container and a biomass semi-gasification combustion furnace inner container (8) are fixed on the main body. The biomass semi-gasification combustion furnace is fixed with the heating inner container that is provided with multiple water pipes (19). Hot air generated by the biomass semi-gasification combustion furnace is passed via an annular air channel (23). The heating inner container is connected with a gas inlet (24).    USE - Biomass hot water furnace.    ADVANTAGE - The furnace ensures high heat energy utilization ratio and saves energy, and is environment-friendly. The combustion furnace inner container is convenient to change.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass hot water furnace.    Main body (2)    Heating inner container (5)    Biomass semi-gasification combustion furnace inner container (8)    Biomass semi-gasification combustion furnace (9)    Water pipes (19)    Annular air channel (23)    Gas inlet (24)
NOVELTY - The method involves providing an irradiation bag with a chloramphenicol casing. Front and rear automatic turn over parts and a suspension chain are arranged in the irradiation bag. The suspension chain is provided with a speed electric parameter, where frequency range of the speed electric parameter is 12-24HZ.    USE - Intestine chloramphenicol degradation and irradiation method.    ADVANTAGE - The method enables reducing processing cost and economic loss, effectively avoiding bad influence of external environment condition, protecting sausage casing color, improving production and radiation efficiency and ensuring convenient operation, high tensile strength and shear strength.
NOVELTY - The device comprises a film breaking device for processing the mixture of organic sludge and organic component, an anaerobic sludge bed, and a solid-liquid separating device. The breaking device is ultrasonic breaking device or microwave breaking device. The solid-liquid separation device is a plate filter press, a frame filter press, a belt filter press or a centrifugal dehydrator.    USE - The device is useful for processing food waste and organic sludge for producing organic fertilizer.    ADVANTAGE - The device is capable of easily processing food waste and organic sludge with high efficiency thus effectively producing the organic fertilizer in an environmentally-friendly manner.
NOVELTY - The furnace has a furnace body whose side is arranged with an interlayer. The interlayer is provided with a heat conducting oil inlet. The interlayer is connected with an oil outlet. A lower part of the furnace body is provided with a methanol steam inlet and equipped with a discharging port. A top part of the furnace body is provided with a methanol steam outlet and a feeding port.    USE - Efficient biological oil reaction furnace.    ADVANTAGE - The furnace has simple structure and high production efficiency. The furnace saves energy and reduces production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of an efficient biological oil reaction furnace.
NOVELTY - The furnace has a furnace body whose inner side is provided with a storage hopper (3). The storage hopper is provided with a feeding port at an upper part of a storage bin. A bin cover (1) is provided with a combustion area. A grate (9) is fixed on a burning gasification area and an ash bin (10). An air pre-heating chamber (14) is connected with a combustion section of a hot air inlet (15). An upper smoke pipe (16) is connected with cyclone dust collectors (17). The cyclone dust collectors are provided with a draught fan. The cyclone dust collectors are connected with a gas-water separator.    USE - Down suction-type biomass fuel gasification furnace.    ADVANTAGE - The furnace is simple in structure and convenient to use. The furnace improves gas heating and cleanness ranges of a tar content of about less than 10 mg/m3 under a standard state so as to improve heating efficiency of a biomass energy utilization system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a down suction-type biomass fuel gasification furnace.    Bin cover (1)    Storage hopper (3)    Grate (9)    Ash bin (10)    Air pre-heating chamber (14)    Hot air inlet (15)    Upper smoke pipe (16)    Cyclone dust collectors (17)
NOVELTY - Fixed bed anaerobic digestion marsh gas reaction device comprises upflow anaerobic sludge bed (12), where a reaction chamber of the upflow anaerobic sludge bed is provided with a fixed carrier (3).    USE - The fixed bed anaerobic digestion marsh gas reaction device is useful for degrading organic matter.    ADVANTAGE - The device effectively degrade organic matter, improves methane yield, has improved stability and high load of reactor operation impact.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fixed bed anaerobic digestion marsh gas reaction device.    Fixed carrier (3)    Sampling port (5)    Overflow port (7)    Upflow anaerobic sludge bed (12)
NOVELTY - Humic acid and fertilizer are prepared from papermaking black liquor by performing strong chemical oxidation degradation on papermaking black liquor, then separating after acidification to obtain humic acid solution and precipitate, mixing precipitate and residue material of papermaking raw material, and adding activated sludge to prepare solid organic fertilizer, or adding inorganic fertilizer to prepare organic/inorganic complex fertilizer.    USE - Method of preparing humic acid and fertilizer from papermaking black liquor (claimed).    ADVANTAGE - The method can realize clean utilization of waste resource by completely using papermaking black liquor, thus eliminating pollution caused by the black liquor and converting it into humic acid with high added value.
NOVELTY - The generator has a plastic container that is provided with upper and lower opening portions. A lid is arranged in the plastic container. The area of plastic container is divided into several areas. The areas of plastic container are intersected with each other.    USE - Plastic biogas generator.    ADVANTAGE - The plastic biogas generator can be dismantled effectively. The sealing property and compressive capacity of plastic biogas generator can be improved efficiently. The sun protection effect of plastic biogas generator can be improved. The service life of plastic biogas generator can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plastic biogas generator.
NOVELTY - A 9-(4-(2-(tetrazole-5-yl)phenyl)benzyl)-substituted theophylline compound is new.    USE - A 9-(4-(2-(tetrazole-5-yl)phenyl)benzyl)-substituted theophylline compound for medicine preparation.    ADVANTAGE - The preparation is simple and easy to operate. There are a few organic solvents. The environmental pollution is small and the raw materials are easy to get.    DETAILED DESCRIPTION - New 9-(4-(2-(tetrazole-5-yl)phenyl)benzyl)-substituted theophylline compound is of formula (I).    R=-H, -Cl, -CH3, -CH2CH3, or -CH2CH2CH3.    An INDEPENDENT CLAIM is included for a method for preparation of 9-(4-(2-(tetrazole-5-yl)phenyl)benzyl)-substituted theophylline compound.
NOVELTY - Polyhydroxyalkanoate is synthesized by taking residual sludge fermentation liquid as substrate, pouring city aerobic active sludge into a sludge acclimation device, adding culture medium aqueous solution, performing aerobic aeration, and acclimating to obtain acclimated active sludge; putting city residual sludge into a reactor, adding sodium hydroxide to perform hot alkali pretreatment, then anaerobic fermenting, and separating volatile fatty acid from fermentation liquid; and reacting acclimated active sludge with volatile fatty acid in sodium acetate as external carbon source.    USE - Method of synthesizing polyhydroxyalkanoate (claimed).    DETAILED DESCRIPTION - Synthesis of polyhydroxyalkanoate comprises:    (A) taking residual sludge fermentation liquid as substrate, pouring city aerobic active sludge into a sludge acclimation device, adding culture medium aqueous solution, performing aerobic aeration, mud sedimentation, discharging water, and continuously acclimating for 18-22 cycles to obtain stable acclimated active sludge;    (B) putting city residual sludge into a reactor, then adding sodium hydroxide to perform hot alkali pretreatment, adjusting pH to neutral, then inoculating anaerobic sludge, stirring and anaerobic fermenting, and separating volatile fatty acid from fermentation liquid; and    (C) putting the acclimated active sludge into a synthesis reactor, then adding the volatile fatty acid into the reactor, adjusting pH to neutral, and under condition of intermittent aeration, adding sodium acetate as external carbon source and reacting to synthesize polyhydroxyalkanoate.
NOVELTY - Producing methane by garbage, comprises performing pre-treatment for the garbage; putting the garbage into the garbage filling region; putting materials underwent hydrolytic acidification into microorganism bacterium agent filling region and performing methane generation reaction under the function of the microorganism bacterium agent; flow out of the microorganism bacterium agent filling region and return to the garbage filling region and mixing the same with the original materials in garbage filling agent; and performing circulation to continuously convert the garbage to be the methane.    USE - The process is useful for producing methane.    ADVANTAGE - The process is easy in rancidity, long in gas generation starting time, low in gas generation rate and gas generation speed, can realize the purpose of greatly quickening the gas generation process of the easy-rancidity garbage by a little fungicide, improves the gas generation rate of the garbage, reduces the amount of the residue and the waste liquid, and reduces the capacity of the reaction and the running cost.    DETAILED DESCRIPTION - Producing methane by garbage, comprises (a) performing pre-treatment for the garbage; (b) putting the garbage into the garbage filling region for hydrolytic acidification; (c) putting materials underwent hydrolytic acidification into microorganism bacterium agent filling region and performing methane generation reaction under the function of the microorganism bacterium agent; (d) flow out of the microorganism bacterium agent filling region and return to the garbage filling region, sequentially performing hydrolytic acidification and mixing the same with the original materials in the garbage filling agent; and (e) performing circulation for many times to continuously convert the garbage to be the methane and raising the ratio of the methane gas in the methane till further converting the garbage to be the methane.
NOVELTY - A medical embolism microsphere, comprises polycaprolactone as the raw material, where the microsphere is in a shape of ball, the interior is opened with holes, where the diameter of the microsphere is 200-300 microns, and it is stable in the pure water.    USE - For tumor treatment (claimed).    ADVANTAGE - The medical embolism microsphere is stable in the pure water; has drug loading rate to the ibuprofen of 12%; has good biocompatibility; and is completely nontoxic to human body. The degradation test shows that the degradation of the microsphere in the buffer solution (HBS) of pH 1.2 for one week is less than 5%, degradation of the microsphere in the buffer solution (PBS) of pH 7.4 for one week is 10%. The method of preparing medical embolism microsphere is simple, easy to industrial production with low cost and no environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing medical embolism microsphere involving dissolving polycaprolactone in 14% dichloromethane as the oil phase, blending the oil phase with the water solution of the sodium oleate at high speed for forming water-in-oil (w/o) emulsion; adding the emulsion in polyvinyl alcohol solution with certain concentration and blending for forming water-in-oil-in-water (w/o/w) complex phase emulsion; blending for a period of time and controlling the temperature at 43 degrees C, and evaporating the dichloromethane to obtain the microsphere.
NOVELTY - Preparing taxifolin monomer from Engelhardia roxburghiana leaf comprises crushing or cutting the dried E. roxburghiana leaf, adding solvent to extract, and concentrating the extract into paste; adding buffer liquid to the paste to suspend or dissolve, and adding enzyme to process enzymolysis; removing the impurities in the enzymolysis liquid alcohol, obtaining upper clear liquid or filtrate, concentrating and purifying the upper clear liquid or filtrate to obtain the taxifolin crude product; and recrystallizing the taxifolin crude product.    USE - The taxifolin monomer is useful for preventing and treating fatty liver (claimed).    ADVANTAGE - The method: directly carries out enzymolysis of E. roxburghiana wall leaf extract; has strong reaction specificity, high conversion rate, and simple and feasible process; causes less pollution, and is suitable for large scale industrial production; and overcomes the disadvantages of large destructive effect to aglycone, and device corrosion.    DETAILED DESCRIPTION - Preparing taxifolin monomer from Engelhardia roxburghiana leaf comprises: (i) crushing or cutting the dried E. roxburghiana leaf, adding solvent to extract, and concentrating the extract into paste; (ii) adding buffer liquid (30-100 ml) with given pH to the paste to suspend or dissolve, and adding enzyme to process enzymolysis at given temperature; (iii) removing the impurities in the enzymolysis liquid alcohol, obtaining upper clear liquid or filtrate, concentrating the upper clear liquid or filtrate until no alcohol exists, and purifying the upper clear liquid or filtrate to obtain the taxifolin crude product; (iv) recrystallizing the taxifolin crude product to obtain the taxifolin monomer with purity of greater than 99%.
NOVELTY - A biological diesel pour point depressant comprises 3-30 wt.% alpha -hydroxy polyester compound; and 70-97 wt.% polymethylacrylate.    USE - Diesel pour point depressant useful for base oil (claimed).    ADVANTAGE - The diesel pour point depressant has good depression effect in cold filter point.    DETAILED DESCRIPTION - A biological diesel pour point depressant comprises 3-30 wt.% alpha -hydroxy polyester compound of structure (I); and 70-97 wt.% polymethylacrylate of structure (II).    R1=1-22C alkyl;    R2=H or CH3;    R3=H or 1-6C alkyl;    R4,R5=H or CH3;    n=1-100;    R6=1-22C alkyl;    R7=H or CH3; and    m=1-100.    An INDEPENDENT CLAIM is included for preparing a biological diesel pour point depressant comprises:    (A) providing alkyl methacrylate and/or alkyl acrylate, ester compound or other oxygen-containing groups of alpha -hydroxy of ester compound, and diluent, initiator, and/or chain transfer agent with nitrogen gas at 30-180 degrees C for 1-24 hours and at 0.1-1 MPa to form polymethacrylate and/or polyester composition;    (B) feeding a reaction mixture comprising 10-70 wt.% alkyl methacrylate and/or alkyl acrylate and 10-30 wt.% ester compound, alkyl or alkyl acrylate monomer is 1-30C alkyl; and    (C) adding diluting agent of 0-200 wt.% reaction mixture and initiator into the reaction mixture which is 0.01-3 wt.% of chain transfer agent.
NOVELTY - The culture medium comprises 25 g/L of glucose, 40 g/L g/L of soybean meal, 2 g/L of monopotassium phosphate, 1 g/L of calcium carbonate, 0.0051 g/L of ferrous sulfate, 0.0005 g/L of manganese chloride, and 50 g/L of phytosterol. The substances are dissolved or dispersed in water. The fermentation culture medium has a pH of 7.2.    USE - The culture medium is useful for transforming phytosterol into androstadienedione using microorganism.    ADVANTAGE - The culture medium is capable of transforming the phytosterol into androstadienedione with high efficiency and less energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for transforming phytosterol into androstadienedione using microorganism.
NOVELTY - A farnesol is synthesized by reacting geraniol(E)-3,7-dimethyl-2,6-octadiene-1-alcohol, dimethyl sulfide and N-chlorosuccinimide in dichloromethane to obtain geranyl chloride; reacting geranyl chloride and ethyl acetoacetate to obtain geranyl ethyl acetoacetate under the presence of potassium carbonate, adding sodium hydroxide, heating and decarboxylation to obtain geranyl acetone; and reacting geranyl acetone with acetylene under the presence of inorganic base to obtain (E)-3,7-11-trimethyl dodecane-6,10-diene-1-alkyne-3-alcohol.    USE - Method for the synthesis of farnesol (claimed).    ADVANTAGE - The method has low cost, safe reaction route, environmental protection and obtains high purity products.    DETAILED DESCRIPTION - Synthesis of farnesol comprises:    (A) reacting geraniol(E)-3,7-dimethyl-2,6-octadiene-1-alcohol, dimethyl sulfide and N-chlorosuccinimide in dichloromethane to obtain geranyl chloride;    (B) reacting geranyl chloride and ethyl acetoacetate to obtain geranyl ethyl acetoacetate under the presence of potassium carbonate, adding sodium hydroxide, heating and decarboxylation to obtain geranyl acetone;    (C) reacting geranyl acetone with acetylene under the presence of inorganic base to obtain (E)-3,7-11-trimethyl dodecane-6,10-diene-1-alkyne-3-alcohol;    (D) reacting (E)-3,7-11-trimethyl dodecane-6,10-diene-1-alkyne-3-alcohol and acetic anhydride to obtain (E)-3,7-11-trimethyl dodecyl-6,10-diene-1-alkyne-3-acetic ester under acid catalysis;    (E) rearranging (E)-3,7-11-trimethyl dodecyl-6,10-diene-1-alkyne-3-acetic ester under the presence of silver salt catalysis to obtain (E)-3,7-11-trimethyl-1,2,6,10-tetraalkenyl acetic ester;    (F) hydrolyzing (E)-3,7-11-trimethyl-1,2,6,10-tetraalkenyl acetic ester under the presence of inorganic base aqueous solution to obtain farnesal; and    (G) farnesal deacidizing into farnesol by using sodium borohydride in carbinol.
NOVELTY - Use oil angle and saponin hydrogen fatty alcohol device comprises ester exchange reactor, rectifying tower, high pressure heat exchanger, high-pressure heater, fixed bed reactor, hydrogen separator and alcohol rectifying tower; high-pressure heat exchanger to top part provided with material inlet; and fixed bed reactor at bottom and top respectively provided with reaction inlet and outlet, reaction outlet connected with high-pressure heat exchanger to heat medium inlet, hydrogen inlet of hydrogen separator connected with heating medium outlet.    USE - Use oil angle and saponin hydrogen fatty alcohol device.    ADVANTAGE - The device saves production energy consumption and has low cost.    DETAILED DESCRIPTION - Use oil angle and saponin hydrogen fatty alcohol device comprises ester exchange reactor, rectifying tower, high pressure heat exchanger, high-pressure heater, fixed bed reactor, hydrogen separator and alcohol rectifying tower; high-pressure heat exchanger to top part provided with material inlet, bottom provided with material outlet, side wall provided with heating medium inlet and heating medium outlet; and fixed bed reactor at bottom and top respectively provided with reaction inlet and outlet, the top and bottom of the hydrogen separator provided with hydrogen outlet and outlet, side wall provided with hydrogen inlet, reaction outlet connected with high-pressure heat exchanger to heat medium inlet, hydrogen inlet of hydrogen separator connected with heating medium outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the use oil angle and saponin hydrogen fatty alcohol device.
NOVELTY - Hydrogen production involves combusting biomass with oxygen to produce carbon dioxide gas. The produced gas is introduced into a furnace containing charcoal on top biomass to produce carbon monoxide gas. The obtained carbon monoxide is reacted with water to obtain hydrogen gas. The produced hydrogen and carbon dioxide are passed through a bed of calcium oxide to form calcium carbonate.    USE - Method for producing hydrogen from biomass and charcoal (claimed) used as fuel and for generating electricity.    ADVANTAGE - The method efficiently stores thermal energy from biomass without loss of hydrogen production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of hydrogen production plant.    Biomass plant (1)    Calcium carbonate filter (2)    Charcoal oven (3)    Water pipe (4)    Reactor (6)
NOVELTY - A propylene and propane removing method involves absorbing catalytic cracking dry gas continuously entering an absorption tower for obtaining product gas removing heavy component. Pressure of the absorption tower is changed to normal pressure from the intermediate pressure to obtain intermediate gas. Recombinant is obtained from absorbent of the heavy component gas as replacement gas under vacuum condition. Desorption process is performed in the tower to absorb pressure. Circulation adsorption process is performed by using pressurized gas. Pressure swing adsorption cycle is completed.    USE - Method for removing propylene and propane in catalytic cracking dry gas.    ADVANTAGE - The method enables increasing yield of ethylene by 95%.    DETAILED DESCRIPTION - A propylene and propane removing method involves absorbing catalytic cracking dry gas continuously entering a loading adsorbent fixed absorption tower for obtaining product gas removing heavy component. Absorption process is completed in the absorption tower at intermediate pressure by utilizing a low-concentration recombinant in pressing process. The pressure of the absorption tower is changed to normal pressure from the intermediate pressure to obtain intermediate gas from the adsorption tower. Displacing gas and absorbed residual ethylene in the adsorption tower are removed. Recombinant is obtained from adsorbent of the heavy component gas as replacement gas under vacuum condition. Desorption process is performed in the absorption tower to absorb pressure. Circulation adsorption process is performed by using pressurized gas. Pressure swing adsorption cycle is completed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for removing propylene and propane in catalytic cracking dry gas. '(Drawing includes non-English language text)'
NOVELTY - Producing a catalyst material, involves hindering reaction rate of a displacement reaction to control formation of platinum clusters, where an atomic layer of metal atoms is displaced with platinum atoms, to produce a catalyst material that includes an atomic layer of the platinum atoms.    USE - The method is useful for producing catalyst material for electrochemical reactions within fuel cell for generating electric current.    ADVANTAGE - The produced catalyst material has uniform atomic layer of platinum atoms.    DETAILED DESCRIPTION - Method for producing a catalyst material, involves (a) hindering reaction rate of a displacement reaction to control formation of platinum clusters, where an atomic layer of metal atoms is displaced with platinum atoms, to produce a catalyst material that includes an atomic layer of the platinum atoms, (b) displacing an atomic layer of metal atoms with platinum atoms in the presence of a surfactant to produce a catalyst material that includes an atomic layer of the platinum atoms, or (c) (i) providing a particle that includes a metal core that is covered with an atomic layer of metal atoms, (ii) providing a solution that includes a surfactant and a platinum salt, and (iii) treating the particle with the solution to displace the metal atoms with platinum atoms from the solution and produce a catalyst material.
NOVELTY - Mechanical or mechanochemical treatment of biomass, comprises compacting a mixture containing the biomass by pressing it through the openings of at least one compactor at least one time.    USE - The process is useful: for mechanical or mechanochemical treatment of biomass, which is a lignocellulosic biomass comprising dissolving pulp, mechanical mass, spruce chips or reed canary grass, or optionally from birch, aspen, poplar, alder, Eucalyptus or Acacia, or agricultural residues, grasses, straw, leaves, bark, seeds, hulls, flowers, vegetables or fruits from materials, such as cotton, corn, wheat, oat, rye, barley, rice, flax, hemp, Manila hemp, sisal hemp, jute, ramie, kenaf, bagasse, bamboo or reed; as a pre-treatment of biomass to precede an enzymatic total hydrolysis of the biomass to produce carbohydrates; and for producing ethanol from the carbohydrates (all claimed).    ADVANTAGE - The process: can be operated in a continuous manner by using more than one compactor and more than one compacting cycle, thus the multiple compactors are operated sequentially; requires the use of minimal amounts of solvents and thus the process can easily be scaled up to industrial scales in an environmentally friendly manner at low temperatures, low pressures and during short/limited periods of time; and provides an energy-efficient and cost-effective manner of manufacturing ethanol or other similar chemicals, and thus, the process can be used not only in dry processing methods, but also in joined enzymatic and dry-processing methods.
NOVELTY - A catalyst comprises oxygen-doped graphene.    USE - Catalyst is used for producing hydrogen peroxide, and forming layers of electrodes used for oxygen reduction reaction at cathode of cells, such as fuel cells e.g. proton-exchange membrane fuel cells (all claimed), and metal-air batteries. Uses include but are not limited to stationary or portable power sources, electric vehicles, transport industries, phones, cameras, music players, game devices, navigation devices, prosthetic devices, and portable computers.    ADVANTAGE - The catalyst has excellent tolerance with respect to methanol crossover effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell;    (2) method of reducing oxygen;    (3) use of oxygen-doped graphene as catalyst for oxygen reduction reaction; and    (4) production of hydrogen peroxide.
NOVELTY - The apparatus has a water supply device (1) that comprises relief valves and level sensor, and supplies water to a hydrogen generator (2) generating compound of oxygen and hydrogen from water. The supplied water is directly transported to a boiler (3) burning the compound of oxygen and hydrogen. A control unit (4) is connected to the hydrogen generator, such that heat is produced after immediately burning all the produced compound of oxygen and hydrogen produced in the hydrogen generator.    USE - Apparatus for production of heat and electrical energy from water, used in organic Rankine cycle (ORC) system.    ADVANTAGE - The apparatus can be advantageously used for obtaining heat and electrical energy for retail customers without need of storing the compound of hydrogen and oxygen, and without need of long distributions obtained from the apparatus to the customer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the apparatus for production of heat and electrical energy from water.    Water supply device (1)    Hydrogen generator (2)    Boiler (3)    Control unit (4)
NOVELTY - The fluidized bed boiler (100) comprises a unit (210) for heating a heat transfer medium (212), a unit for transferring the heat transfer medium to a torrefaction reactor, a unit for receiving the heat transfer medium from the torrefaction reactor, a heat exchanger (118) for heating torrefaction gases to be used in the torrefaction reactor, a bed material, a bed channel for conveying the bed material from the fluidized bed boiler to the torrefaction reactor, and a return channel for conveying the bed material from the torrefaction reactor to the fluidized bed boiler.    USE - The fluidized bed boiler is useful as a heat source for a reactor of a torrefaction system for torrefying biomass (all claimed) including wood chips, straw and hay into biocoal.    ADVANTAGE - The fluidized bed boiler is capable of economically, energy-efficiently and rapidly torrefying the biomass into biocoal with high energy content and without requiring separate burner for the excess of torrefaction gases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for torrefying biomass; and    (2) a torrefaction system.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a torrefaction reactor integrated with a bubbling fluidized bed boiler.    Fluidized bed boiler (100)    Heat exchanger (118)    Unit for heating a heat transfer medium (210)    Heat transfer medium (212)    Fan. (214)
NOVELTY - The high pressure hydrogen producing apparatus comprises a piston unit (56), which applies pressing force to a cell device in the stacking direction of the unit cells (12). The piston unit has first hydrogen passage (70) facing the cell and communicating with hydrogen communication hole, a second hydrogen passage (72) communicating with the first hydrogen passage, and a hydrogen-lead-out passage (76) communicating with two hydrogen passages and leads hydrogen out of hydrogen producing apparatus. Two hydrogen passages are spaced at equal angular intervals centering on the end face of piston.    USE - High pressure hydrogen producing apparatus for use in e.g. water electrolysis apparatus.    ADVANTAGE - Achieves simple and economical structure water electrolysis apparatus that can reliably apply appropriate load with the piston unit. Enables piston unit to smoothly advance and retract axially without tilting since hydrogen pressure acts axially or in retracting direction. Improves performance of stacking and maintains good and stable functions.    DESCRIPTION OF DRAWING(S) - The drawing shows the partial sectional view of the water electrolysis apparatus.    Unit cells (12)    Piston unit (56)    First hydrogen passage (70)    Second hydrogen passage (72)    Hydrogen-lead-out passage (76)
NOVELTY - The fuel cell has gas diffusion sheets (12,14) which are adjacently formed by an anode catalyst layer. The gas diffusion sheet spreads the hydrogen-containing-gas supplied to the anode catalyst layer. The gas diffusion sheet is formed in adjacent state. The separators (20,30) supply the hydrogen-containing-gas to the gas diffusion sheet. The carbon of the low-crystallization degree is added to electric power generation surface inside the gas diffusion sheet more relatively than the carbon of the anode catalyst layer.    USE - Fuel cell, e.g., polymer electrolyte fuel cell, for generating power.    ADVANTAGE - Suppresses oxidation of catalyst layer carbon, suppresses fall of draining property accompanying the sacrificial oxidation, and ensures water-repellent property at the side of membrane electrode assembly (MEA) since the carbon of the low-crystallization degree is added to electric power generation surface inside the gas diffusion sheet more relatively than the carbon of the anode catalyst layer. Increases current density of fuel cell by reducing the contact resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    MEA (1)    Gas diffusion sheets (12,14)    Separators (20,30)    Protrusion section (24)    Porous body layer (34)
NOVELTY - A lignocellulosic biomass is saccharified by compression-molding process which compresses and molds the lignocellulosic biomass to pellet form, and performing saccharification treatment process which saccharifies compressed molding material.    USE - Saccharification of lignocellulosic biomass.    ADVANTAGE - Biomass feedstock can be efficiently dispersed in high concentration in the reaction liquid. The volume of compression molding is reduced. Plant construction cost and storage cost are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the compression molding apparatus.    Body frame (1)    Dies (2)    Roller drive part (3)    Roller (4)    Small hole (5)
NOVELTY - The alcohol based fuel comprises 40-50 parts by weight (pbw) of methanol, 2-4 pbw of ethanol, 2-4 pbw of dimethyl ether, and 40-50 pbw of hydroxy methyl n-valerate.    USE - Used as an alcohol-based fuel.    ADVANTAGE - The alcohol-based fuel can be economically and safely prepared with long service life and high purity and without toxicity in an environmentally friendly manner, and is easy to store.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing alcohol group fuel.
NOVELTY - A buckle type methane collection cover comprises skylight port, air collection cover (5), watertight ring (4), and inner watertight ring or airtight ring, where matched bumps distributed uniformly are arranged between the air collection cover and the watertight ring. The air collection cover is rotated. The air collection cover bump is buckled under the watertight ring bump. The air collection cover is buckled.    USE - As buckle type methane collection cover (claimed); and for the domestic methane tank for concrete or composite material or steel structure and large, middle and small sized methane engineering.    ADVANTAGE - The buckle type methane collection cover is convenient, easy and quick to use; and improves the management and air production effect of the methane tank.    DESCRIPTION OF DRAWING(S) - The figure shows sectional view of buckle type methane collection cover.    Day window (1)    Water sealing ring (4)    Air collection cover (5)    Sunshine plate (6)    Water seal ring bump (7)    Skirt bump (8)
NOVELTY - The engine has an electromagnetic radiation device (40) that radiates the electromagnetic waves from an electromagnetic wave oscillator to the combustion chamber of engine main portion. A plasma generation apparatus generates the electromagnetic wave plasma in combustion chamber, according to the electromagnetic waves radiation. A coaxial cable (50) is connected to the input side of electromagnetic radiation device. A holding element (51) is attached to the engine main portion (20), for holding the coaxial cable.    USE - Internal combustion engine mounted in motor vehicle.    ADVANTAGE - The force acted on the coaxial cable of electromagnetic radiation device can be reduced, by holding the coaxial cable with holding element. Hence the damages occurred in the connection portion of coaxial cable can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the internal combustion engine.    Engine main portion (20)    Electromagnetic radiation device (40)    Connection portion of radiation device (41)    Coaxial cable (50)    Holding element (51)
NOVELTY - Method for converting hydrogen and carbon dioxide into methane by methanogenic microorganisms in a reaction vessel, involves contacting the methanogenic microorganisms with an in-gas comprising hydrogen and carbon dioxide, where ratio of partial pressure of hydrogen to the partial pressure of carbon dioxide inside the reaction vessel in at least one methane production phase is 5:1 or more.    USE - The method and bioreactor are useful for converting hydrogen and carbon dioxide into methane by methanogenic microorganisms in reaction vessel (claimed).    ADVANTAGE - The method is cost-effective, environmentally-friendly, robustic, and convenient to perform, and consumes less energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) bioreactor for converting hydrogen and carbon dioxide into methane comprising (a) at least one reaction vessel for fermenting, growing and/or culturing methanogenic microorganisms, (b) at least one device for introducing and/or removing gaseous substances into the at least one reaction vessel, (c) at least one device for introducing and/or removing a liquid substance or a cell suspension into or from the bioreactor or reaction vessel, (d) devices for measuring, maintaining and/or adjusting oxidation reduction potential, temperature, pressure, head pressure, off-gas concentration and content, partial pressure ratio of hydrogen and carbon dioxide and/or pH value, (e) at least one device for removing off-gas from one reaction vessel, (f) at least one stirring device inside the reaction vessel, and/or (g) at least one device for gas liquid mass transfer;    (2) culture of methanogenic microorganisms having a biomass concentration of at least 6 g biomass/l, where no additional methanogenic microorganism is added after inoculation or cell retention is applied during fermentation; and    (3) use of the methanogenic microorganisms for converting hydrogen and carbon dioxide into methane.
NOVELTY - The method involves heating the liquid bio-oil in a boiler and pumping to screw auger. The combustible biological material is passed to auger with preset internal air temperature. The fiber is moved on horizontal plane and engaged by spray method of bio-oil, and is mechanically exposed to hot air inside the auger. The heat is removed from the torrefied fiber when the fiber has been completely torrefied the material and put through cooling auger. The withdrawn heat is re-circulated back to start the process of preheating green fiber before the initial spray of bio-gas occurs.    USE - Method for producing torrefied fiber.    ADVANTAGE - The torrefaction process virtually eliminates the fine wood particles or dust mixed in the bio oil, decreases the torrefaction time and increases the energy value. The spraying of bio-oil directly on the biomass eliminates the need to re-circulate and reheat the oil. The torrefaction process removes all the moisture and increases the British thermal unit (BTU) value of the fiber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process of producing torrefied fiber.
NOVELTY - Metal-organic framework prepared by a process comprising (a) reacting 3,3',3",5,5',5"-benzene-1,3,5-triyl-hexabenzoic acid and a copper salt and an acid in a polar solvent, (b) allowing the reaction to run at an elevated temperature for at least one day, and (c) separating the metal-organic framework from the polar solvent, is claimed.    USE - The metal-organic framework is useful for storing gases, preferably methane for fueling vehicles (claimed).    ADVANTAGE - The metal-organic framework is safe and effective for storing gases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of preparing the metal-organic framework comprising the steps (a)-(c) as above per se; and    (2) a method-I of storing gases in a metal-organic framework, comprising using a microporous framework to optimize methane storage density and volumetric methane storage, where the microporous framework comprises open copper sites and linker channel sites.
NOVELTY - The apparatus has a rotation chamber connected to a fluidized chamber. A bottom nozzle is provided in the fluidized chamber. A pyrolysis gas chamber stores pyrolysis gas. Chamber surfaces are provided with the gas chamber. An extraction arrangement is provided with a chemical cleaning unit. An exhaust dust collection system and an exhaust after treatment system are provided with a heating surface. The fluidized chamber is connected to a gas cooling chamber.    USE - Apparatus for disposing organic and inorganic waste such as vegetable waste, animal waste and municipal waste.
NOVELTY - The method involves milling biomass in a raspberry system. Dust is burned in a pulverized fuel burner and a steam boiler. Temperature of the exhaust gas is in the range of 300 to 860 degree Celsius.    USE - Method for preparing and combusting organic biomass in a power boiler.
NOVELTY - Obtaining potassium chloride, comprises: submitting brine to concentration; making brine separation after the concentration resulting in a first solid content and a first liquid content; cooling the first liquid content; separating the first liquid content after cooling, thus resulting in a second solid content and a second liquid content; performing enrichment of the second solid content; and separating the second solid content after enrichment, thus resulting in a third solid content and a third liquid content.    USE - The process is useful for obtaining potassium chloride (claimed), which is useful in e.g. medical environment as a substitute of electrolyte in the organism, and cooking.    ADVANTAGE - The process: reduces energy consumption; is cost-effective; increases vapor saving; reduces natural gas consumption; and is simple and eco-friendly.
NOVELTY - The method involves pyrolysing wood i.e. timber, at temperature from 350 to 750 degree Celsius and pressure of 10 to 1000 kPa in hot reaction zone for less than 10 seconds.    USE - Method for obtaining bio-oil.
NOVELTY - The method comprises taking Phellodendron (200 parts by weight (pbw)), radix paeoniae rubra (200 pbw), Salvia (100 pbw), peach seed (140 pbw), herbal lycopi (120 pbw), radix linderae (120 pbw), cow herb seed (80 pbw), radix angelicae (80 pbw), purifying and drying the material, crushing Phellodendron into powder, mixing the materials using water (12-times) with a medicine, heating the materials until it reaches 80 degrees C and then adding peach seed, and continuing heating and boiling the materials for three times.    USE - The method is useful for preparing traditional Chinese medicine capsule, which is useful for treating prostatitis and prostatic hyperplasia.    ADVANTAGE - The method is capable of economically preparing the traditional Chinese medicine capsule in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises taking Phellodendron (200 parts by weight (pbw)), radix paeoniae rubra (200 pbw), Salvia (100 pbw), peach seed (140 pbw), herbal lycopi (120 pbw), radix linderae (120 pbw), cow herb seed (80 pbw), radix angelicae (80 pbw), purifying and drying the material, crushing Phellodendron into powder, mixing the materials using water (12-times) with a medicine, heating the materials until it reaches 80 degrees C and then adding peach seed, continuing heating and boiling the materials for three times with the first time two hours, the second time add water 10-times the total weight of the medicine and boiling it for 1.5 hours and the third time add water 10-times the total weight of the medicine and boiling it for one hour and then mixing the decoction and filtering it and concentrating into paste that has a relative density of 1.35 under the temperature of 80 degrees C and then reducing the pressure and drying it into powder, adding the powder of Phellodendron, and pouring the powder into capsules to prepare traditional Chinese medicine capsules.
NOVELTY - The special fertilizer comprises 60-70 parts by weight (pbw) of chicken manure, 0.02-0.2 pbw of straw leavening agent, 1-5 pbw of urea, 20-35 pbw of calcium magnesium phosphatic fertilizer, 1-5 pbw of potassium sulfate and 0.5-1 pbw of borax, where the content of the organic matter in the chicken manure is greater than 40% and the water content is less than 20%.    USE - The special fertilizer is useful for Toona ciliata.    ADVANTAGE - The special fertilizer increases: Toona ciliata height of more than 10% compared with conventional compound fertilizer; and Toona ciliata growth and diameter of more than 12%, hence eco-friendly and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing special fertilizer.
NOVELTY - Use of Thalia dealbata for decontaminating livestock biogas slurry, is claimed, where the Thalia dealbata is planted in the livestock biogas slurry pollution environment.    USE - The Thalia dealbata is useful for decontaminating livestock biogas slurry.    ADVANTAGE - The Thalia dealbata is capable of easily and economically decontaminating the livestock biogas slurry with reduced energy consumption in an environmentally friendly manner.
NOVELTY - The apparatus has roof (200) that is installed at the upper portion of the fermenter (100), so that the bad smell is ejected through exhaust duct (300) of roof. The acid (220) and the valley (230) are inclined around the opening portion (210) of the roof. The exhaust duct is mounted towards the peripheral wall (110) of fermenter into the equal space. The drainpipe (240) is connected to the valley. The condensed water staying in the valley is emitted to outside through the drainpipe and waterway (440).    USE - Organic solid waste draining apparatus of fermenter.    ADVANTAGE - The organic solid waste can be drained effectively. The occurrence of bad smell in the roof of fermenter during draining of organic solid waste can be prevented. The moisture generated in the bottom surface of fermenter can be prevented, thus the fermentation efficiency of the fermenter can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the organic solid waste draining apparatus of fermenter.    Fermenter (100)    Peripheral wall (110)    Roof (200)    Opening portion (210)    Acid (220)    Valley (230)    Drainpipe (240)    Exhaust duct (300)    Waterway (440)
NOVELTY - The device has a gas recuperator (5) positioned above a thermal plasma torch along a direction of circulation of fluids. A magnetic field generating device (4) i.e. magnetizer, co-operates with an outlet of the thermal plasma torch, where frequency of magnetic field generated from the magnetizer is matched with frequency of electric current in the plasma torch. A heat exchanger (7) co-operates with an outlet of the gas recuperator. The plasma torch has electrodes e.g. cathode (1a) and anode (1b), which are supplied with electric signals having different phases.    USE - Device for producing and separating a simple product e.g. gas such as hydrogen and oxygen, from a chemically complex product i.e. water vapor, or from a mixture of simple products such as gaseous dihydrogen, tritium, gaseous dioxygen and ozone.    ADVANTAGE - The configuration of the device enables separating the simple product from the chemically complex product or from the mixture of simple products in an optimal manner, with high quality and with low energy consumption, thus obtaining high purity of the separated simple product. The heat exchanger protects the body of the torch even by lowering the temperature of different parts of the body of the torch such that the torch is resistant to industrial operation. The configuration of the device enables adjusting the voltage of the torch for compensating the wear of the torch or variations of flowrate of entry products, and assures better sealing at high temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded partial sectional front view of a simple product producing and separating device.    Cathode (1a)    Anode (1b)    Magnetic field generating device (4)    Gas recuperator (5)    Heat exchanger (7)
NOVELTY - An internal aeration type artificial wetland sewage treatment system comprises aeration pipe and aeration ring, where the aeration pipe is provided with pipes that are connected on main pipe and branch pipe port of the aeration ring.    USE - Internal aeration type artificial wetland sewage treatment system.    ADVANTAGE - The system solves the problem of manual wetland dissolved oxygen, and it is not easy to be blocked.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of internal aeration type artificial wetland sewage treatment system.
NOVELTY - Microbial oil removing device comprises a carbon steel shell, and an aeration device, where the upper part of the carbon steel shell is provided with a water inlet, a water outlet, an oil outlet and the sewage discharge port. The carbon steel shell is set with filling material. The aeration device comprises an air inlet, an air inlet branch pipe, an air inlet main pipe, a micro-porous aerator and an external air supply device. The gas inlet is set on the side wall of the carbon steel shell.    USE - Used as a microbial oil removing device.    ADVANTAGE - The device is economical; has high production efficiency; does not produce secondary pollution; can achieve high chemical oxygen demand and biochemical oxygen demand removal rate; can increase the oil removal rate to 99%; and can reduce the corrosion rate by 50%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the microbial oil removing device.
NOVELTY - Sludge compost primary mixing machine comprises a cylinder, a support component, a mixing component, a servicing window, a speed reducing motor and a cylinder body. The mixing component and speed reducing motor are respectively fixed on the support component by a bolt. The servicing window is set on outer wall of the cylinder body. The mixing component comprises a blade, a mounting base and a rotating shaft. The base is welded on the rotating shaft. The blade is fixed on the mounting base by the bolt. The blade working surface is a cylindrical surface, a spiral surface and a plane.    USE - Used as a sludge compost primary mixing machine.    ADVANTAGE - The mixing machine solves the problem of the blades serious abrasion and low service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sludge compost primary mixing machine.
NOVELTY - Integrated and externally heated biomass pyrolyzing device comprises a machine frame, a feeding hopper, a conveying device, a pyrolyzing device, a heating device and a discharging device, where each parts are arranged on the machine frame. The feeding hopper is connected with the pyrolyzing device. The heating device is coated out of the pyrolyzing device. An insulation layer is coated out of the pyrolyzing device and the heating device. A discharge port and a pyrolyzing gas outlet are arranged on the terminal end of pyrolyzing device. The discharge port is connected with discharging device.    USE - Used as an integrated and externally heated biomass pyrolyzing device.    ADVANTAGE - The device has simple operation with high treatment efficiency, consumes less energy, does not cause secondary pollution, supplements the energy demands by utilizing the gas generated in the pyrolyzing process to produce biochar; utilizes the waste heat for drying the pyrolysis raw material, and achieves the automatic control of the whole process.    DETAILED DESCRIPTION - Integrated and externally heated biomass pyrolyzing device comprises a machine frame, a feeding hopper, a conveying device, a pyrolyzing device, a heating device and a discharging device, where each parts are arranged on the machine frame. The feeding hopper is connected with the pyrolyzing device through the conveying device. The heating device is coated out of the pyrolyzing device. An insulation layer is coated out of the pyrolyzing device and the heating device. A discharge port and a pyrolyzing gas outlet are arranged on the terminal end of the pyrolyzing device. The discharge port is connected with the discharging device. The pyrolyzing gas outlet is connected with the heating device.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the integrated and externally heated biomass pyrolyzing device.
NOVELTY - Manufacture of fuel includes removing heavy metal, sterilizing and deodorizing, sludge treatment, dehydrating and drying, grinding the sludge after dehydration and drying in a grinder; putting the sludge after grinding into a blender mixer, adding combustion improver and agglomerant in the blender mixer, heating to obtain heated mixed materials; and compressing pressure and forming the heated mixed materials, and packaging.    USE - Method for manufacturing fuel (claimed).    ADVANTAGE - The method has low cost of dehydration treatment and low small energy consumption, and is harmless and environment-friendly.    DETAILED DESCRIPTION - Manufacturing fuel comprises:    (A) putting heavy metal extraction agent in sludge, water-washing and stirring, filtering and separating solid phase and liquid phase after defecation;    (B) adding potassium permanganate powder which is 0.5-2% of the sludge total amount, and stirring uniformly;    (C) changing the sludge through sterilization and deodorization into a seal pot, adding aseptic agent and activated carbon in the seal pot, and then stirring uniformly;    (D) putting the sludge after the pre-treatment into a dehydration machine, adding industrial salt, stirring uniformly, then processing pressure dehydration, and then changing it into a drying machine for drying after dehydration;    (E) grinding the sludge after dehydration and drying in a grinder;    (F) putting the sludge after grinding into a blender mixer, adding combustion improver and agglomerant in the blender mixer, heating at 40-60 degrees C to obtain heated mixed materials; and    (G) compressing pressure and forming the heated mixed materials, and packaging.
NOVELTY - The method involves feeding fixed quantity of biomass through the input unit. The biomass is supplied to the dryer unit through the input unit. The thermal oil is warmed and the microwave is irradiated. The dried biomass is injected by the half carbonization unit at the ambient pressure through the dryer unit and mixed with oil. The inner temperature of the dryer unit is set to 50-70 degrees C.    USE - Method for producing bio-coal for co-firing with coal in coal-based power plant.    ADVANTAGE - The installation cost is reduced, the energy is reduced and the work efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for producing bio-coal for co-firing with coal in coal-based power plant.
NOVELTY - The composition comprises Propolis (25 parts by weights (pbw)), Coptis (25 pbw), Pulsatilla (30 pbw), cardamom (25 pbw), ginger ale (30 pbw), Psorale (25 pbw), shrubalthea flower (30 pbw) and gall (25 pbw).    USE - The composition is useful for treating porcine proliferative enteritis. No biological data given.    ADVANTAGE - The composition can be simply prepared without pollution and toxicity, and has no adverse events.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composition.
NOVELTY - The cracker has air blower connected with cracking chamber. The airlock feeding device is provided with motor for driving the cracking chamber. The upper end of emergency discharge device is connected with cracking chamber. The fire tube opening is set with tangential swirling flow guide device. The fire unit is connected with fan of primary air pipe and secondary air pipe. The fuel is chosen from wooden meal, rice hull, Chinese medicine drug, organic substance, and blue algae.    USE - Biomass fuel cracker.    ADVANTAGE - The leakage of tempering flue gas from feeding device can be prevented for increasing the cracking efficiency. The generation of tar and consumption of heat can be reduced, thus the burn-off condition and higher safety factor can be improved. The fuel cracker is high in applicability, strong in practicability, and convenient to operate. The processing of the cracker can be simplified. The use cost of the cracker can be reduced. The cracker can be really cracked at high temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel cracker.
NOVELTY - Prevention of circulating pump sealing leakage comprises washing mechanical seal cavity of circulating pump for biodiesel, peeling mechanical seal cavity of carbon-containing particle, and carbonaceous particle of diesel liquid storage, and coking carbon granule of 19-40C ester by carbon and high temperature carbonization.    USE - Method of prevention of circulating pump sealing leakage.    ADVANTAGE - The method does not only can reduce circulating pump sealing leakage rate, but also can continuously produce biological diesel oil.
NOVELTY - Preparing formulation, comprises (i) mixing galangal, Litsea cubeba and pepper, immersing in alcohol solution for 25-28 days after wrapping by a gauze, stewing the soaked solution for 20-24 hours, precipitating and filtering, repeating the stewing process, precipitating and filtering the soaked solution for 1-2 times, and obtaining the raw medicament slurry; (ii) adding a camphor alcohol solution into the raw medicament slurry, and uniformly stirring; (iii) adding turpentine into the medicament solution obtained in step (ii), and rapidly canning to obtain the finished product.    USE - The formulation is useful for treating and preventing plant root disease e.g. bacterial wilt, blight, and root rot caused by frost or flood (claimed).    ADVANTAGE - The method is simple, utilizes raw materials, which is of low cost, and produces product, which increases the production by enhancing disease resistance in crop; reduces the usage of fertilizer, reduces the production cost, and is ecofriendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the formulation prepared by using the above mentioned method.
NOVELTY - Microbial in situ processing of kitchen waste comprises preprocessing, processing, subsequent processing, standardizing, and packing target product, where the processing comprises: using microorganism as a source to carry out decomposition and reduction of kitchen waste by firstly choosing all kinds of organic kitchen waste comprising cellulose as skeleton e.g. animal fiber, plant fiber, grass fiber and wood fiber, and breaking the cellulose chain.    USE - The method is useful for microbial in situ processing of kitchen waste.    ADVANTAGE - The method: does not require external power until the environment temperature is above 10 degrees C; ensures harmless decomposition; reduces the kitchen waste transportation process; yields stable processed organic material without environmental pollution; does not require a high temperature sterilization for microbial decomposition process, unlike during fermentation to inhibit the growth of microorganism.
NOVELTY - A biological waste material comprehensive use value-added device comprises carbonizing furnace. The carbonization furnace is provided with a conveying mechanism.    USE - Biological waste material comprehensive use value-added device useful for discarding sawdust, straw or bamboo tip or producing carbon powder, tar, wood gas or acetic acid.    ADVANTAGE - The biological waste material comprehensive use value-added device has high use efficiency, good effect, large value and low labor intensity.
NOVELTY - The furnace has energy storage coil (6) which is located on a panel (4). A furnace liner (2) is provided with a combustion chamber (9) that is connected with a feeding port (15). The outer wall of a furnace outer liner (1) is provided on an insulating plate (7). An energy storage coil is provided with flue portion (18) that is connected with a smoke inlet (181). An auxiliary smoke channel (17) of lower side wall is provided with a secondary air inlet passage (13) that is provided with auxiliary smoke channel air inlet hole.    USE - Biomass semi-gasification furnace.    ADVANTAGE - The heat utilization rate can be improved, and the product yield can be improved effectively, and the heat efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass semi-gasification furnace.    Furnace outer liner (1)    Furnace liner (2)    Panel (4)    Energy storage coil (6)    Insulating plate (7)    Combustion chamber (9)    Secondary air inlet passage (13)    Feeding port (15)    Auxiliary smoke channel (17)    Flue portion (18)    Smoke inlet (181)
NOVELTY - The device comprises an outer wall body (5), a soft fermenting bag (1), a mixing area (7), a marsh gas outlet, a supporting frame (6), and a slope (8). The outer wall body is connected with the mixing area and the soft fermenting bag. A top of the soft fermenting bag is provided with the marsh gas outlet. The soft fermenting bag is arranged on the supporting frame. The mixing area is provided with the slope.    USE - The device is useful for producing marsh gas combined with organic fertilizer production.    ADVANTAGE - The device is capable of economically and conveniently producing the marsh gas combined with organic fertilizer production with high-quality and yield.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for producing marsh gas combined with organic fertilizer production.    Soft fermenting bag (1)    Outer wall body (5)    Supporting frame (6)    Marsh gas outlet (7)    Slope. (8)
NOVELTY - The method comprises adding tolterodine alkali and L-tartaric acid to react and salify with ethanol-methanol-water ternary mixing solvent, heating and refluxing the mixture to fully dissolve, refluxing and insulating the mixture for 40 minutes, cooling the mixture at 0 degrees C, insulating the mixture for 3 hours, filtrating the mixture to obtain filtrate, drying the filtrate to obtain a rough product, adding the rough product into the ethanol-methanol-water ternary mixing solvent, heating and refluxing the mixture to fully dissolve, and adding active carbons to heat.    USE - The method is useful for preparation of tolterodine tartrate.    ADVANTAGE - The method ensures easy and economical preparation of the tolterodine tartrate with high quality and purity and improved yield in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises adding tolterodine alkali and L-tartaric acid to react and salify with ethanol-methanol-water ternary mixing solvent, heating and refluxing the mixture to fully dissolve, refluxing and insulating the mixture for 40 minutes, cooling the mixture at 0 degrees C, insulating the mixture for 3 hours, filtrating the mixture to obtain filtrate, drying the filtrate to obtain a rough product, adding the rough product into the ethanol-methanol-water ternary mixing solvent, heating and refluxing the mixture to fully dissolve, adding active carbons to heat, insulating and refluxing the mixture for 60 minutes, thermally filtrating the mixture to obtain filtrate, cooling the filtrate at 0-5 degrees C, insulating the filtrate for 2 hours, filtrating the mixture to obtain filtrate, and drying the filtrate to obtain a finished product. The weight ratio of the ethanol-methanol-water ternary mixing solvent comprises: salifying of tolterodine racemic alkali, ethanol, methanol and water of 1.0:2.4:1.2:1.1; and recrystallizing: L-tolterodine tartrate, ethanol, methanol and water of 1:2.36:1.18:1-1.
NOVELTY - A tobacco leaf special organic fertilizer, comprises (weight by parts): decomposed fertilizer (30-60), starch (10-20), bran (3-5), fulvic acid (3-5), oleic acid (3-5), zinc fertilizer (1-2), and potash fertilizer (1.5-2). The zinc fertilizer is zinc sulfate heptahydrate. The potash fertilizer is potassium nitrate, potassium chloride or potassium sulfate.    USE - As special organic fertilizer of tobacco leaf (claimed).    ADVANTAGE - The tobacco leaf provided by special organic fertilizer can supplement soil rich nutrient elements and adjust water content of soil C, N ratio, and at the same time it provides the use of starch and protein (bran). The special organic fertilizer can be directly absorbed by the nutrient element for tobacco leaf, and also can keep the ecological balance of tobacco- planting soils in the soil. The fertilizer improves the quality of the tobacco leaf.
NOVELTY - Sludge treatment comprises using dry anaerobic fermentation and low temperature carbonization treatment.    USE - A sludge treatment method.
NOVELTY - Preparing acidic biological organic fertilizer comprises (1) drying crop straws crushing, then uniformly mixing with a pig manure of a mass ratio of 1:2-1:4, and (2) adding molasses (1.5-3wt.%) and effective microorganism inoculants (1-3wt.%) into the mixture obtained in the step (1) for fermenting, stirring uniformly, transferring into a aluminum foil bag with an exhaust valve, and placing it in a fermentation chamber for a complete anaerobic fermentation for 14-20 days at 28-30 degrees C.    USE - The method is useful for preparing acidic bio-organic fertilizer for saline-alkali soil.    ADVANTAGE - The method is simple and economical, enables use of crop straw and pig manure, and produces an improved fertilizer having lower pH using cheaper raw materials. The fertilizer improves the soil geology, reduces insect pests and plant diseases.
NOVELTY - Preparing biological fuel gas using waste biomass, comprises (i) processing waste biomass into semi-liquid slurry; (ii) performing steam gasification treatment to semi-liquid slurry to obtain the crude oil; and (iii) performing supercritical water gasification treatment to the crude oil to obtain the crude biological fuel gas.    USE - The method is useful for preparing biological fuel gas using waste biomass.    ADVANTAGE - The method adopts two-step gasification process, which increases the gasification rate of the carbon element in waste biomass, and avoids tar carbon deposition blockage to achieve continuous feeding.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biological fuel gas, prepared by the method as mentioned above.
NOVELTY - The furnace has a furnace main body provided with a fluidized bed gasification section and a fixed bed cracking section. A top part of the fluidized bed gasification section is provided with a flue gas inlet (1). A bottom wall of the fluidized bed gasification section is provided with a gasification agent inlet. A recording head is linked to a gasification agent entrance of a nozzle (3). An outer side of the fixed bed cracking section is fixed in a fixed bed grate (8). The fixed bed grate is located on a gas outlet (7). A bottom part of a gas draught fan is connected with the gas outlet.    USE - Solid biomass gasification cracking furnace.    ADVANTAGE - The furnace can make flue gas from tar by a catalytic cracking reaction so as to improve utilization rate of solid biomass, and avoids tar secondary pollution to environment.    DETAILED DESCRIPTION - The furnace is provided with a fixed bed that is made of metallurgical coke.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a solid biomass gasification cracking furnace in partial section.    Flue gas inlet (1)    Nozzle (3)    Fixing depth bed (6)    Gas outlet (7)    Fixed bed grate (8)
NOVELTY - Improving sandy soil, comprises: (i) uniformly spraying bentonite via a special cast spreading machine on the soil surface before autumn or spring to prepare soil; (ii) plowing using an agricultural machinery, uniformly mixing bentonite and sandy soil in the top soil layer, and completely mixing using a rotary cultivator; and (iii) watering before sowing required for irrigation.    USE - The method is useful for improving sandy soil, saline alkali soil, infertile soil, yellow soil, and soil that is difficult to harden (claimed).    ADVANTAGE - The method is economical and environmental-friendly and has rapid effect.
NOVELTY - The Liriomyza attractant comprises 0.4 wt.% of cis-9-tricosene, 0.15 wt.% of tricosenol, 0.06 wt.% of linalool, 0.04 wt.% of 3-hexene-1-ol, 0.5 wt.% of beta -caryophyllene, 1.5 wt.% of 2-hexenal, 0.3 wt.% of 2-hexenol, 0.25 wt.% of 1-ethylhexenol, 2.4 wt.% of 3-hexenol acetate, 0.6 wt.% of alpha -ionone, 0.3 wt.% of beta -ionone, 0.5 wt.% of n-hexane, 9.0 wt.% of sodium dodecyl benzene sulfonate, and 84 wt.% of water.    USE - Used as a Liriomyza attractant. No biological data given.    ADVANTAGE - The Liriomyza attractant can be simply, conveniently and safely prepared without toxicity in an environmental friendly manner.
NOVELTY - A DF-28 bioorganic fertilizer comprises balloonflower, feces of poultry and livestock, and crop leftovers as main raw materials. The fertilizer is obtained by adding the raw materials with zinc, boron and other trace elements, and fermenting using active bio-enzyme.    USE - DF-28 bioorganic fertilizer.    ADVANTAGE - The fertilizer can breed beneficial bacteria in soil within 3-5 days after the fertilizer applied and as long as soil has enough moisture under constant temperature. It increases soil fertility, improves soil structure, eliminates soil hardening, and strengthens ability of crops to resist disease and insect pests to increase crop yield and improve quality of agricultural products. Further, the fertilizer can reduce soil and environment pollution since the main raw materials are mostly wastes materials.
NOVELTY - Carbon-based urea fertilizer is made by mixing (pts.wt.) bio-carbon black (12-52), urea (23-64), beneficial bacteria agent (0.02-1.1), and synergistic agent (2.4-5.3); and according to the different needs of soil condition, making granular fertilizer or powder fertilizer. The beneficial bacteria agent is nitrogen-fixing bacteria, phosphate-solubilizing bacteria, silicate bacteria, or Bacillus. The synergistic agent is wood vinegar solution, amino acids, humic acid, or natural plant extract growth agent.    USE - Carbon-based urea fertilizer.    ADVANTAGE - The carbon-based urea fertilizer can reduce loss rate of urea in the soil; reduces fertilizer input cost; avoids adverse effects on soil and ground water environment; and realizes the effect of weight loss reduction. It can also activate and improve the soil urease so that urea can be directly converted into nitrogen nutrition elements that can be absorbed by crops so that impact of urea and biuret is greatly reduced to avoid soil compaction caused by simple use of urea and soil loose, alleviate soil compaction phenomenon, increase soil aggregate structure, reduce soil bulk density, improve soil physical activity, improve soil environment, increase fertilizer-storing and water-holding capacity of soil, complement lack of trace elements necessary to crops caused by single application of phosphorus, and allow crops to absorb more balanced nutrients to achieve increased yield.
NOVELTY - Method (M1) for extracting raw oil for biodiesel, involves irradiating animal fat in microwave for extracting oil and separating residues from the oil.    USE - The method (M1) is useful for extracting raw oil which is used for manufacturing biodiesel (claimed).    ADVANTAGE - The method (M1) is rapid, consumes less energy, extracts 90% of oil from animal fat and produces high yield of biodiesel with purity of 96.5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for manufacturing biodiesel, which involves pre-processing the extracted oil by acid catalyst and subjecting the oil to transesterification in presence of base catalyst and alcohol.
NOVELTY - The apparatus has fan and heater that are operated according to control signal of micro computer (2). Water level sensor and temperature sensor senses water level of food garbage and temperature of fermenter (1) respectively. A deodorizing unit (10) has guide tube that guides odor molecule within bath (7).    USE - Food garbage treating apparatus.    ADVANTAGE - Food garbage can be treated effectively in short period of time without environmental contamination. Convenience of using the apparatus is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the food garbage treating apparatus.    Fermenter (1)    Micro computer (2)    Bath (7)    Deodorizing unit (10)    Exhaust pipe (11)
NOVELTY - System for processing by-product oil expressed from microalgae, comprises pre-processor for pre-processing the by-product of the microalgae, acid fermenter for fermenting the pre-processed by-product, processor for processing the pre-processed by-product, and purification/separation unit.    USE - The system is useful for processing by-product oil expressed from microalgae and producing biogas, preferably carbon dioxide and methane (claimed).    ADVANTAGE - The system processes by-product oil expressed from microalgae by economical and environmentally-friendly method.
NOVELTY - A furosin is extracted from Bischofia polycarpa leaves by crushing B. polycarpa leaves, adding to carbon dioxide supercritical extractor, and controlling extraction pressure, temperature, carbon dioxide flow and time; absorbing through strong-alkaline styrene type anion exchange resin, eluting using sodium hydroxide solution, collecting and eluting, and filtering; collecting outflow liquid through strong-acid styrene type cation exchange resin, collecting outflow liquid, filtering, concentrating, and drying; and adding to silica-gel chromatography column.    USE - Method for extracting furosin from B. polycarpa leaves (claimed).    ADVANTAGE - The method is convenient in operation, less in pollution, and less in energy consumption; and the product is high in purity.    DETAILED DESCRIPTION - Extracting furosin from B. polycarpa leaves, comprises (A) crushing B. polycarpa leaves, adding to carbon dioxide supercritical extractor, controlling extraction pressure to be 20-30 MPa and temperature to be 45-55 degrees C, controlling carbon dioxide flow to be 1-3 ml/g raw drug-minutes, controlling extraction time to be 120-140 minutes, and obtaining extract; (B) absorbing through strong-alkaline styrene type anion exchange resin, eluting using 0.5 mol/L sodium hydroxide solution, collecting and eluting, and filtering; (C) collecting outflow liquid through strong-acid styrene type cation exchange resin, collecting outflow liquid, filtering, concentrating, and drying; and (D) adding to silica-gel chromatography column, eluting using methanol-chloroform mixed solvent with volume ratio of 5:1, collecting the eluent part, combining the eluents of the (3-5)th column volumes, concentrating, adding acetone crystal, separating the crystal, washing, drying, and obtaining the final product.
NOVELTY - A preparation for treating plant pathogen nematodes, involves mixing trichloroiminocyanuric acid, chlorobromoisocyanaria acid or sodium dichloro isocyanurate with cosolvent, surfactant and filler.    USE - For treating plant pathogen nematodes (claimed).    ADVANTAGE - The method treat nematodes harm, replace riskiest pesticide or reduce usage of pesticide at the maximal degree, reduce harm of pesticide residue and the harm to people and livestock, reduce environment pollution; and is efficient and harmfulless, green and environment-friendly, is featured with simple and convenient operation, friendly environment and easy popularization and use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating plant pathogen nematodes, involving dissolving the preparation into water to irrigate root of the crop which harm to the nematodes or scatter it into the soil to kill the nematodes.
NOVELTY - Preparation of biological diesel oil comprises reacting acid oil and epoxy compound to cause epoxy compound ring-opening reaction with free acid in grease; separating unreacted epoxy compound to obtain grease mixture; subjecting grease mixture into ester exchange with low carbon alcohol; and condensing to obtain biodiesel.    USE - Preparation of biological diesel oil (claimed).    ADVANTAGE - The method reduces grease acid value and free acid in fat with epoxy ring-opening reaction to generate new component.
NOVELTY - A memantine hydrochloride is synthesized by reacting halogenated dimethyladamantane with nitrile derivative, concentrated sulfuric acid and an organic acid; adding water to obtain 1-acetamido-3,5-dimethyladamantane crystal as intermediate product, hydrolyzing by adding an alcohol and a base, extracting, salifying to obtain crude product, and re-crystallizing.    USE - Method of synthesizing a memantine hydrochloride.    ADVANTAGE - The method is simple, short, convenient and environment-friendly; simplifies post-treatment operation; has improved efficiency, and increased yield to 90% from 70%.
NOVELTY - A betalain is extracted from Phytolacca acinosa pulp and fruit by selecting mature India pokeberry purple black berry, removing fruit stem, using water as solvent for normal temperature continuous counter-current leaching, filtering the extract solution, and filling in sealed container for storage; filtering the stored liquid using diatomite filter to obtain ultrafiltrate; and processing the ultrafiltrate concentration by reverse osmosis.    USE - Method for extracting betalain from mature P. acinosa pulp and fruit (claimed) used in fields of food, cosmetic and medicine.    ADVANTAGE - The method does not use organic chemical reagent, thus avoiding generation of toxic substance. It uses normal low temperature micro-ultrafiltration-reverse osmosis process which saves energy and reduces decomposition and loss of pigment. The yield of the product is higher than 8%.    DETAILED DESCRIPTION - Extracting betalain from P. acinosa pulp and fruit, comprises (A) selecting mature India pokeberry purple black berry, removing fruit stem, using water as solvent for normal temperature continuous counter-current leaching, filtering the extract solution using 16-60-mesh stainless steel screen, and filling in sealed container for storage; (B) filtering the stored liquid using diatomite filter to obtain ultrafiltrate; and (C) processing the ultrafiltrate concentration by reverse osmosis, concentrating solution by vacuum centrifugal evaporator, further concentrating when the solid content reaches 30-40%, and spraying and drying.
NOVELTY - Preparation of (2,2')bipyridinyl-4,4'-dicarbaldehyde involves adding 4,4'-dimethyl-(2,2')bipyridinyl (20-40 ml.%), N-halo-succinic acid (II) and initiator into organic solvent, where ratio of (2,2')bipyridinyl-4,4'-dicarbaldehyde, compound (II) and initiator is 1:5-6:0.1-1.2, mixing under inert gas and at 55-80 degrees C for 20-40 hours, cooling and filtering product to room temperature, neutralizing by alkali solution until pH is 7-8, separating to produce organic phase and mixing it with alkaline liquid, cooling to room temperature, purifying, extracting, evaporating and concentrating.    USE - For preparing (2,2')bipyridinyl-4,4'-dicarbaldehyde used as chemical and medicament synthesis intermediate.    ADVANTAGE - The method avoids the use of the strong oxidizer to sewage discharge; has short reaction steps, simple operation, and low cost; and avoids pollution.
NOVELTY - An efficient fertilizer preparing method involves adding refluxed acid with iminodiacetonitrile and waste mother liquid to generate hydrochloride of iminodiacetic acid and iminodiacetic mother liquor. The obtained solution is distilled and neutralized by adding alkali to obtain glycine waste mother liquid acid neutralized product, where the obtained product comprises ammonium chloride, ammonium salt and iminodiacetic cyanogens.    USE - Method for preparing efficient fertilizer by using iminodiacetonitrile and waste mother liquid to use as organic fertilizer (claimed).    ADVANTAGE - The method enables preparing efficient fertilizer in a simple, inexpensive and eco-friendly manner without discharge of waste.
NOVELTY - A griffonin medicinal material purifying method involves extracting liquid from griffonin medicinal material for 30-180 minutes. The extracted liquid is collected and analyzed. Recycling agent is added into the extracted liquid. The extracted liquid is dissolved and dispersed in water. The dispersed liquid is subjected to a macro-porous resin adsorption process. The resulting solution is purified by high speed counter-current chromatography. The purified solution is concentrated using 30-60 percent of ethanol. The concentrated solution is dried to obtain purified griffonin medicinal material.    USE - Method for purifying griffonin medicinal material.    ADVANTAGE - The method enables purification of the griffonin medicinal material in a simple, convenient, safe and reliable manner without causing pollution and producing solvent residue.    DETAILED DESCRIPTION - A griffonin medicinal material purifying method involves extracting 70 percent of liquid from griffonin medicinal material under pressure of 25-35 mega Pascal and temperature of 45-60 degrees C for 30-180 minutes. The extracted liquid is collected and analyzed, and recycling agent is added into the extracted liquid. The extracted liquid is dissolved and dispersed in water. The dispersed liquid is subjected to a macro-porous resin adsorption process. The resulting solution is purified by high speed counter-current chromatography, and the purified solution is concentrated using 30-60 percent of ethanol. The concentrated solution is dried to obtain purified griffonin medicinal material.
NOVELTY - The method involves coating an electrolytic membrane (2) with an electrode paste (1) that contains alcohol as its solvent. Fixed rollers (3,4) then fix the paste to the membrane, after which the membrane is made to dry at normal temperature, of which the membrane absorbs the moisture content of the paste during the drying process.    USE - Manufacturing method for fuel cell membrane electrode assembly.    ADVANTAGE - Reduces the local internal stress difference caused by swelling and the contractility of the coated and non-coated portions of the electrolytic membrane as the moisture content of the electrode paste is absorbed by the membrane during the drying process, thus suppressing formation of wrinkles. Improves manufacturing efficiency since the electrolytic membrane can be manufactured with a sufficient degree of continuity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a manufacturing apparatus for a fuel cell membrane electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory schematic diagram of the manufacturing apparatus of the fuel cell membrane electrode assembly. (Drawing includes non-English language text)    Electrode paste (1)    Electrolytic membrane (2)    Fixed rollers (3,4)    Electrolytic membrane roll for unwinding (6)    Paste coating portion (11)
NOVELTY - The device comprises a reactor, a heating element, a gas holder, a reversibly electric motor, a cantilever beam, and supports. The reactor is connected to the gas holder by a hose, and is rigidly fixed to a shaft of the reversibly electric motor. The electric motor and cantilever beam are positioned on the supports.    USE - The device is useful for anaerobic fermentation of organic waste for obtaining biogas.
NOVELTY - The installation comprises a system for preparation raw material, a reactor, a system for removing biogas with a vacuum pump, a system for removal of slime, and a substrate. The reactor comprises inlet branch pipes. An axial- blade twister is placed in the branch pipes of an upper cover of the reactor housing.    USE - The installation is useful for anaerobic processing of organic waste.
NOVELTY - Catalyst composition comprises solid base catalyst comprising solvent chosen from methanol, vegetable oil and biodiesel fuel, and calcium oxide powder. The calcium oxide powder has surface with particle diameter of 100 mu m or less, and is changed into active oxide state.    USE - The catalyst composition, method and apparatus are useful for preparing biodiesel fuel (all claimed).    ADVANTAGE - The method is cost-effective, utilizes waste products obtained from industry, and suitable for mass production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing catalyst composition, involves pulverizing baked limestone having particle diameter of 0.5 mm or more with the solvent;    (2) method (M2) for preparing biodiesel fuel, involves (a) performing the above-mentioned steps in method (M1), (b) reacting vegetable oil and methanol in presence of catalyst composition obtained product in method (M1), and producing fatty-acid methyl ester, and (c) heating the oil phase of upper phase and improving the formation rate of fatty-acid methyl ester after leaving still reaction liquid obtained at step (b), and separating and removing glycerol phase of the produced lower phase; and    (3) apparatus comprising grinder for pulverizing solvent and baked limestone, first stirring vessel for making vegetable oil and methanol react in presence of the catalyst composition, stationary separation tank for separating glycerol phase and oil phase, and second stirring vessel for improving formation rate of fatty-acid methyl ester.
NOVELTY - A solar energy pipeline continuous biodiesel preparation device comprises product storage tank (1), pipeline reactor (2), black coating (3), glass cover plate (4), heat collector (5), valve (6), and storage tank (7), where the storage tank is connected with pipeline reactor, and the storage tank is higher than the pipeline reactor.    USE - As a solar energy pipeline continuous biodiesel preparation device, useful for producing biological diesel oil.    ADVANTAGE - The device changes the traditional biologic diesel oil consumption of the high energy electrical energy mode; provides bottomless and inexhaustible renewable clean energy solar energy, which reduces the production cost of the biodiesel; and has compact structure, and low cost.    DETAILED DESCRIPTION - A solar energy pipeline continuous biodiesel preparation device comprises product storage tank (1), pipeline reactor (2), black coating (3), glass cover plate (4), heat collector (5), valve (6), and storage tank (7), where the storage tank is connected with pipeline reactor, and the storage tank is higher than the pipeline reactor. The pipeline reactor close to the material storing tank is provided with a valve. The pipeline reactor is connected with heat collector, and from the bottom enters the heat collector. The pipeline reactor is S shape from the upper part of the heat collector. The product storage tank is set at the outlet end of the pipeline reactor. A glass cover plate is set at the front end of the heat collector and is coated with black coating.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the solar energy pipeline continuous biodiesel preparation device.    Product storage tank (1)    Pipeline reactor (2)    Black coating (3)    Glass cover plate (4)    Heat collector (5)    Valve (6)    Storage tank (7)
NOVELTY - An organic waste raw material, fats and oils, other than waste oil are mixed to obtain mixture. The obtained mixture is heated to more than 100 degrees C in anaerobic environment and carbonized (S4) by thermally-decomposing the organic compounds in the mixture, to obtain organic waste fuel (S5).    USE - Manufacture of organic waste fuel (claimed).    ADVANTAGE - The method efficiently and safely provides organic waste fuel with excellent handleability.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of organic waste fuel. (Drawing includes non-English language text)    Primary heat-processing (S1-S3)    Carbonization (S4)    Organic waste fuel (S5)
NOVELTY - The invention relates to a method and apparatuses for the production of materials or fuels, humus, Maillard or Maillard-like reaction products from a solid-fluid mixture of water and a carbon-containing component and for the treatment thereof, wherein the the solid-fluid mixture is treated at a temperature of over 100 DEG C and a pressure of over 5 bar. Feed materials are thereby fed continuously to a first reactor via a heat exchanger, and the reaction mixture is fed from one to a following reactor in a batch mode, and reaction products are continuously discharged from a last reactor.
NOVELTY - Disclosed is a new approach to cost-effective bacterial culture medium, which comprises bird feathers extract for production of toxins at an industrial scale. Also disclosed is an economical process for producing bio-insecticides. More particularly, disclosed is production of Bacillus sphaericus (Bs) and Bacillus thuringiensis variety israelensis (Bti)-based biopesticides, which utilizes cheap and locally available biological waste material through simple fermentation technology. Image 0/0
NOVELTY - Disclosed is a thin film sectionalized anaerobic digester (TFSAD), which comprises group or consortium of bacteria retained in a suitably designed digester, where solid retention time (SRT) is higher than hydraulic retention time (HRT) facilitating high rate efficient anaerobic digester (AD) to produce better quality and quantity of fertilizer and biogas with higher percentage of methane and nutrient in organic fertilizer. Image 0/0
NOVELTY - The device has a heatable carbonization reactor (1) operatively connected with a heating element and enclosed by a heating jacket, where external heat energy is supplied to the reactor. Cooling energy is supplied from a container or a cooling tank (9) to a gasification reactor (16). Moisture i.e. water, is supplied to the container or a cooling tank to ensure constant process control. Reaction gas is supplied from the carbonization reactor and/or the container or cooling tank to a gas accumulator (21) and to the gasification reactor.    USE - Device for thermo-chemical carbonization and gasification of aqueous and/or dry biomass for producing an energy carrier i.e. carbon, and/or raw material carrier (all claimed).    ADVANTAGE - The design of the device enables production of carbon and gases from the biomass for heating and driving devices in a simple, energy-saving and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for thermo-chemical carbonization and gasification of aqueous and/or dry biomass for producing an energy- and/or raw material carrier.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a device for thermo-chemical carbonization and gasification of aqueous and/or dry biomass for producing an energy- and/or raw material carrier.'(Drawing includes non-English language text)'    Heatable carbonization reactor (1)    Cooling tank (9)    Gasification reactor (16)    Gas accumulator (21)    Gas engine (48)
NOVELTY - Producing a fuel comprises (a) providing carbon dioxide (6), (b) providing hydrogen (11) from water and (c) synthesizing methanol from the supplied carbon dioxide and hydrogen, where carbon dioxide in step (a) is provided from a flue gas (4) of the combustion of the fuel.    USE - The method is useful for producing a fuel for internal combustion engines, preferably Otto engines.    ADVANTAGE - The method enables recycling of carbon dioxide, which is produced in the flue gases from the combustion of fuels in power plants, enables processing of the flue gases of power plants from fossil fuels and helps in converting methanol into dimethyl ether as diesel fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for producing a fuel.    Flue gas (4)    Carbon dioxide (6)    Hydrogen (11)    Methanol (12)    Dimethyl ether (18)
NOVELTY - The apparatus (110) has a stage (112) that mounts a to-be-processed resin (22) with a radioactive substance. The stage is positioned in the vacuum vessel (114). The voltage or an electric field is supplied to the upper space of the stage in the vacuum vessel by capacitive coupling. The electric power is supplied in the space with respect to the oxygen plasma using inductive coupling. The electric field is supplied for igniting oxygen plasma in the space.    USE - Resin reducing treatment apparatus used for nuclear facility.    ADVANTAGE - The stability of the plasma can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating resin reducing treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reducing treatment system.    To-be-processed resin (22)    Treatment reducing apparatus (110)    Stage (112)    Vacuum vessel (114)    Supply mechanism (122)
NOVELTY - A waste to fuel conversion process (P1) involves providing low-moisture carbon-based waste material; exposing the waste material to catalytic liquid reaction media under oxygen-free atmosphere within reactor; and recovering gaseous hydrocarbon fuel from the reactor.    USE - As waste to fuel conversion process (claimed) (where the fuel is used to power turbines and/or vehicles).    ADVANTAGE - The process enhances economically reasonable fuel sources; is environmentally friendly; and is also highly desirable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste to fuel process (P2) involving exposing solid carbon-based material to liquid reaction media to form hydrocarbon fuel mixture, where the fuel mixture comprises non-condensable hydrocarbon fuel and condensable hydrocarbon fuel; and separating the non-condensable hydrocarbon fuel from the condensable hydrocarbon fuel.
NOVELTY - The device comprises a control main machine (1), a raw material tank, a finished product oil storage tank (2), a circulating oil pump (3), an electromagnetic valve, a circulating pipeline, gauges, a gas metering device, and a 485 main line. The 485 main line is connected with the control main machine. The circulating oil pump is provided with the finished product oil storage tank. The raw material tank comprises an additive tank, a methanol tank (5) and a gasoline tank (6).    USE - The device is useful for preparing methanol gasoline.    ADVANTAGE - The device is capable of automatically and safely preparing the methanol gasoline with less energy consumption.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device of preparing methanol gasoline.    Control main machine (1)    Finished product oil storage tank (2)    Circulating oil pump (3)    Methanol tank (5)    Gasoline tank. (6)
NOVELTY - Method for producing biodiesel, fatty-acid-ethyl-ester (FAEE) and fatty-acid-methyl-ester (FAME) in vivo, involves inserting an exogenic cDNA of FAEES into algae genome, and expressing recombinant FAEES in algae, where insertion of the exogenic FAEES into algae genome enables the algae to produce recombinant FAEES, and it can be applied to other plants as well.    USE - The method is useful for producing biodiesel, FAEE and FAME in vivo. The FAEE and FAME is used in consumer goods, pharmaceuticals, functional food, drug and industrial product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of recombinant FAEES in algae synthesizes fatty acid ethyl ester in vivo from the fatty acids, using intrinsic ethanol or extrinsic ethanol and methanol produced by the organism.
NOVELTY - Refining oil comprises contacting an oil with hydrogen to perform a hydrodeoxygenation reaction using iron oxide as a catalyst, where the iron oxide comprises ferrous oxide, iron(IV) oxide, ferric oxide, and/or ferroferric oxide.    USE - The method is useful for refining oil including biomass degraded oil, biomass diesel oil, lubricating oil, edible oil, plastics degraded oil, and/or tired degraded oil (all claimed).    ADVANTAGE - The method: utilizes the magnetite powder, which after the reaction, is easily recycled; provides improved reaction rate; and decreases reaction pressure and energy consumption, and thus cost effective.
NOVELTY - A fuel supply pump (190) is located between fuel tank (180) and flow channel integration mechanism (111), so that fuel is supplied from fuel tank to fuel cell stack (140). The exhaust gas produced by reaction of the fuel cell stacks is flowed into fuel tank. The exhaust gas and vapor that enters gas-liquid separation tank (170) through flow channel integration mechanism is released to external environment of fuel cell system by condensation and evaporation device (150).    USE - Fuel cell system for electricity generation using fuel such as methanol or hydrogen and oxygen.    ADVANTAGE - The size of fuel cell system is reduced and leakage of fuel is prevented.    DETAILED DESCRIPTION - A supply terminal (220) is connected with container (210) and connector portion (221) having fuel delivery conduit (221a) and air line (221b), located in fuel feed line. A one-way valve (230) is connected to the air line, such that air is flowed to container.    DESCRIPTION OF DRAWING(S) - The drawings show the perspective views of fuel cell and fuel supply device.    Flow channel integration mechanism (111)    Fuel cell stack (140)    Condensation and evaporation device (150)    Gas-liquid separation tank (170)    Fuel tank (180)    Fuel supply pump (190)    Container (210)    Supply terminal (220)    Connector portion (221)    Fuel delivery conduit (221a)    Air line (221b)    One-way valve (230)
NOVELTY - Method of using soil improvement agent, involves performing saccharification of substrate containing biomass, fermenting the saccharified solution to obtain fermented solution, distilling the fermented solution to obtain ethanol, separating saccharified residue in saccharified solution, collecting distillation residual liquor, applying saccharification residue or distillation residual liquor in soil, and maintaining soil in oxidation state at particular temperature for one day.    USE - The method is useful for producing soil improvement agent used as basal fertilizer and additive for fertilizer.    ADVANTAGE - The soil improvement agent does not inhibit growth of plants, as degradation of easily degradable organic substance contained in the agent is increased, and generation methane gas is prevented.    DETAILED DESCRIPTION - Method of using soil improvement agent, involves performing saccharification of substrate containing biomass with saccharogenic amylase to obtain saccharified solution, fermenting the saccharified solution to obtain fermented solution, distilling the fermented solution to obtain ethanol, separating the saccharified residue in saccharified solution, collecting distillation residual liquor remained after distillation of fermented solution, applying saccharification residue or distillation residual liquor in soil, and maintaining soil in oxidation state at cumulative temperature of 20-1500 degrees C for one day.
NOVELTY - The system has a nitrification tank (11) that is arranged in the back stage of an adjustment tank (8). Intermittent-type aeration (9) and an agitator (10) are arranged in the nitrification tank. An agitator (12) is arranged in an anaerobic tank (13). An extraction pump (14) is provided to extract supernatant from nitrification tank. The waste water from nitrification tank is transmitted to the anaerobic tank through an exchange pump (15).    USE - Nitrogen removal system of dehydration filtrate used in sewage work such as human waste treatment plant and industrial-waste-water treatment plant.    ADVANTAGE - The density of organic substance can be maintained uniformly in the nitrification and anaerobic tanks, since waste water from nitrification tank is transmitted to the anaerobic tank through exchange pump. The decomposition of sludge floc in nitrification tank can be prevented efficiently. The pH value of nitrogen can be improved. The ammonia nitrogen contained in dehydration filtrate can be removed effectively. The occurrence of harmful microorganisms to water can be prevented. The organic substance in anaerobic tank can be secured reliably. The occurrence of sludge in nitrification and anaerobic tanks can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for nitrogen removal method of dehydration filtrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the nitrogen removal system of dehydration filtrate. (Drawing includes non-English language text)    Adjustment tank (8)    Intermittent-type aeration (9)    Agitator (10,12)    Nitrification tank (11)    Anaerobic tank (13)    Extraction pump (14)    Exchange pump (15)
NOVELTY - A nitrogen removal system of spin-drying filtrate comprises reaction tank (3) which consists of anaerobic tank (1) and aerobic tank (2) in which organic substance is supplied and decomposed, anaerobic digester tank (8) which performs anaerobic digestion process, sludge disposal system which stores temporarily the spin-drying filtrate which separates into solid and liquid with dehydrator (9) to adjustment tank, and nitrification tank which provides intermittent type aeration and agitator in back stage of the adjustment tank.    USE - Nitrogen removal system of spin-drying filtrate for human waste treatment plant and industrial-waste-water treatment plant.    ADVANTAGE - The water treatment process is reduced and the amount of nitrogen load is reduced.    DETAILED DESCRIPTION - A nitrogen removal system of spin-drying filtrate comprises reaction tank (3) which consists of anaerobic tank (1) and aerobic tank (2) in which organic substance is supplied and decomposed, anaerobic digester tank (8) which performs anaerobic digestion process, sludge disposal system which stores temporarily the spin-drying filtrate which separates into solid and liquid with dehydrator (9) to adjustment tank, nitrification tank which provides intermittent type aeration and agitator in back stage of the adjustment tank, extraction pump which extracts supernatant of nitrification tank in anaerobic tank and exchange pump which exchanges waste water of anaerobic tank. An INDEPENDENT CLAIM is included for a nitrogen removal process of the spin-drying filtrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the nitrogen removal system of the spin-drying filtrate. (Drawing includes non-English language text.)    Anaerobic tank (1)    Aerobic tank (2)    Reaction tank (3)    Anaerobic digester tank (8)    Dehydrator (9)
NOVELTY - A gas is supplied to fuel cell (2) and humidified with deuterium reduction water, and water is collected in the exhaust gas of fuel cell. Also claimed is apparatus.    USE - Manufacture of deuterium reduction water.    ADVANTAGE - The deuterium reduction water is efficiently manufactured with low concentration with respect to deuterium.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of deuterium reduction water manufacturing apparatus.    Fuel cell (2)    Generated water tank (3)    Water pump (4)    Raw water tank (5)    Downstream fuel cell (6)
NOVELTY - A biomass charcoal is prepared by collecting biomass materials, drying, removing impurities, crushing, putting into pyrolyzing furnace, and covering; opening an airflow adjusting valve on the carbonized furnace, beginning to heat, keeping at 90-120 degrees C for 6-8 hours, and removing residual water in the materials; sequentially heating to 190-210 degrees C for 1.5-2.5 hours for pre-carbonization; sequentially adjusting furnace temperature to needed carbonization temperature, and performing pyrolysis carbonization in sealed anaerobic environment for 5-15 hours; and cooling the materials.    USE - Method for preparing biomass charcoal (claimed).    DETAILED DESCRIPTION - Preparing biomass charcoal comprises:    (A) collecting biomass materials, drying, removing impurities, crushing, putting into pyrolyzing furnace, and covering;    (B) opening an airflow adjusting valve on the carbonized furnace, switching power supply into connection, beginning to heat, keeping at 90-120 degrees C for 6-8 hours, and removing residual water in the materials;    (C) sequentially heating to 190-210 degrees C for 1.5-2.5 hours for pre-carbonization;    (D) sequentially adjusting furnace temperature to needed carbonization temperature, and closing the airflow adjusting valve on the carbonized furnace so that the materials go through pyrolysis carbonization in the sealed anaerobic environment for 5-15 hours; and    (E) cooling the materials after carbonization to less than or equal to 60 degrees C, opening movable fire grate on bottom of the furnace and sealed baffle plate of discharge port, and discharging the prepared biomass charcoal from the discharge port.    An INDEPENDENT CLAIM is included for a carbonized furnace for preparing the biomass charcoal.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a carbonized furnace.
NOVELTY - The method comprises uniformly mixing a dehydrated sludge with 30% of concentrated hydrogen peroxide, heating the mixture at a temperature of 60 degrees C for 10-30 minutes, adjusting the temperature of the sludge to 55-60 degrees C, adding the sludge into an anaerobic fermenting pot and uniformly mixing, and performing anaerobic fermentation process at 50-60 degrees C. A solid content of the dehydrated sludge is of 20%. A dose of the hydrogen peroxide is 1-2.    USE - The method is useful for improving performance of municipal sludge dry fermentation performance process.    ADVANTAGE - The method is capable of simply and economically improving performance of the municipal sludge dry fermentation process in a real time manner.
NOVELTY - Microbial fuel cell (MFC) method for generating electricity performance and strengthening sludge reduction, where the residual sludge (3) in the total chemical oxygen demand is 9000-13000 mg/liter, involves adding sodium chloride (NaCl) with enhanced conductivity in the remaining sludge, and adding neutral protease and alpha-amylase for the MFC power generating performance, and adding neutral protease and alpha-amylase of the excess sludge microbial fuel cell with the operating temperature of 40-50 degrees C.    USE - For generating electricity performance and strengthening sludge reduction (claimed).    ADVANTAGE - The method is quick, simple, and convenient with low cost; and recycles clean energy at the same time processing the sludge, which not only process the waste, and effectively utilizes the resource.    DETAILED DESCRIPTION - Microbial fuel cell (MFC) method for generating electricity performance and strengthening sludge reduction, where the residual sludge (3) in the total chemical oxygen demand is 9000-13000 mg/liter, involves adding sodium chloride (NaCl) with enhanced conductivity in the remaining sludge, and adding neutral protease and alpha-amylase for the MFC power generating performance, and adding neutral protease and alpha-amylase of the excess sludge microbial fuel cell with the operating temperature of 40-50 degrees C, where the adding amount of NaCl per liter of residual sludge is 180-220 mmol, the adding amount of neutral protease is 8-12 mg, and adding amount of alpha -amylase is 1000 mg on total chemical oxygen demand in residual sludge, where the mass ratio of the neutral protease and alpha -amylase is 1:1-4.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of assembled MFC device.    Tap water (2)    Residual sludge (3)    Anode (4)    magnetic power (5)    Resistor (7)
NOVELTY - Resistance heating composition comprises: carbon nanotubes; an ionic liquid; and a binder resin.    USE - The resistance heating composition is useful: in product of heating composite; and heating apparatus of fusing apparatus (all claimed).    ADVANTAGE - The resistance heating composition: exhibits high heating uniformity and low temperature variation; utilizes carbon nanotubes that exhibits semiconductor properties, metallic properties, improved electrical characteristics, high mechanical strength, thermal conductivity and chemical stability; provides stably processed heating composite; and provides increased printing speed with reduced power consumption, thus exhibiting high heating rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a heating composite comprising a product of the resistance heating composition;    (2) a heating apparatus, comprising a base, and the heating composite disposed on the base, where the heating composite comprises a product of the resistance heating composition; and    (3) a fusing apparatus for a printing apparatus, comprising the heating apparatus configured in a roller form or a belt form, and the base, the heating composite disposed on the base, where the heating composite comprises the product of the resistance heating composition and an insulating layer disposed on a surface of the heating composite opposite the base, and a pressing device facing the heating apparatus.
NOVELTY - Producing ethanol, comprises contacting feedstock comprising acetic acid and hydrogen in reaction zone at hydrogenation conditions including elevated temperature with catalyst composition comprising platinum, palladium and tin on support, where the catalyst has excess amount of platinum relative to amount of palladium based on weight.    USE - The process is useful for producing ethanol (claimed), which is used: in fuels, chemical feedstocks, pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption and solvents for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks, and pharmaceuticals; and as a chemical feedstock to produce chemicals including vinegar, ethyl acrylate, ethyl acetate, ethylene, glycol ethers, ethylamines, ethyl benzene, aldehydes, butadiene, and higher alcohols (butanol).    ADVANTAGE - The process converts greater than 30% of acetic acid.
NOVELTY - Manufacturing turbine and/or diesel fuels, comprises: dehydrating an alcohol feedstock with at least one solid catalyst at 200-400 degrees C to produce an olefin mixture; oligomizering the mixture directly with at least one metallocene based Ziegler Natta catalyst and methylaluminoxane (MAO) cocatalyst to produce oligomer mixture having unreacted olefins and oligomers; introducing an isomerization catalyst to produce in situ, a bimetallic isomerization/oligomerization catalyst to convert the unreacted olefins to oligomers formed through 1,2-addition, and hydrogenating and distilling the oligomers.    USE - The process is useful for manufacturing turbine and/or diesel fuels e.g. ethanol, n-butanol, n-pentanol used as gasoline replacements in e.g. jet aircraft propulsion and military vehicles.    ADVANTAGE - The process improves the yield by efficient conversion of mixed olefin feedstocks to fuels.    DESCRIPTION OF DRAWING(S) - The figure shows a generic diagram for the conversion of mixed olefin feedstocks to turbine and diesel fuels.
NOVELTY - Anaerobic composition system (1) has material supply tub (10), mixer (20), heat hydrolyzed tub (30) and anaerobic digester (40). The material supply tub is used for supply and storage of organic waste. The mixer is provided with pump for mixing organic waste. The heat hydrolyzed tub subjects the organic waste to heat hydrolysis at high temperature and high pressure for disassembling toxic material. The anaerobic digester is capable of producing biogas through anaerobic digestion reaction of the heat hydrolyzed organic waste and phase change materials of paraffin.    USE - As anaerobic composition system.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of anaerobic composition system. (Drawing includes non-English language text)    Anaerobic composition system (1)    Material supply tub (10)    Mixer (20)    Heat hydrolyzed tub (30)    Anaerobic digester (40)    Silencer (50)
NOVELTY - The impurities excluding paper contained in toilet waste are removed, and the foreign substance is removed by crushing the toilet waste. Calorie regulators and coagulant are mixed with crushed toilet waste, dried at high temperature and pulverized to obtain solid fuel. The pulverized fuel is molded, squeezed and extruded to obtain solid fuel.    USE - Manufacture of solid fuel used for thermal power generation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel, which consists of calorie regulator (70-90 wt.%), coagulant (0.1-10 wt.%) and toilet waste (1-20 wt.%).
NOVELTY - The method involves mixing coal with collected sludge. The mixed sludge and coal are compressed and molded. The molded product is heated using heater and dried. The waste synthetic resin or waste plastic film is mixed with dried molded product. The waste synthetic resin or waste plastic film mixed dried molded product is again molded to specific thickness.    USE - Method for manufacturing substitute fuel (claimed).    ADVANTAGE - The substitute fuel can be manufactured easily and consumption of the substitute fuel is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for substitute fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating process for manufacturing substitute fuel. (Drawing includes non-English language text)
NOVELTY - The furnace has a water tank comprising a water tank outer barrel (7) and a water tank inner barrel (8). A horizontal clapboard (16) is set with a secondary air supply conical hopper (21) and divided into upper and lower parts, where the upper part is combustion chamber and the lower part is gasification chamber. A furnace top panel (13) is connected with the gasification chamber corresponding to a furnace opening in a furnace cover (12). The barrel is fixed with a steam air supply pipe (20). A chimney (14) is vertically fixed on the panel, and passes via the tank and the combustion chamber.    USE - Cooking and warming dual-purpose biomass gasification furnace    ADVANTAGE - The furnace has high fuel wide adaptability, and is simple to operate and convenient to use. The furnace occupies less space, and saves electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a cooking and warming dual-purpose biomass gasification furnace.    Water tank outer barrel (7)    Water tank inner barrel (8)    Furnace cover (12)    Furnace top panel (13)    Chimney (14)    Horizontal clapboard (16)    Steam air supply pipe (20)    Secondary air supply conical hopper (21)
NOVELTY - Device comprises feed pipe, valve, pressure gauge, exhaust pressure pipe, thermometer, pipe, spray pipe, tank, stirrer, manhole, filtering material, drain pipe, water inlet valve, discharge pipe, spray pump, bracket, air chamber, degradation chamber and liquid storage chamber.    USE - The device is useful for treating domestic waste (claimed).    ADVANTAGE - The device has higher efficiency, and is uniform and cost-effective.    DETAILED DESCRIPTION - Device comprises feed pipe, valve, pressure gauge, exhaust pressure pipe, thermometer, pipe, spray pipe, tank, stirrer, manhole, filtering material, drain pipe, water inlet valve, discharge pipe, spray pump, bracket, air chamber, degradation chamber and liquid storage chamber, where the device main portion is a cavity structure, top end of the degradation pipe is connected with feeding pipe, upper portion is provided with feed pipe, top end of the degradation pipe is provided with pressure gauge, other end of the water inlet valve is connected with the discharge pipe, discharge pipe is provided is provided with discharge device, and lower portion of the degradation pipe is divided into gas storage chamber.
NOVELTY - The device has a filter arranged at a top part of a furnace body. The furnace body is connected with an inner side of a furnace tube. An ignition system is provided with a rotating mechanism. The rotating mechanism is provided with a transmission mechanism and a driving mechanism. The rotating mechanism is arranged on an inner wall of the furnace tube. The transmission mechanism is connected with the driving mechanism. A pressing material cylinder is connected with a furnace cylinder.    USE - Biomass fuel gas generating device.    ADVANTAGE - The device provides stable gas and improves reliability, and is simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass fuel gas generating device.
NOVELTY - The gasifier has a barrel wall provided with a barrel-shaped gasifier unit (3). The gasifier unit is distributed with multiple air inlet nozzles (4) that are sleeved with an annular gasifier air bellow (2). The air bellow is connected with a gasification fan (1). A lower side of an ash funnel base seat (8) is fixed with the gasifier unit. An upper side of the barrel wall is provided with a drying pyrolysis region. An upper side of the gasifier unit is provided with a fuel gas outlet port that is connected with a fuel gas draft fan (7) via a pipeline.    USE - Fixed bed biomass gasifier.    ADVANTAGE - The gasifier improves oxidation temperature and reduces tar content so as to improve gas quality and working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fixed bed biomass gasifier.    Gasification fan (1)    Annular gasifier air bellow (2)    Barrel-shaped gasifier unit (3)    Air inlet nozzles (4)    Fuel gas draft fan (7)    Ash funnel base seat (8)
NOVELTY - The mechanism has a furnace liner provided in a shell. A feeding port is arranged on the shell and connected with an internal furnace. The internal furnace is provided with the furnace liner, a lower internal furnace and a furnace plate. The feeding port is connected to an upper furnace. A feeding opening of a furnace cover is arranged in a lower part of the internal furnace. The furnace liner is provided with a lower end surface and an upper end surface of a lower surface liner. The lower furnace liner is provided with a lower end surface of the furnace plate.    USE - Biomass fuel combustion mechanism.    ADVANTAGE - The mechanism is simple in design, convenient to change and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a biomass fuel combustion mechanism.
NOVELTY - The device has a combustion chamber (5) whose top part is provided with a feeding device. A bottom part of the feeding device is provided with a discharging device. A firing device (11) and an air blowing device (10) are connected with an air inlet (9). A wall of the combustion chamber is provided with a temperature detection device (19) and a rubbish fuel position detecting device. The feeding device, the discharging device, a blast device, a flue gas component detecting device (18), a temperature detecting device and a detecting head (20) are connected with an automatic control system.    USE - Rubbish fuel vaporizing device.    ADVANTAGE - The device ensures better environment effect by adopting organic waste process technique to avoid pollution in convenient manner. The device utilizes sawdust, crop straw and solid organic waste generated into combustible gas. The device has simple operation, automatic control and economic and social benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a rubbish fuel vaporizing device.    Combustion chamber (5)    Air inlet (9)    Air blowing device (10)    Firing device (11)    Flue gas component detecting device (18)    Temperature detection device (19)    Detecting head (20)
NOVELTY - The furnace has a furnace body whose top part is provided with a rubbish inlet and a pyrolysis gas outlet. A bottom part of the furnace body is provided with a fire grate and a bottom air inlet pipe. The furnace body is provided with two single furnace units that are provided with a common wall. The common wall of the single furnace units is connected with the bottom air inlet pipe and a furnace wall of the furnace body.    USE - Combined large-scale rubbish processing gasification furnace.    ADVANTAGE - The furnace has simple operation, and ensures independent rubbish gasification effect, saves cost, improves rubbish processing rate, reduces heat loss and ensures high production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a combined large-scale rubbish processing gasification furnace.
NOVELTY - Biomass conversion device comprises pyrolysis tank, three-phase purification and separation device, stationary separating device, gas purifying device, gas storage tank pneumatic device, cyclone separator and dust remover. The pyrolysis tank is connected to the three-phase purification and separation device. The three-phase purification and separation device is connected to a stationary separation device and the gas purifying device. The pneumatic device is installed on a pipeline which connects the three-phase purification and separation device and the gas purifying device.    USE - The device is useful for converting biomass into biomass gas, biomass wood vinegar, biomass tar or biochar.    ADVANTAGE - The device is simple, easy to operate and environmental-friendly; achieves biomass conversion rate of 0.5-1.5 tons/hour; simplifies pyrolysis unit; and is suitable for rural use.    DETAILED DESCRIPTION - Biomass conversion device comprises a pyrolysis tank, a three-phase purification and separation device, a stationary separating device, a gas purifying device and a gas storage tank. The pyrolysis tank is connected to the three-phase purification and separation device. The three-phase purification and separation device is connected to a stationary separation device and the gas purifying device. The gas purifying device is connected to the gas storage tank. The device further comprises a pneumatic device, a cyclone separator and a dust remover. The pneumatic device is installed on a pipeline which connects the three-phase purification and separation device and the gas purifying device. The cyclone separator is connected to the pyrolysis tank. The dust remover is connected to the purification and separation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass conversion device for converting biomass into biomass gas, biomass wood vinegar, biomass tar or biochar.
NOVELTY - Foldable flexible biogas storage tank comprises a main body of fermentation tank (1), an outer water seal groove of fermentation tank (2), an inner layer coated dome (3), a foldable flexible biogas storage tank (4), a peripheral column, a tension spring, a load balance, an inner layer coated dome hook (5), an outer foldable flexible gas storage tank hook. The main body of the fermentation tank is connected with the inner layer coated dome through the inner layer coated dome hook. The outer water seal groove of the fermentation tank is connected with outer foldable flexible gas storage tank.    USE - Used as a foldable flexible biogas storage tank.    ADVANTAGE - The foldable flexible biogas storage tank integrates the biogas storage tank and the fermentation tank.    DETAILED DESCRIPTION - Foldable flexible biogas storage tank comprises a main body of fermentation tank (1), an outer water seal groove of fermentation tank (2), an inner layer coated dome (3), a foldable flexible biogas storage tank (4), a peripheral column, a tension spring, a load balance, an inner layer coated dome hook (5), an outer foldable flexible gas storage tank hook. The main body of the fermentation tank is connected with the inner layer coated dome through the inner layer coated dome hook. The outer water seal groove of the fermentation tank is connected with the outer foldable flexible gas storage tank through the foldable flexible gas storage tank hook. The tension spring is connected with the peripheral column and the outer foldable flexible gas storage tank. The load balance is placed on the top of the outer foldable flexible gas storage tank.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the foldable flexible biogas storage tank.    Main body of fermentation tank (1)    Outer water seal groove of fermentation tank (2)    Inner layer coated dome (3)    Foldable flexible biogas storage tank (4)    Inner layer coated dome hook (5)
NOVELTY - The system has a fuming device with a combustion chamber (5). A combustion chamber top part is provided with a feeding device. An air outlet pipe (32) is connected with a bottom part of a chamber (38) of a fuel pipe (37) through a flue gas component detecting device (18). A purifying chamber (30) is formed close to the air outlet pipe and provided with a filtering device. An automatic control system is connected with the feeding device, a discharging device, a blast device and the detecting device. A combustible gas furnace uses wooden meal, crop straw and solid organic waste as fuel.    USE - Rubbish fuel fuming system.    ADVANTAGE - The combustible gas furnace uses wooden meal, crop straw and solid organic waste as fuel, thus avoiding environmental pollution effectively, improving combustion efficiency, increasing production efficiency and increasing fully automatic control and economic and social benefits. The system has convenient operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a rubbish fuel fuming system.    Combustion chamber (5)    Flue gas component detecting device (18)    Purifying chamber (30)    Air outlet pipe (32)    Fuel pipe (37)    Chamber (38)
NOVELTY - The method involves cutting leaves and stem of a plant, and drying the leaves and stem by pressing to obtain cubes or bales. The dried leaves and stem are chopped in specific size. The chopped leaves and stem are mixed in a ratio of 10 to 50 weight percent.    USE - Method for producing solid fuel from biomass of plant in Calamagrostis and Solidago species.
NOVELTY - Preventing mulberry pests, comprises applying total alkaloids (2%) and water in a ratio of 1:600-2500 by spraying 45-55/667 m2 on the mulberry leaf surface for 4 hours, and picking normal leaves for feeding silkworms after 5 days.    USE - The method is useful in preventing mulberry pests.    ADVANTAGE - The method is simple, economical, environmental friendly, and non toxic to humans and domestic animals.
NOVELTY - Preparing combustion coal by using sludge comprises (i) dehydrating the sludge, where the moisture content of the sludge is 40-55 wt.%, (ii) adding combustion improver and stabilizer to the sludge after dehydration, where the wt. % of the combustion improver after dehydration is 20-30%, and the wt. of the dried sludge after dehydration is 8-15%, (iii) stirring, and mixing the sludge, and (iv) introducing the mixture uniformly for rotational molding, and drying.    USE - The method is useful for preparing combustion coal.    ADVANTAGE - The method is simple, and economical; prepares combustion coal with a high combustion value (more than 5000 kilocalories); improves the combustion performance; saves coal; and promotes the sludge resource utilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for device for preparing combustion coal using sludge, comprising a water removing machine for dehydrating the sludge and then conveying to a sludge dehydrator conveying device. The sludge conveying device connected with the inlet end of the mixer connected with a material mixing and conveying device which is inturn connected with a forming device. The forming device is connected with a final product conveying device. The blender feeding end is connected with combustion supporting agent quantitative adding device and stabilizing agent quantitative adding device, where the sludge conveying device and the mixer is provided with a sludge meter.
NOVELTY - Processing city domestic sludge, comprises (i) adding microbial strain (10-25% the weight of the city domestic sludge) into city domestic sludge, and fermenting at 10-40 degrees C for 3-8 hours, and (ii) adding earthworm of Daping (0.5-1% the weight of city domestic sludge) into the fermented city domestic sludge for processing at 20-25 degrees C for 3-4 months at a humidity of 50-65%.    USE - The city domestic sludge and its product are useful for vermiculture, and as organic fertilizers in forestry and agricultural fields and as protein source in the livestock and poultry feed replacing fish meal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for product prepared by processing city domestic sludge, comprising earthworm and excrement of earthworm.
NOVELTY - Cultivation method for producing selenium enriched garlic plant, involves adding selenium source to garlic growth medium, adjusting the selenium content to 0.2-100 mg/kg in growth medium, and adding alkaline substance or alkaline solution to growth medium as a whole or in parts and adjusting pH f the medium to 7-8. The selenium exists as Se-methylselenocysteine which comprises a total selenium content of 80% or more.    USE - The cultivation method is useful for producing selenium enriched garlic plant.    ADVANTAGE - The method enriches selenium content in garlic plants to 3-1500 mg/kg, and is environmentally-friendly.
NOVELTY - Method for processing dry leaf blade embedded from tree leaves, involves selecting vegetable field in certain range, dividing vegetable field into 5 blocks, burying tree leaves in left 1-3 blocks, moving the mud of the field to one end, changing one half into pit, filling leaves in pit, adding sand in pit, watering cause corrosion, and after the half is full, and the other half is put into pit, and repeating front operation, growing vegetables to make vegetables absorb rotten leaf nutrient, and selecting fast mature variety.    USE - The method is useful for processing dry leaf blade embedded from tree leaves which is used as fertilizer.    ADVANTAGE - The method is environmentally-friendly. The rotten period of tree leaves are relatively long, thus does not generate harmful substance and makes soil property loosen.    DETAILED DESCRIPTION - Method for processing dry leaf blade embedded from tree leaves, involves selecting soil property in certain range of small area as vegetable field of river sand, dividing vegetable field into 5 blocks, burying tree leaves in left 1-3 blocks, moving the mud of the block land to one end, changing one half of field into pit, filling tree leaves in pit, after filling the tree leaves, adding sand in pit, watering cause corrosion and after the half is full, changing the other half into a pit, repeating front operation after the whole field is filled with tree leaves growing the vegetables, making the vegetables absorb rotten leaf nutrient to reduce environment pollution, changing field block wheel into grow vegetables and embed tree leaves in spring, summer and winter, reserving one block field for embedding tree leaves in autumn, reserving 2-3 block to embed tree leaves, where the planted vegetable variety is mature fast and improves turnover efficiency, and planted vegetables are capable of eating or feeding animals.
NOVELTY - Making biomass carbon fertilizer, involves air-drying biomass raw materials cornstalk and corncob and crushing; soaking the crushed cornstalk and corncob into modifier solution with concentration of 1-10% for 8-24 hours, and drying in electric heating constant temperature blast drying box at 80-100 degrees C; and pre-oxidizing the treated cornstalk and corncob in box type furnace at 245 degrees C for 0.5-2 hours, and carbonizing under oxygen deficit or oxygen-free condition at 250-650 degrees C for 0.5-4 hours, grinding and passing through a sieve of 10-100 meshes to obtain the biomass carbon fertilizer.    USE - For preparing biomass carbon fertilizer (claimed).    ADVANTAGE - The method is simple and low cost; reduces the emission of carbon dioxide gas by the biomass raw materials; and provides high yield of biomass carbon fertilizer. The biomass carbon fertilizer provides the crop product with higher quality and without secondary pollution to the soil of farmland.    DETAILED DESCRIPTION - Making biomass carbon fertilizer, involves air-drying biomass raw materials cornstalk and corncob and crushing; mixing the crushed cornstalk and corncob according to a mass ratio of (0-10):(10-0) and sum of mass ratios of 10, soaking into modifier solution with concentration of 1-10% for 8-24 hours, and drying in an electric heating constant temperature blast drying box at 80-100 degrees C; and pre-oxidizing the treated cornstalk and corncob in a box type furnace at 245 degrees C for 0.5-2 hours, and carbonizing under the oxygen deficit or oxygen-free condition at 250-650 degrees C for 0.5-4 hours, grinding and passing through a sieve of 10-100 meshes to obtain the biomass carbon fertilizer. The modifier is ammonium dihydrogen phosphate, diammonium phosphate, potassium dihydrogen phosphate.
NOVELTY - Method for extracting coixol from coix lacryma-jobi, involves crushing root of coix lacryma-jobi, extracting the crushed mixture using acid water, filtering the extracting solution using a nanofiltration membrane, concentrating the liquid using a reverse osmosis membrane, regulating pH of the liquid using ammonia water to 8-10, extracting the liquid for 2-3 times using chloroform, recycling the extract until the amount is reduced and crystallized, and recrystallizing the liquid using 75% ethanol solution to obtain the product.    USE - The method is useful for extracting coixol from coix lacryma-jobi.    ADVANTAGE - The method is easy, environmentally-friendly and suitable for industrial production, and consumes less energy.
NOVELTY - A counter biomass waste resource pyrolytic carbon gasification device comprises a heating carbon gasification furnace (1) comprising a vertical storage hopper connected to furnace body, heat exchange chamber, a gas buffer chamber having a biological heavy tar outlet, a combustion chamber having a grate and an ignition channel, and counter carbon gasification furnace (105); and a high temperature mixed gas separator (2) having a mixed gas inlet (2011) connected to counter carbon gasification furnace.    USE - A counter biomass waste resource pyrolytic carbon gasification device.    ADVANTAGE - Then device reduces pollution and saves resources.    DETAILED DESCRIPTION - A counter biomass waste resource pyrolytic carbon gasification device comprises:    (A) a heating carbon gasification furnace (1) comprising a vertical storage hopper connected to furnace body, heat exchange chamber, a gas buffer chamber having a biological heavy tar outlet, a combustion chamber having a grate and an ignition channel, and counter carbon gasification furnace (105); and    (B) a high temperature mixed gas separator (2) having a mixed gas inlet (2011) connected to counter carbon gasification furnace.    The vertical storage hopper has a storage bin cover. The furnace body has an ignition port (1081) and a carbon discharging opening. The heat exchange chamber has side walls having a water inlet and a water outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a counter biomass waste resource pyrolytic carbon gasification device.    Heating carbon gasification furnace (1)    High temperature mixed gas separator (2)    Counter carbon gasification furnace (105)    Ignition port (1081)    Mixed gas inlet (2011)
NOVELTY - A counter-burning biomass waste resource pyrolysis gasification device comprises a heating gasification furnace (1) comprising a vertical storage hopper connected with a furnace body, a heat exchange chamber having a heat exchange tube, a gas buffer chamber, an air buffer chamber connected to a smoke tube (105), a storage hopper cover, a pyrolysis chamber, a combustion chamber having a grate, a heat exchange chamber, and an ignition channel connected to the heat exchange chamber.    USE - A counter-burning biomass waste resource pyrolysis gasification device.    ADVANTAGE - The device reduces pollution, and saves resources.    DETAILED DESCRIPTION - A counter-burning biomass waste resource pyrolysis gasification device comprises:    (A) a heating gasification furnace (1) comprising a vertical storage hopper connected with a furnace body, a heat exchange chamber having a heat exchange tube, a gas buffer chamber, an air buffer chamber connected to a smoke tube (105), a storage hopper cover, a pyrolysis chamber, a combustion chamber having a grate, a heat exchange chamber, and an ignition channel connected to the heat exchange chamber; and    (B) a high temperature mixed gas separator (2) comprising a shell having a high temperature mixed gas inlet (2011), a static separation chamber, a biogas outlet, a biological mixed liquor outlet, and a biological fuel gas outlet.    The heat exchange chamber has water inlet and water outlet. The static separation chamber has a baffle plate, a clapboard dividing the separation chamber, a biological mixed liquor inlet, a mixed liquid inlet, a biological light tar outlet, a biological acid outlet, and a biological heavy tar outlet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a counter-burning biomass waste resource pyrolysis gasification device.    Heating gasification furnace (1)    High temperature mixed gas separator (2)    Smoke tube (105)    High temperature mixed gas inlet (2011)
NOVELTY - Producing green solid fuel by using biomass mixed material comprises (a) crushing the biomass mixed material to obtain particles (average diameter 10-30 mm), (b) then feeding (in wt.%) water (5-20), coal powder (5-30), lime (1-3) and sodium carboxymethyl cellulose (5-10) into the mixture obtained from the step (a), (c) heating the mixture under stirring condition at 150-250 degrees C for 1-3 hours, (d) naturally cooling the mixture at a cooling rate of 20-30 degrees C/minute, and (e) extruding the cooled mixture into a solid.    USE - The method is useful for producing green solid fuel by using biomass mixed material.    ADVANTAGE - The green solid fuel utilizes mixture of straw biomass, agro-forestry wood waste, waste plastic or urban organic solid waste as the raw material; ensures low heat disposal, synergistic effect between the materials, and continuous use; has high efficiency, high density and high calorific value; and is convenient to store and transport.
NOVELTY - The system has an exhaust device (6) that is provided with air storage tank (6a) connected with a dry-type anaerobic fermentation tank through a pipeline. A pretreatment pond (1d) of a feed system (1) is connected with a feed port of a dry-type anaerobic fermentation tank (2) through a pipeline. The anaerobic fermentation tank is connected with a heat preservation heating system (4) through pipeline. The dry-type anaerobic fermentation tank is connected with a sludge dewatering machine (5a) and a sewage treater (5b) of a biogas liquid and slag treating system (5).    USE - Anaerobic fermentation system.    ADVANTAGE - The organic resource of anaerobic fermentation system can be reduced. The organic resource can be recycled effectively. The recycling rate of organic resource can be reduced. The energy consumption of anaerobic fermentation system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the anaerobic fermentation system. (Drawing includes non-English language text)    Feed system (1)    Pretreatment pond (1d)    Dry-type anaerobic fermentation tank (2)    Heat preservation heating system (4)    Biogas liquid and slag treating system (5)    Sludge dewatering machine (5a)    Sewage treater (5b)    Exhaust device (6)    Air storage tank (6a)
NOVELTY - A Bacillus subtilis CH-001 strain deposited as CCTCC NO. M 2011111, is new.    USE - The B.subtilis CH-001 and its fermentation broth are useful for inhibiting Staphylococcus aureus, degrading keratin and collagen (all claimed), and for producing feed additive.    ADVANTAGE - The B.subtilis CH-001 has high stability and broad spectrum activity, and is cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for producing B.subtilis fermentation broth involves inoculating B.subtilis (0.1-0.5%) to inorganic salt-feather powder containing culture medium, performing shaking culture at 160 revolutions/minute, 35-41 degrees C and pH 7-8 for 12-36 hours until the cell density at optical density (OD)600 reaches 0.5 , where the culture medium (pH 8) comprises (in g/l): sodium chloride (0.5), potassium dihydrogen phosphate (0.4), dipotassium hydrogen phosphate (0.3), and feather powder (10); and (2) fermentation broth prepared by the method.
NOVELTY - Method for lignocellulose degradation, involves using dilute acid solution, lignin-degrading enzyme and cellulose-degrading enzyme.    USE - The method is useful for degrading lignocellulose. The degraded product is used as energy source for producing yeast biomass.    ADVANTAGE - The method has lignocellulose degradation rate of 70-90%, and causes no harm to environment.
NOVELTY - Water-soluble fertilizer and fine phosphate are manufactured by mixing water-insoluble phosphate mother liquor and transforming agent, controlling the pH of the mixture at 2-13, and reacting at 0-180 degrees C and pressure of 0-1 MPa.    USE - Method of manufacturing water-soluble fertilizer and fine phosphate.    ADVANTAGE - The method is simple and environment-friendly, has improved resource utilization rate, and reduces production cost.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of a method of manufacturing water-soluble fertilizer and fine phosphate (Drawing includes non-English language text).
NOVELTY - A honeysuckle fertilizer comprises (pts.wt.) amino acid fertilizer (18-28), organic fertilizer (17-27) and needed amount of azophoska.    USE - Honeysuckle fertilizer.    ADVANTAGE - The fertilizer can improve quality of honeysuckle and increase honeysuckle chlorogenic acid content by 12.9% and luteoloside content by 69.64% as compared to honeysuckle without being applied with the fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising preparing organic fertilizer by fermenting poultry excrement; preparing amino acid fertilizer by fermenting or hydrolyzing plant meal; and mixing organic fertilizer with amino acid fertilizer and azophoska.
NOVELTY - Isolating helenalin from single stamen Chrysanthemum, involves using Brazilian Chrysanthemum or dichromatism single-stamen Chrysanthemum as raw material, crushing the raw material, extracting the crushed product, collecting the extract, concentrating the extracted liquid, adding the extract to silica gel high-pressure column, performing petroleum ether-acetone gradient elution, recycling the reagent until proper volume is reached, crystallizing and performing dichloromethane or methanol recrystallization process, and obtaining the product.    USE - The method is useful for isolating helenalin from single stamen Chrysanthemum.    ADVANTAGE - The method has high extraction efficiency, is suitable for industrial production, and produces large amount of product. The product is environmentally-friendly.    DETAILED DESCRIPTION - Method of isolating helenalin from single stamen Chrysanthemum, involves using Brazilian Chrysanthemum or dichromatism single-stamen Chrysanthemum as raw material, crushing the raw material to 20-60 meshes, adding the crushed product to supercritical fluid extractor, extracting the crushed product using ethanol and supercritical carbon dioxide, collecting the extract, refluxing and extracting using acetone, concentrating the extracted liquid, extracting the concentrated product using n-butyl alcohol, adding the extract to silica gel high-pressure column, performing petroleum ether-acetone gradient elution, recycling the reagent until proper volume is reached, crystallizing and performing dichloromethane or methanol recrystallization process, and obtaining the product (helenalin).
NOVELTY - Preparing needle mushroom nutrient fluid by food processing residual comprises (i) taking needle mushroom as parent strain from a slant culture and inoculating into a first-grade shaking bottle, and amplifying and culturing to obtain a first-grade seed, (ii) inoculating bagasse as a main material to first-grade seed of the shaking bottle, taking out the solid culture medium of complete mycelium, and crushing to obtain mycelium powder, namely needle mushroom fermentation fungi, and (iii) extracting needle mushroom fermentation fungi by hot water leaching and amino acid as extraction solution.    USE - The method is useful for preparing needle mushroom nutrient solution.    ADVANTAGE - The method is environmental friendly, reliable and suitable for industrial production.
NOVELTY - Method for preparing diatom sample, involves discarding supernatant from water sample containing diatom to obtain diatomite precipitate, adding concentrated hydrochloric acid to precipitate, heating the solution, adding concentrated nitric acid to the precipitate, heating the solution, washing the precipitate, mixing the sample with alcohol to form suspension, coating the suspension to cover, heating and drying the cover, and adding one drop of naphrax to the slide and cover glass.    USE - The method is useful for preparing diatom sample.    ADVANTAGE - The method is rapid, simple, less-labor intensive, and environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing diatom sample, involves (a) obtaining water sample containing diatom, and discarding supernatant to obtain precipitate of diatomite sample, (b) adding concentrated hydrochloric acid to the precipitate, heating the solution for 2-3 hours at 95-98 degrees C, and removing supernatant, (c) adding concentrated nitric acid to the precipitate, heating the solution for 4 hours at 5 degrees C at constant temperature water bath of 95-98 degrees C, and removing supernatant to obtain precipitate, (d) washing the obtained precipitate using distilled water repeatedly, centrifuging the solution, and removing supernatant to obtain treated diatomite sample with 75%alcohol, (e) cleaning glass slides and cover slips placed on heating plate at 60-70 degrees C, and drying the slides, (f) mixing the sample with alcohol to form suspension, (g) coating the suspension to the upper portion of the cover, and heating and drying the cover for 20 minutes, (h) adding one drop of naphrax to the slide and cover glass, covering the slide with glue, and pressing cover, and (i) sealing the slide on alcohol lamp.
NOVELTY - A mixture is prepared using yellow soil pulverized material, barley stone pulverized material, zeolite pulverized material, germanium stone pulverized material, germanium stone pulverized material, enterolith pulverized material, paper manufacture wastewater sludge pulverized material (20-60 wt.%), waste lime pulverized material (5-20 wt.%), waste coal pulverized material (5-25 wt.%), food waste pulverized material (10-40 wt.%), waste oil (2-10 wt.%) and additive (2-10 wt.%). The mixture is molded and dried to obtain combustibles.    USE - Manufacture of combustibles.    DETAILED DESCRIPTION - Paper manufacture wastewater sludge is dehydrated and dried to have water content of 50% or less, and pulverized to obtain wastewater sludge pulverized material. Food waste is dehydrated and dried to have water content of 50% or less, and pulverized to obtain pulverized food waste of 100 mesh. Waste lime is dried and pulverized to 100 mesh. Waste coal pulverized material is prepared by pulverizing waste coal. Yellow soil is pulverized into 100 mesh to obtain yellow soil pulverized material, and mixed with barley stone pulverized material, zeolite pulverized material, germanium stone pulverized material and enterolith pulverized material. A mixture is prepared by mixing paper manufacture wastewater sludge pulverized material (20-60 wt.%), waste lime pulverized material (5-20 wt.%), waste coal pulverized material (5-25 wt.%), food waste pulverized material (10-40 wt.%), waste oil (2-10 wt.%), additive (2-10 wt.%) and obtained stone mixture. The obtained mixture (90-95 wt.%) and seawater (5-10 wt.%) are mixed and molded into pellet type molded material. The molded material is dried to obtain combustibles.
NOVELTY - Preparing ethanol fuel, involves (a) manually storing the biomass-free substances including metal, plastic and glass, and mechanically crushing the components, (b) adding the crushed kitchen garbage to liquefied enzyme, liquefying the obtained mixture, and maintaining the temperature to 80-100 degrees C, (c) adding saccharifying enzyme and pectinase to perform enzymolysis, and (d) inoculating alcohol fermentation dry yeast to perform anaerobic digestion.    USE - The method is useful for preparing ethanol fuel.    ADVANTAGE - The method requires no addition of water to dilute and sterilize at high temperature, reduces fermentation time of ethane, and saves water source and energy.    DETAILED DESCRIPTION - Method for preparing ethanol fuel using multienzyme complex and fractional hydrolysis of kitchen garbage, involves (a) manually storing the biomass-free substances including metal, plastic and glass which are collected from kitchen garbage, mechanically crushing the residual biomass components after leachating and draining oil from the components, and enabling the particle size of the crushed components to 8 mm or less, (b) adding the crushed kitchen garbage to liquefied enzyme (0.05-0.2 volume/volume%), liquefying the obtained mixture for 30 minutes, and maintaining the temperature to 80-100 degrees C, (c) utilizing a predetermined amount of sulfuric acid or sodium hydroxide to regulate the pH value of liquefying materials to 4.5-5, adding saccharifying enzyme (0.02-0.1 volume/volume%) and pectinase (0.005-0.02 volume/volume%) to perform enzymolysis for 2-4 hours at 45-50 degrees C, and (d) utilizing sulfuric acid or sodium hydroxide to regulate the pH value of materials to 5-6 after enzymolysis, inoculating alcohol fermentation dry yeast to perform anaerobic digestion at 30 degrees C, enabling the inoculums concentration to 0.3 volume/volume%, and enabling the fermentation time to 15-24 hours.
NOVELTY - A marine organism pet degerming liquid comprises (wt.%): marine organism element (6-7), cationic polymerization guanidine (3-4), Bacillus peptide (0.5) and purified water (balance).    USE - Marine organism pet degerming liquid for sterilizing pet breeding environment, pet hair, wounds, product for pets and pet odor.    ADVANTAGE - The liquid can effectively kill pathogenic enteropathogen, pyogenic coccus and pathogenic Saccharomycetes. It has 99.99% sterilizing rate, can effectively prevent various diseases, which is ideal disinfectant for family feeding pet, pet house and zoo. The liquid is also a marine biological environment-friendly product; does not contain iodine, chlorine, aldehyde, phenol, mercury and materials harmful to human and domestic animal; is colorless, flavorless, non-toxic, and has no corrosion, no stimulation, simple production technique, low cost and no pollution to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the marine organism pet degerming liquid which comprises slowly adding cationic polymerization guanidine into water in variable speed mixer; orderly adding marine active element and Bacillus peptide, adding deionized water; and uniformly stirring, qualifying, packing.
NOVELTY - A bio-organic fertilizer is produced by processing furfural residue and domestic sludge by drying, crushing and sieving until the granularity is 2-3 mm to obtain mixed material; adding yeast bacteria in the mixture, uniformly mixing, adding water, and using plastic film or canvas sealing for fermentation at 55-70 degrees C for 6-8 days and for 15 days at 20 degrees C; and spreading the ferment material, removing water until the water content is 8-10%, crushing into powder, and packaging finished product.    USE - Method for producing bio-organic fertilizer (claimed) used to adjust soil structure to promote crop to grow.    ADVANTAGE - The method can change waste into valuable material, has simple operation, and can eliminate environment pollution.    DETAILED DESCRIPTION - Producing bio-organic fertilizer comprises:    (A) collecting furfural residue and domestic sludge, and removing impurities, the water content being 12-15%;    (B) processing furfural residue and domestic sludge at a weight ratio of 3:2 by drying, crushing and sieving until the granularity is 2-3 mm to obtain mixed material;    (C) adding yeast bacteria in the mixture, uniformly mixing, adding water, and using plastic film or canvas sealing for fermentation at 55-70 degrees C for 6-8 days and for 15 days at 20 degrees C; and    (D) spreading the ferment material, removing water until the water content is 8-10%, crushing into powder, and packaging finished product.
NOVELTY - Preparing high purity steroid alkaloid germine (Germine) involves crushing black false hellebore raw drug, reflowing and extracting by ethanol, drying to obtain an extract, dissolving by acid solution, degreasing by diethyl ether, extracting by chloroform, concentrating to obtain total black false hellebore steroid alkaloid, hydrolyzing by alkali liquid, preparing germine by a chromatographic column separation process, namely column chromatography purification, recrystallizing, and drying to obtain a final monomer product.    USE - For preparing high purity steroid alkaloid germine (Germine) (claimed) used as a raw drug or as precursor of a germine derivative which is used for treating thrombolysis and platelet aggregation.    ADVANTAGE - The purity of the germine prepared by the method is more than 90%. The method involves simple operation step, provides high yield and has low impurity content, and avoids use of large amount of organic solvent, is environment friendly, and has strong feasibility.
NOVELTY - A granular fuel comprises (wt.%) livestock manure (60-80), biomass powder (10-30), and activated carbon (0.1-30).    USE - A granular fuel.    ADVANTAGE - The biomass powder is added to the livestock manure to remove the peculiar smell of the manure and reduce the ignition point of the fuel. The raw materials have wide source. The activated carbon provides 500-700 calories/kg heat for the fuel. The activated carbon generates carbon dioxide while burning, and the burning product does not pollute the environment.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the floatation system.    Storage device (11)    Distributing device (12)    Cylinder (13)    Hopper-shaped reflection device (14)    Floating plate (15)
NOVELTY - A regenerative coal comprises (pts.wt.) straw fuel (65-75), dry sludge organic cellulose (15.5-21.7), and dry sludge ash (9.5-13.3). The straw fuel is crop straw, sugar crop, starch crop and plant waste residue, forestry and wood waste, or municipal garbage. The dry sludge organic cellulose and dry sludge ash are generated from paper production.    USE - A regenerative coal.    ADVANTAGE - The regenerative coal has increased yield and is inexpensive. It is easy to produce, safe and reliable, energy-saving, and environment-friendly.
NOVELTY - Treating physicochemical three-phase resource waste comprises dividing the urban waste, selecting the plastic, crushing the waste, adding into a reaction tower to ferment and adding anaerobic bacteria, discharging the methane combustible gas released, discharging the generated solid fertilizer the bottom, dissolving the harmful heavy metals and ions in the liquid phase, separating the reaction liquid from the sludge into a purifier, adjusting pH, discharging a precipitate containing harmful heavy metal ions, and reflowing the liquid, allowing the sludge to enter into a culture tank to culture.    USE - The method is useful for treating physicochemical three-phase resource waste.    ADVANTAGE - The method processes multiple resources; eliminates secondary pollution; has low investment for devices; and is economical.    DETAILED DESCRIPTION - Treating physicochemical three-phase resource waste comprises (a) dividing the urban waste, selecting the plastic and other materials, (b) crushing the waste, (c) adding the crushed waste into a reaction tower to ferment for 5-10 days and adding anaerobic bacteria in the reaction tower, discharging the methane combustible gas released during the reaction from the top of the tower, discharging the generated solid fertilizer from the bottom of the tower, dissolving the harmful heavy metals and ions in the liquid phase, and (d) separating the reaction liquid from the sludge into a purifier, adjusting the pH to 9, discharging a precipitate containing harmful heavy metal ions, and reflowing the liquid, allowing the sludge to enter into a culture tank to culture, where the urban waste solid, liquid and gas three phase resource processing in the reaction tower utilizes combustion gas for the thermal processing of plastic separated from the waste.
NOVELTY - Waste landfilling based on bioreactor principle, comprises garbage landfilling, filtering waste, then collecting and processing the filtered solution, and using the filtered liquid for recharging the landfill waste, ensuring microbial degradation to generate landfill gas and discharging the filtered solution.    USE - The method produces garbage landfill gas useful for generating power or carrying out harmless treatment and then is discharged into the atmosphere (claimed).    ADVANTAGE - The method ensures strong and rapid degradation function, has short stabilization time, does not require treatment equipments and hence saves the cost.
NOVELTY - Preparing high-purity etioline comprises: (i) crushing Veratrum stenophyllum diels, performing thermal reflux extraction by using ethanol for 2-4 times, combining extracts, filtering and concentrating; (ii) diluting concentrated solution with water, adding into macroporous adsorption resin column, eluting with deionized water, ammonia water or sodium hydroxide aqueous solution and ethanol, to obtain eluent containing steroidal alkaloids, and vacuum concentrating; and (iii) separating etioline using high-speed countercurrent chromatography, concentrating, and drying.    USE - The method is useful for preparing high-purity etioline.    ADVANTAGE - The method is simple, environmental-friendly, and suitable for large-scale production; and produces high purity product.    DETAILED DESCRIPTION - Preparing high-purity etioline comprises: (i) crushing Veratrum stenophyllum diels, performing thermal reflux extraction by using ethanol (65-95%) for 2-4 times, extracting for 1-2.5 hours each time, combining the extracts, filtering, and concentrating to obtain a concentrated solution; (ii) diluting the concentrated solution with water, adding to a macroporous adsorption resin column, eluting the impurities with deionized water for 20 times, eluting with ammonia water or aqueous solution of sodium hydroxide (0.05-0.1%) for 10 times, eluting with ethanol (10-40%), and finally eluting with ethanol (75-95%) to obtain an eluent containing Veratrum stenophyllum steroidal alkaloids, and performing vacuum concentrating to obtain the extract; and (iii) taking chloroform-methanol-butanol-ammonia water (0.1%) as a solvent system, then separating the etioline by using a high-speed countercurrent chromatography, collecting the etioline component, concentrating, and drying to obtain the high-purity etioline.
NOVELTY - A chiral alpha -amino acid derivative is prepared by adding chiral sulfinyl ester imide compound into organic solvent, then adding halide metal reagent at -78 to 40 degrees C, and reacting for 0.2-2 hours; after reaction, adding ammonium chloride solution and quenching; extracting the aqueous phase with organic solvent, washing the organic phase with saturated saline, depressurizing and concentrating, and drying over anhydrous sodium sulfate; and purifying by silica gel column chromatography and eluting with petroleum ether and ethyl acetate.    USE - Method of preparing chiral alpha -amino acid derivative (claimed) used in preparing polypeptide drug.    ADVANTAGE - The method has simple operation, high diastereoselectivity, mild reaction condition, rapid synthesis speed, high yield, and low cost. The used materials are low in cost, easy to obtain, and stable to light and heat, do not generate noble metal and highly toxic product, thus the operation is safe. Further, the method is suitable for preparation of different substituted chiral alpha -amino acids and their derivatives.
NOVELTY - Manufacture of 2-(2-methyl phenoxy)-methylene phenyl methyl glyoxylate involves mixing 2-(2-methylphenoxy)-methylene benzoyl cyanide with bromide compound and concentrated sulfuric acid, reacting at 55-75 degrees C for 1-5 hours, cooling the reaction solution to 40-45 degrees C, adding lower alcohol, reflowing for 3-5 hours, cooling the mixture to room temperature, extracting by organic solvent, combining the organic layers and concentrating. The molar ratio of 2-(2-methylphenoxy)-methylene benzoyl cyanide, bromide compound and concentrated sulfuric acid is 1:20-120:1-10.    USE - Manufacture of 2-(2-methyl phenoxy)-methylene phenyl methyl glyoxylate.    ADVANTAGE - The 2-(2-methyl phenoxy)-methylene phenyl methyl glyoxylate is manufactured efficiently and economically with reduced energy consumption, by simple method.    DETAILED DESCRIPTION - Manufacture of 2-(2-methyl phenoxy)-methylene phenyl methyl glyoxylate involves mixing 2-(2-methylphenoxy)-methylene benzoyl cyanide with bromide compound and concentrated sulfuric acid, reacting at 55-75 degrees C for 1-5 hours, cooling the reaction solution to 40-45 degrees C, adding lower alcohol, reflowing for 3-5 hours, cooling the mixture to room temperature, extracting by organic solvent, combining the organic layers and concentrating. The content of solvent after being concentrated is less than 3%. The molar ratio of 2-(2-methylphenoxy)-methylene benzoyl cyanide, bromide compound and concentrated sulfuric acid is 1:20-120:1-10. The molar ratio of 2-(2-methylphenoxy)-methylene benzoyl cyanide and lower alcohol is 1:3.75-7.5.
NOVELTY - The module has a module filtering element arranged with a composition polymer membrane that is formed with a non-porous monolithic selectively layer, where the layer is made of poly-trimethylsilylpropyne and covered on a surface of a tape of porous material. Thickness of layer is about 0.5 to 5 m. The layer is dried at room temperature and atmospheric pressure. The composition polymer membrane is stored into butyl alcohol for 24 hours and dried in air to form constant mass.    USE - Biogas separating module.
NOVELTY - A food grade liquid carbon dioxide product producing method involves removing mechanical water, and desulfurizing the mechanical water. Carbon dioxide gas containing impurity is obtained, and methane and ethylene in the carbon dioxide gas are removed.    USE - Method for producing food grade liquid carbon dioxide product.    ADVANTAGE - The method enables producing the food grade liquid carbon dioxide product that can be preserved for a long time, in an inexpensive manner, and preventing potential safety hazard.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for producing food grade liquid carbon dioxide product.
NOVELTY - Method involves preparation of raw material, stage-by-stage treatment and obtaining of fuel. Preparation of raw material is performed by means of refining. Treatment is performed at three stages. At the first stage fish oil is mixed with absolute ethanol or methanol in ratio of 1:2-1:5. At the second stage concentrated sulphuric acid in quantity of 2-10% is added to the obtained mixture and ester interchange reaction is performed at temperature of not more than 40 degrees C during 20-60 min. At the third stage the mixture temperature is brought to boiling temperature and kept at this temperature during 60-480 min with separation into glycerin and mixture of ethyl or methyl ethers of fatty acids. Then, mixture is neutralised with alkali liquor, washed with water and settled. After that, impurities are removed by centrifuging so that fuel is obtained, which is then dehydrated and cleaned.    USE - Oil and gas industry.    ADVANTAGE - Improving physical and chemical properties. 3 cl, 1 tbl, 5 ex
NOVELTY - The apparatus has distilled water storage tank (60) whose inlet tube (61) is provided with pump (65) and connected with electrolyzer (10). The outlet (71) of gas filter (70) is connected to electrolyzer, through which hydrogen/oxygen-mixed gas generated from the electrolyzer is flowed. A controller (80) controls the drive of pump. A water level sensor (21) senses water level in inner side of electrolyzer. A pressure sensing sensor (23) reads pressure of inner side of electrolyzer. A temperature sensor (22) detects temperature of inner side of electrolyzer.    USE - Apparatus for generating hydrogen oxygen mixing gas.    ADVANTAGE - The distilled water filled in the storage tank can be controlled conveniently. The stability of the apparatus can be improved. The damaging of engine the oxy-hydrogen mixing gas can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for generating hydrogen oxygen mixing gas.    Electrolyzer (10)    Water level sensor (21)    Temperature sensor (22)    Pressure sensing sensor (23)    Distilled water storage tank (60)    Inlet tube (61)    Pump (65)    Gas filter (70)    Outlet (71)    Controller (80)
NOVELTY - The method involves injecting a material into an inner part of a furnace. The furnace is heated at 700 degree Celsius. Nitrogen is supplied to a heated material with natural gas mixing with liquefied natural gas (LNG) for preventing oxidation scale. A scull is ejected from the heated material. The natural gas is made of 20 to 28 weight percent of carbon monoxide, 30 to 40 weight percent of hydrogen, 0.1 to 1 weight percent of methane and 40 to 45 weight percent of nitrogen.    USE - Method for forming a hot press line.    ADVANTAGE - The method enables preventing generation of decarburization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hot press line forming apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a hot press line forming method.'(Drawing includes non-English language text)'
NOVELTY - A liquefied fertilizer manufacturing method involves: sprouting step comprising germinating the rice plant; mixing step comprising putting the sprouted rice plant into a fermentation tank at a ratio of 40-80 kg per 800 mu l of water; and fermentation step comprising mixing water in the fermentation tank and fermenting after putting the microorganism into the sprouted rice plant.    USE - Method for manufacturing a liquefied fertilizer that is utilized for a rice plant. No biological data given.    ADVANTAGE - The method enables manufacturing the liquefied fertilizer in an environmental-friendly manner.
NOVELTY - The system (100) has hydrogen transmission pipe (31) that is connected to one side of seawater electrolysis facility (30) to transfer effluent e.g. hydrogen generated in electrolysis process. The seawater electrolysis facility is provided to use seawater to produce chlorine material. A fuel cell e.g. polymer electrolyte fuel cell (PEMFC) or phosphoric-acid fuel cell (PAFC) is connected to the hydrogen transmission pipe to produce electricity from the effluent.    USE - Fuel cell system used in nuclear power generation system and thermal power generation system (all claimed).    ADVANTAGE - The fuel cell system utilizes the effluent additionally generated and recycles useless thrown away effluent to generate electricity effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system.    Seawater electrolysis facility (30)    Fuel cell (31)    Heat exchanger (50)    Heating apparatus (60)    Fuel cell system (100)
NOVELTY - The system has a hydrogen storage transfer pipe connected with a side of a seawater electrolysis facility for transferring an effluent that is generated in an electrolysis process. A fuel cell is connected with a hydrogen transmission pipe. A minor hydrogen storage part is connected with the hydrogen storage transfer pipe. An electric hybrid car is connected with a fuel cell rear end. A hydrogen refining facility refines a part of the effluent. A hydrogen agent wet apparatus dehumidifies hydrogen. The hydrogen refining facility is electrically connected with the fuel cell.    USE - Hydrogen charge and electric charge combined system for an electric charger that is utilized to charge an electric vehicle i.e. electric hybrid car.    ADVANTAGE - The system generates direct current power without a separate rectifier, so that the system is convenient to recycle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen charge and electric charge combined system.'(Drawing includes non-English language text)'
NOVELTY - The system (100) has hydrogen transmission pipe (31) that is connected to one side of seawater electrolysis facility (30) to transfer effluent e.g. hydrogen generated in electrolysis process. The electrolysis facility is provided to use seawater to produce chlorine material. A fuel cell e.g. polymer electrolyte fuel cell (PEMFC) or phosphoric-acid fuel cell (PAFC) is connected to the transmission pipe to produce electricity from the effluent. A direct current (DC)-alternating current (AC) converter (41) converts DC electricity produced in fuel cell into AC electricity.    USE - Fuel cell system used in nuclear power generation system and thermal power generation system (all claimed).    ADVANTAGE - The fuel cell system utilizes the effluent additionally generated and recycles useless thrown away effluent to generate electricity effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Seawater electrolysis facility (30)    Hydrogen transmission pipe (31)    DC-AC converter (41)    Heating apparatus (60)    Fuel cell system (100)
NOVELTY - The present invention relates to a continuous system and method for producing bio-diesel, The continuous method for producing bio-diesel comprises the following steps of: (a) pressurizing and heating a liquid state alcohol to reach a subcritical state or a high-pressure liquid state; (b) utilizing a continuous extraction module to perform continuous extraction, wherein the continuous extraction module has a plurality of extraction tanks, and at least one of the extraction tanks is used for receiving alcohols at the subcritical state or high-pressure liquid state and performing extraction from the grease material source in the extraction tanks so as to obtain a extracted product; (c) performing transesterification for the extracted product to obtain a transesterification product; and (d) separating the transesterification product to obtain the bio-diesel. The continuous system and method for producing bio-diesel according to the present invention utilizes alcohols at subcritical state or high-pressure liquid state to extract grease and produces bio-diesel through supercritical alcohol transesterificaition, and the extraction is performed by means of continuous extraction modules and method. Since the system utilizes the same alcohol for both extraction and transesterification processes to simplify the processes and to save the man power and energy resource.
NOVELTY - Improved preparation of fatty acid alkyl-esters (FAAE) from triglyceride oils using solid base catalysts, comprises: (i) mixing alcohol and triglyceride; (ii) adding the catalyst to alcohol-oil mixture; (iii) heating the alcohol-oil mixture as obtained in step (ii) in an oil bath to form reaction mixture; (iv) filtering the reaction mixture as obtained in step (iii) to separate the catalyst from the reaction products; (v) separating glycerol from the filtrate as obtained in step (iv) to obtain fatty acid alkyl esters.    USE - The process is useful for preparing fatty acid alkyl-esters (FAAE) from triglyceride oils using solid base catalysts (claimed).    ADVANTAGE - The process is highly improved and uses very low alcohol/oil molar ratio and catalyst and/or products are easily separable after the reaction through simple physical processes. The properties of thus obtained biodiesel meet the standard biodiesel values and can directly be used as transport fuel. Also, the process uses water alone as the reaction medium (or solvent) for the synthesis of precursors.    DETAILED DESCRIPTION - Improved preparation of fatty acid alkyl-esters (FAAE) from triglyceride oils using solid base catalysts, comprises: (i) mixing alcohol and triglyceride oil in a molar ratio of alcohol:oil in the range of 1.5:1 to 30:1; (ii) adding the catalyst to alcohol-oil mixture as obtained in step (i) in the range of 1 to 12 wt.% with respect to the triglyceride oil taken; (iii) heating the alcohol-oil mixture as obtained in step (ii) in an oil bath having temperature in the range of 30-100 degrees C for a period in the range of 1-24 hours to form reaction mixture; (iv) filtering the reaction mixture as obtained in step (iii) to separate the catalyst from the reaction products; (v) separating glycerol from the filtrate as obtained in step (iv) to obtain fatty acid alkyl esters.
NOVELTY - The present invention relates to a trans-esterification method and equipment for producing bio-diesel, comprising: a tank in which a blended liquid including an ester material and an alcohol material is filled; and a shaft having one end where a catalyst reactor is disposed and the catalyst reactor has a solid catalyst immersing in the blended liquid.
NOVELTY - High energy density slurry comprises ground coal and a pretreated biomass slurry having a viscosity of less than or equal to 0.7 Pas and having a solid loading of at least 40 wt.%.    USE - The slurry is useful as feedstock for a hydro-gasifier for generating rich producer gas.    ADVANTAGE - The slurry exhibits: high energy density, thus making it pumpable; and a viscosity of less than or equal to 0.7 Pas, and thus it can be easily pumped into the reactor.
NOVELTY - Invention relates to waste processing methods, particularly methods of producing biogas from organo-containing wastes. The method involves adding a complex stimulant into the fermented organo-containing wastes, said stimulant containing ground phytomass of red amaranth and aerobically stabilised activated sludge in ratio 1:1 per 2-3 wt %, with subsequent treatment of the obtained mixture with ultrasound at frequency 22 kHz and intensity 6-8 W/cm for 4-8 minutes.    USE - Chemistry.    ADVANTAGE - Method significantly speeds up the process of methanogenic fermentation, reduces the temperature at which chemical reactions begin and considerably increases output of biogas. 2 tbl, 2 ex
NOVELTY - An application of soil improvement material involves carrying out saccharification process of substrate with saccharogenic amylase by making the rice straw as biomass into a substrate obtaining a saccharification solution, fermentation-processing of saccharification solution and obtaining a fermentation solution, separating saccharification residue in the solution, and collecting remaining distillation residual liquors after distillation of the fermentation solution when manufacturing ethanol according to the process of distilling the fermentation solution.    USE - Application of soil improvement material for paddy soil.    ADVANTAGE - Production of methane gas is suppressed.    DETAILED DESCRIPTION - An application of soil improvement material involves carrying out saccharification process of substrate with saccharogenic amylase by making the rice straw as biomass into a substrate obtaining a saccharification solution, fermentation-processing of saccharification solution and obtaining a fermentation solution, separating saccharification residue in the solution, collecting remaining distillation residual liquors after distillation of the fermentation solution when manufacturing ethanol according to the process of distilling the fermentation solution, and maintaining oxidation-reduction potential of the paddy soil in the range of plus minus 0-500 mV after applying saccharification residue or distillation residual liquor to paddy soil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the application of the soil improvement material. (Drawing included non-English language text.)
NOVELTY - An oxygen reduction catalyst comprises transition metal complex containing ligand which has the same number of oxygen and nitrogen atoms coordinated to transition metal. Transition metal has sintered body obtained by heating ligand forming compound having hydrogen atoms bonded to oxygen atoms.    USE - An oxygen reduction catalyst for fuel cell (claimed).    ADVANTAGE - Oxygen reduction catalyst is cheap, and oxygen reduction reaction is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell comprising electrolyte to which anion component can be moved and fuel side electrode and oxygen side electrode which are arranged on opposite sides of electrolyte, wherein oxygen side electrode contains oxygen reduction catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell. (Drawing includes non-English language text).    Fuel cell (1)    Fuel side electrode (2)    Oxygen side electrode (3)    Electrolyte layer (4)    Oxygen supply member (6)
NOVELTY - The method involves inputting biomass (1) over a pressure lock (2) into a low temperature deaerator (5). The gasification of fixed charcoal (7) is performed for thermally dividing long-chained pyrolysis gases (6) in a charcoal fixed bed gasifier (8) with descending gasification. The regenerative heating of low temperature deaerator is carried out with sensible heat of generator gas (9) and without cooling down generator gas. The dust is filtered from hot generator gases and incineration of dust free hot gas (12) is carried out in combustion chamber of a gas turbine.    USE - Method for performing integrated biomass overpressure fixed bed gasification of steam turbine in power plant.    ADVANTAGE - The power generation efficiency in power plants can be optimized favorably. The cost for performing integrated biomass overpressure fixed bed gasification can be reduced significantly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass overpressure fixed bed gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the fixed bed gasification method.    Biomass (1)    Pressure lock (2)    Low temperature deaerator (5)    Pyrolysis gas (6)    Fixed charcoal (7)    Charcoal fixed bed gasifier (8)    Generator gas (9)    Dust free hot gas (12)
NOVELTY - Recovery of oil from an aqueous solution containing oil and solids, comprises: adjusting the aqueous solution to an acidic pH; separating the oil- and solids-containing fraction from the acidic aqueous solution with an separation agent which is hydrophilic or assumes a hydrophilic character in response to water; recovering the oil- and solids-containing fraction separated using the separation agent; extracting oil away from solids with a water-insoluble extraction agent; and recovering the oil-containing water-insoluble extraction agent.    USE - The method is useful for recovery of oil from an aqueous solution containing oil and solids, where the separated solid is useful as a biomass or a soil improver, and the recovered oil is useful as a renewable transportation fuel, a lubricant or a raw material in processes to manufacture transportation fuels or lubricant components, and as a raw material in the manufacture of biodiesel or renewable diesel (all claimed).    ADVANTAGE - The method: enables both the recovery of oil from effluent and concurrently the reduction of an environmental burden caused by this effluent; is economical; and provides removing other organic matter e.g. polymeric carbohydrates from the aqueous solution, which reduces significantly the organic load of effluent and facilitates its handling.
NOVELTY - A field-scale composting reactor includes a base frame, a container pivotally mounted on the base frame, and a crank connected with the container and designed for the user to roll the container for agitation. The container is formed of a centric shaft and a housing mounted around the centric shaft. Six windows with meshes formed on the housing and a channel formed within the shaft are helpful for the air flow between the inside and outside of the container when the user agitates the container.
NOVELTY - The synthetic smokeless coal comprises main material including rice (57.9-77.9 parts by weight (pbw)) and corn starch main material (23.1-43.1 pbw), and auxiliary material including anthracite coal particle. The synthetic smokeless coal is prepared by polishing the rice particle and anthracite coal particle of 200 meshes, putting the materials into a stirrer, adding water at the same time using the corn starch and water of 1:2, uniformly mixing the materials to obtain the clinker of paste, and putting the paste in the coal manufacturing machine.    USE - Used as a synthetic smokeless coal.    ADVANTAGE - The synthetic smokeless coal can be economically, safely and reliably prepared with reduced energy consumption in an environmentally friendly manner, and is easy to store.    DETAILED DESCRIPTION - The synthetic smokeless coal comprises main material including rice (57.9-77.9 parts by weight (pbw)) and corn starch main material (23.1-43.1 pbw), and auxiliary material including anthracite coal particle. The synthetic smokeless coal is prepared by polishing the rice particle and anthracite coal particle of 200 meshes, putting the materials into a stirrer, adding water at the same time using the corn starch and water of 1:2, uniformly mixing the materials to obtain the clinker of paste, putting the paste in the coal manufacturing machine and then pressing into cylindrical or oval shape molded coal, maintaining the temperature at normal temperature, and finally drying the contents to obtain the synthetic smokeless coal.
NOVELTY - A hydrogen-generating apparatus (1A) comprises a hydrodesulfurization device (3) which removes the sulfur compound in supplied raw material, a hydrodesulfurization device (4) which removes the sulfur compound in the raw material which passed the hydrodesulfurization device (3) at a temperature in which the hydrodesulfurization device (3) is more than the temperature at which sulfur compound is removed, and a hydrogen generator (2) which generates hydrogen-containing gas using the raw material which passed the hydrodesulfurization devices (3) and (4).    USE - Hydrogen-generating apparatus is used for fuel cell system.    ADVANTAGE - The hydrogen-generating apparatus de-sulfurizes the raw material with high concentration of sulfur compound and suppresses the release and enlargement of heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen-generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of hydrogen-generating apparatus. (Drawing includes non-English language text)    Hydrogen-generating apparatus (1A,1B)    Hydrogen generator (2)    Hydrodesulfurization devices (3,4)    Housing (5)    Material supply device (6)
NOVELTY - A high concentration sodium chloride-containing organic waste liquid having high pH, is diluted, such that sodium chloride concentration is diluted. The resultant organic waste liquid is neutralized to the pH of 5.5-8.5, and subjected to methane fermentation process. Thus, organic waste liquid is processed.    USE - Processing method of organic waste liquid discharged during manufacture of soap and biodiesel.    ADVANTAGE - The method efficiently processes organic waste liquid at high speed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste disposal apparatus.
NOVELTY - Method for processing organic wastewater containing solid organic substance, involves performing organic acid fermentation of the organic wastewater containing solid organic substance, diluting the acid fermentation product with dilution water, carrying out aggregation process of the dilution liquid, separating the dilution liquid into solid and liquid, and performing methane fermentation of the collected supernatant.    USE - The method is useful for treating organic wastewater containing solid organic substance.    ADVANTAGE - The method is stable, lowers concentration of ammonia nitrogen in supernatant, prevents inhibition of methanogen in methane fermentation process, increases amount of soluble organic substance, and improves methane gas recovery.
NOVELTY - The sludge is cut by rotation of a rotation unit arranged at a cutting apparatus. The sludge is supplied to a carbonization furnace in which carbonization process is performed by burning the sludge. The temperature of carbonization furnace is detected (S202). The rotation speed of rotation unit of cutting apparatus is decreased (S206), by determining (S203) whether temperature of the carbonization furnace is more than predetermined temperature and by determining (S205) whether predetermined time is exceeded.    USE - Temperature control method of sludge carbonization process.    ADVANTAGE - The burning temperature of carbonization furnace is maintained as constant, by considering the self-sustained combustion process of sludge. Hence abnormal increase in temperature of the carbonization furnace by the self-sustained combustion process of sludge can be prevented. The stable control of temperature of sludge carbonization process can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge carbonization-process installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the temperature control method of sludge carbonization process. (Drawing includes non-English language text)    Step for setting sludge burning values to burning temperature controller (S201)    Step for detecting temperature in carbonization furnace (S202)    Step for determining whether temperature in carbonization furnace is more than predetermined temperature (S203)    Step for determining whether predetermined time of carbonization process is exceeded (S205)    Step for decreasing rotation speed of rotation unit of cutting apparatus (S206)
NOVELTY - A sliding component has an amorphous-carbon film containing silicon and nitrogen formed in the sliding face of a base material. The atomic ratio of nitrogen content to carbon content in the amorphous-carbon film is 0.1-0.25.    USE - Sliding component is used for motive power system.    ADVANTAGE - The sliding component has low friction coefficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of sliding component which involves forming amorphous-carbon film by plasma chemical vapor deposition on the sliding face of base material using hydrocarbon type gas, nitrogen gas and gas containing silicon atom as source gas; and    (2) a sliding structure which has a pair of sliding components that slide under unlubricated condition.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating relationship of nitrogen/carbon ratio and friction coefficient of sliding component. (Drawing includes non-English language text)
NOVELTY - The method involves detecting the temperature of circulating water supplied to high-pressure water electrolyzer (12). The electrolyzing process is performed with current density lower than the current density at the time of driving start of the water electrolyzer. The electrolyzing process is performed with current density preset based on temperature of circulating water at the time of the rated operation, when maintaining the constant temperature of the circulating water.    USE - Operating method of water electrolyzer used in water electrolysis system for electrolyzing pure water.    ADVANTAGE - The driving of water electrolyzer is operated with the current density lower than the current density at the time of driving start of electrolyzer, so that rapid raise of a cell voltage of electrolyzer is reduced. The size reduction of water electrolysis system is reduced and improvement of system efficiency is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the structure of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Water electrolyzer (12)    Water circulation apparatus (14)    Water supply apparatus (18)    Controller (20)
NOVELTY - A fuel contains mixed gas which comprises oxygen and hydrogen-containing gas, and combustible-gas component other than oxygen and hydrogen-containing gas, and is obtained by transmitting oxygen and hydrogen-containing gas to the vibration blade to which the vibration generated by the vibration generation unit is attached by the vibration rod and vibrating the vibration blade while making to-be-processed water produce vibration flow stirring when subjected to the electrolysis process.    USE - Fuel. Uses include but are not limited to internal combustion of vehicles and generators, fuel cell, and burner for boiler, cooking appliances and welding machine.    ADVANTAGE - The fuel is manufactured efficiently and safely by reducing emission of carbon dioxide, carbon monoxide or hydrocarbon.
NOVELTY - The method involves distributing oxalic acid nickel on a porous metal substrate (2). The porous metal substrate is heated by a heating part, where heating temperature of the porous metal substrate is less than or equal to 800 degrees Celsius. A nickel particle i.e. acicular nickel (7), is formed in the porous metal substrate. The nickel particle is arranged in a fuel electrode (3). An electrolyte (4) and an air electrode (5) are laminated by a lamination part. An oxygen ion conductor is provided with a porous membrane. The oxygen ion conductor is formed on the porous metal substrate.    USE - Method for manufacturing a solid oxide fuel cell i.e. metal support-type solid oxide fuel cell.    ADVANTAGE - The electrolyte and the air electrode are laminated by the lamination part, so that oxidation and heat deformation of the metal substrate during high temperature baking can be prevented and reduction of internal resistance of the cell and improvement of a dimension system can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a solid oxide fuel cell.'(Drawing includes non-English language text)'    Porous metal substrate (2)    Fuel electrode (3)    Electrolyte (4)    Air electrode (5)    Acicular nickel (7)
NOVELTY - A methane conversion collecting system of geological storage carbon dioxide comprises methane conversion part (1) equipped with cable (3) which electronically connects electrode well (10) with electrode well installed in underground storage layer (4) of carbon dioxide, and power supply device (2), wherein electrode well consists of separator (14) which prevents contact of electrode well outer wall (11), anode electrode (12), and cathode electrode (13), and cathode electrode arranges methane bacterium on surface in which contact with carbon dioxide is possible.    USE - A methane conversion collecting system of geological storage carbon dioxide (claimed).    ADVANTAGE - Energy supplies other than electronic supply are not required, and electric power, such as renewable energy, is effectively used.    DETAILED DESCRIPTION - A methane conversion collecting system of geological storage carbon dioxide comprises methane conversion part (1) equipped with cable (3) which electronically connects electrode well (10) with electrode well installed in underground storage layer (4) of carbon dioxide, and power supply device (2), wherein electrode well consists of separator (14) which prevents contact of electrode well outer wall (11), anode electrode (12), and cathode electrode (13), cathode electrode arranges methane bacterium on surface in which contact with carbon dioxide is possible, and separator has gas-liquid permeability. An INDEPENDENT CLAIM is included for methane conversion collection method of geological storage carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of a methane conversion part in a methane conversion collecting system.    Methane conversion part (1)    Power supply device (2)    Cable (3)    Underground storage layer of carbon dioxide (4)    Electrode well (10)
NOVELTY - A thermally-conductive type gas sensor (31) provided in the vicinity of a gas pipe (18) connected to the biogas generation tank (10) measures the density of one component gas such as hydrogen gas contained in a biogas generated by biogas generation tank. A flowmeter (32) measures the flow volume of biogas flowing through the gas pipe connected to biogas generation tank. A control apparatus (33) computes the production amount of one component gas based on the density of one component gas, and flow volume of biogas.    USE - Gas generation assistance apparatus of biogas production system (claimed).    ADVANTAGE - The creation state of the component gas contained in the biogas can be measured easily and rapidly by small and cheap structure.    DETAILED DESCRIPTION - The gas generation assistance apparatus (30) assists the generation of the biogas in the biogas generation tank that generates the biogas containing two component gas by which heat conductivity differs, by fermentation of the organic substance by microorganisms.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas production system provided with the gas generation assistance apparatus. (Drawing includes non-English language text)    Biogas generation tank (10)    Gas pipe (18)    Gas generation assistance apparatus (30)    Gas sensor (31)    Flowmeter (32)    Control apparatus (33)
NOVELTY - A multi-function continuous combined apparatus for lignocellulosic biomass pretreatment of cellulosic ethanol is invented. The system design includes the pressure isolation feeder, low-temperature screw-reactor vessel, continuous squeezer, high-temperature screw-reactor vessel, pressure relief device, flash receiver and steam and chemical injection package The apparatus can provide multi lignocellulosic biomass pretreatment processes such as acid/base catalyzed steam explosion pretreatment, two-step pretreatment process and hydrothermal steam explosion by mean of continuous feeding, transfer, mixing, high temperature reaction, solid-liquid separation and flash. Takes advantage of this performance, not only may apply development in the source of raw materials, but also may choice a suitable pretreatment process depend on the raw material characteristic and the sequentially hydrolysis and fermentation procedures. As a result, it can reduce the cost and improve the competitiveness of cellulosic ethanol industry.
NOVELTY - The method involves providing a cupola arrangement (250) for containing a metal bath. An inductive element (125) is operated to react with the metal bath by injecting air and oxygen enriched air or oxygen. Feedstock e.g. municipal solid waste (MSW), is supplied to the cupola arrangement. A plasma torch (115) e.g. carbon or graphite rod, arranged in a downdraft arrangement to work in series with the inductive element is operated on the metal bath selectably directly and indirectly by injecting steam (220) to enhance production of synthesis gas.    USE - Method for producing synthesis gas as a primary product from renewable feedstock e.g. organic compound, fossil fuel and hazardous material (all claimed).    ADVANTAGE - The method enables reducing emissions from operation of a cupola syngas plant and an amount of electricity needed for operating a synthesis gas cupola system. The method enables integrating an inductive heating system with optional plasma torch assistance into the cupola arrangement for producing the synthesis gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cupola arrangement showing an indirect application of a plasma torch positioned at an angle relative to a cupola.    Municipal solid waste (MSW)    Plasma torch (115)    Inductive element (125)    Steam (220)    Cupola arrangement (250)
NOVELTY - The fuel cell system (10) has a hydrogen generation system (12), and an electrical generation system (14) comprising a fuel cell (30). A gas buffer (40) stores hydrogen generated by the hydrogen generation system when the hydrogen generated exceeds an amount consumable by the fuel cell to generate electricity.    USE - Fuel cell system used to power any electronic device or to charge a battery. Uses include but are not limited to cell phones, personal digital assistants, personal gaming devices, global positioning devices and rechargeable batteries.    ADVANTAGE - Inflatable volume compensator in fluid communication with first pressure is provided to compensate for any volume imbalance between the reaction chamber and liquid reservoir. Water knock-out device is also provided to remove water or water vapor from hydrogen gas. Discrete individual fuel pellets are provided to allow a control of the volume and rate of hydrogen generation. Improves hydrogen production rates and hydrogen yields by improving contact between magnesium and iron and silicon. Produces uniform hydrogen generating reaction using only water as liquid reactant.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the fuel cell system.    Fuel cell system (10)    Hydrogen generation system (12)    Electrical generation system (14)    Fuel cell (30)    Gas buffer (40)
NOVELTY - An electrode (11a) comprises nickel-tungsten-sulfur (Ni-W-S) alloy film (2) provided on base material (1), wherein film contains 8-44 mass% S and 0.6-3 mass% W.    USE - An electrode for alkaline water electrolysis used for hydrogen-producing apparatus (claimed).    ADVANTAGE - Hydrogen-producing efficiency and current efficiency of electrode are improved, film is easy to manufacture at low cost, corrosion resistance is excellent, durability is favorable, and electrode can be used for a long period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of electrode (11a) for alkaline water electrolysis which involves depositing Ni-W-S alloy film (2) using dry-type film-forming method or wet film formation method by contacting Ni-W-S alloy plating liquid on base material (1) and forming Ni-W-S alloy film consists of 8-44 mass% S and 0.6-3 mass% W; and    (2) hydrogen-producing apparatus containing electrolysis cell arranges alternately the electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of a cathode electrode for alkaline water electrolysis in which Ni-W-S alloy film is provided as cathode electrode.    Base material (1)    Ni-W-S alloy film (2)    Electrode for alkaline water electrolysis (11a)
NOVELTY - Producing hydrogen gas comprises: sorbing a liquid hydrocarbon fuel to a gasification catalyst to form a sorbed hydrocarbon fuel; heating the sorbed hydrocarbon fuel to a first temperature for a first period of time sufficient to form coke; and gasifying the coke at a second temperature at a pressure for a second period of time in the presence of water and/or oxygen, so as to produce a gaseous mixture comprising hydrogen gas and carbon monoxide, and to regenerate the catalyst.    USE - The method is useful for producing hydrogen gas.    ADVANTAGE - The method: is carbon neutral; regenerates the catalyst; does not require additional heating while adsorption under ambient conditions, thus saving operating cost in energy savings and consequently also reducing carbon dioxide emissions; and utilizes lower temperature for the reaction due to the catalyst, thus improving the economy of the method.
NOVELTY - The method involves measuring temperature of a steam stream, temperature of a carbon-containing feedstock stream and temperature of a combined feedstock stream (30). A steam-to-carbon ratio is controlled within the combined stream. The temperature of the carbon-containing stream and the temperature of the combined stream are controlled based on the temperature of the steam stream. The combined feedstock stream is applied to a hydrogen-producing region (52) of a hydrogen-producing fuel processing system (12) to produce a mixed gas stream that includes hydrogen gas as a majority component.    USE - Method for actively controlling operation of a hydrogen-producing fuel processing system (claimed) in hydrogen-production and fuel cell industries to provide electric current or power to an energy consuming device. Uses include but are not limited to a light or lighting assembly, a household appliance, an appliance utilized in an office or other commercial establishments, a computer, and a signaling or communication equipment.    ADVANTAGE - The method enables utilizing feedback control strategy to maintain pressure of the carbon-containing feedstock stream at desired carbon-containing feedstock pressure and/or within desired carbon-containing feedstock pressure range to maintain the desired S/C ratio.    DETAILED DESCRIPTION - The carbon-containing feedstock includes methane, propane and natural gas. An INDEPENDENT CLAIM is also included for a hydrogen-producing fuel processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hydrogen-producing fuel processing system.    Hydrogen-producing fuel processing system (12)    Combined feedstock stream (30)    Hydrogen-producing region (52)    Optional controller (100)    Status signals (102)
NOVELTY - The method for concentrating alcohol involves sealing and storing an alcohol aqueous solution for predetermined period, on a laminate formed by extrusion laminating polyethylene terephthalate on at least one surface of a film-like substrate (B) having air permeability.    USE - Method for concentrating alcohol (e.g. ethanol and methanol) used as fuel for motor vehicles.    ADVANTAGE - The method efficiently and economically concentrates alcohol in alcohol aqueous solution, by a simple process, with reduced consumption of energy and chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for laminate used for alcohol concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the arrangement of apparatus for manufacturing laminate.    Die (1)    Die lip (2)    Chilled roll (3)    Pressure roll (4)    Substrate (B)
NOVELTY - Preparing a hydrocarbon, comprises: subjecting a bio oil from at least one renewable source to a hydrotreatment process, where, in the hydrotreatment process, hydrocarbons are formed from the bio oil in a catalytic reaction employing a catalyst, and an iron content of the bio oil is less than 1 wppm calculated as elemental iron.    USE - The process is useful for preparing hydrocarbon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a bio-oil intermediate, comprising a bio-oil from at least one renewable source, where the iron content of the bio oil is less than 1 wppm calculated as elemental iron.
NOVELTY - The system comprises a device (11) for generating dinitrogen, a device (12) for generating dihydrogen from water, a unit (13) for mixing dinitrogen and dihydrogen, a flow control unit installed to impose a value of flow at an exit of the dinitrogen and dihydrogen generation devices, a locking unit for blocking the flow values imposed at the exit of the dinitrogen and dihydrogen generation devices, and a unit for controlling a flow value to be imposed. The dihydrogen generation device comprises a proton exchange membrane (126), and a stack of cells.    USE - The system is useful for producing a mixture of dinitrogen-dihydrogen, and in a seal test apparatus (claimed) for telecommunication cables.    ADVANTAGE - The compact system is capable of easily producing the mixture of dinitrogen-dihydrogen, and provides efficient seal testing thus enhancing the lifespan of the cables.    DETAILED DESCRIPTION - The system comprises a device (11) for generating dinitrogen, a device (12) for generating dihydrogen from water, a unit (13) for mixing dinitrogen and dihydrogen, a flow control unit installed to impose a value of flow at an exit of the dinitrogen and dihydrogen generation devices, a locking unit for blocking the flow values imposed at the exit of the dinitrogen and dihydrogen generation devices, and a unit for controlling a flow value to be imposed. The dihydrogen generation device comprises a proton exchange membrane (126), and a stack of cells (125) of which each comprises the proton exchange membrane. INDEPENDENT CLAIMS are included for:    (1) a seal test apparatus; and    (2) a process for producing a mixture of dinitrogen-dihydrogen.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a system for producing a mixture of dinitrogen-dihydrogen.    Device for generating dinitrogen (11)    Device for generating dihydrogen (12)    Mixing unit (13)    Cells (125)    Proton exchange membrane. (126)
NOVELTY - Waste reclamation process comprises taking 100% of the food-contaminated waste streams from various fast food-serving facilities or venues and converting them all into usable products and energy sources with zero effluent and zero landfill.    USE - The process is useful for reclaiming solid waste from waste streams of fast food restaurants, casual dining restaurants, cafeterias, schools, colleges and universities, concession stands, arenas, stadiums, and other entertainment venues, and other places that offer simple food items for dine in or carry-out.    ADVANTAGE - The process is capable of reclaiming solid waste from waste streams of e.g. fast food restaurants in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIMS are included for a 100% post-consumer fuel pellet system with steady programmed BTU content from low-density poly, high density poly, extracted cup carton poly, sludge food waste and packaging chafe.
NOVELTY - Processing a biomass fuel compact comprises: combining a composition of combustible biomass materials; comminuting the composition of biomass materials; adding an adhesive to the biomass materials to form a composite biomass, where the adhesive comprises a starch and a hydroxide; forming the composite biomass into a shapeform; and heat treating the composite biomass shapeform at a base temperature sufficient to break O-H bonds, where the base temperature is below a torrefaction temperature of the composite biomass such that torrefaction of the biomass materials does not occur.    USE - The method is useful for processing a biomass fuel compact.    ADVANTAGE - The biomass fuel compact reduces emissions of greenhouse gas carbon dioxide into the atmosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass fuel compact manufactured by the method, where the combustible biomass materials include at least a portion of microwave receptors.
NOVELTY - A device comprises a salinity detecting probe (1), a salinity detector (3), an automatic control system (7), potassium concentrated solution storage tank (8), and a metering pump (11). The automatic control system is provided with analog-to-digital (A/D) signal converter, logic calculator, a D/A signal converter, A/D signal converter, logic calculator, and D/A signal converter which are connected in sequence. The salinity detector is connected with the A/D signal converter. The D/A signal converter is connected with the metering pump.    USE - Device for improving fresh active sludge nitration flora salt-resistant ability.    ADVANTAGE - The device can easily realize engineering operation, and has stable and efficient biological treatment effect.    DETAILED DESCRIPTION - A device comprises a salinity detecting probe (1), a salinity detector (3), an automatic control system (7), potassium concentrated solution storage tank (8), and a metering pump (11). The salinity detector is connected with the automatic control system. The automatic control system is connected with the metering pump. The metering pump is connected with the potassium concentrated solution storage tank. The automatic control system is provided with analog-to-digital (A/D) signal converter, logic calculator, a digital-to-analog (D/A) signal converter, an A/D signal converter, logic calculator, D/A signal converter which are connected in sequence. The salinity detector is connected with the A/D signal converter. The D/A signal converter is connected with the metering pump.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional diagram of the device for improving fresh active sludge nitration flora salt-resistant ability.    Salinity detecting probe (1)    Salinity detector (3)    Automatic control system (7)    Potassium concentrated solution storage tank (8)    Metering pump (11)
NOVELTY - An organic amino acid liquid fertilizer production device comprises stirrer (1), sterilizing natural ferment storage tank (2), normal temperature water tank (3), first filter (4), secondary fermentation tank (5), second filter (6), micro-generating bacteria feeding fermenting tank (7) and finished product tank (8) connected in turn. The stirrer, sterilizing fermenting naturally storage tank and secondary fermentation tank are respectively connected with an air supply device (9) through a pipeline.    USE - Device for producing organic amino acid liquid fertilizer (claimed).    ADVANTAGE - The device has simple structure, convenient use, low cost and good effect. It meets the requirement of environmental protection department, processes the waste in real time, and improves environmental sanitation.    DETAILED DESCRIPTION - Organic amino acid liquid fertilizer production device comprises stirrer (1), sterilizing natural ferment storage tank (2), normal temperature water tank (3), first filter (4), secondary fermentation tank (5), second filter (6), micro-generating bacteria feeding fermenting tank (7) and finished product tank (8) connected in turn. The stirrer, sterilizing fermenting naturally storage tank and secondary fermentation tank are respectively connected with an air supply device (9) through a pipeline. The stirrer, normal temperature water tank, first filter and micro-generating bacteria feeding fermenting tank are respectively connected with a water supply device (10) through the pipeline.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an organic amino acid liquid fertilizer production device.    Stirrer (1)    Sterilizing natural ferment storage tank (2)    Normal temperature water tank (3)    First filter (4)    Secondary fermentation tank (5)    Second filter (6)    Micro-generating bacteria feeding fermenting tank (7)    Finished product tank (8)    Air supply device (9)    Water supply device (10)
NOVELTY - Preparation of gasificationable bulk material from biogenous raw materials comprises delivery and acquisition of the materials dates, comminution of the materials, adjusting the moisture content to a target range and compaction of the comminute materials.    USE - The method is useful for the preparation of gasificationable bulk material.    ADVANTAGE - The process provides bulk material with excellent shelf life and good transportability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the gasification-capable bulk material from biogenous raw materials with many dimensionally stabilities and transportable solid individual bodies whose main ingredients are cellulose, hemicellulose, polysaccharides, peptides, lipids, resins and/or pectins.
NOVELTY - Methane tank comprises vertical cylindrical housing, reactionary portion which is filled with cattle-breeding drains, substrate with anaerobic biomass, upper and lower coating in form of cone, branch pipe for feeding wastewater, branch pipe for withdrawal of biogas and branch pipe for treated drain, in center portion of anaerobic biomass, which is in methane tank and/or in flow of anaerobic biomass, which is in portion of blades of intermixing device, and sources of ultrasonic fluctuations.    USE - Methane tank.
NOVELTY - A solid waste compost fermenter comprises a tank having concrete bottom floor (4) and side wall (5). The concrete of the floor has air ducts (2) that are uniformly arranged and pre-buried in it. Each air duct is uniformly provided with branch ducts (3), where a vent groove (1) is set at the outlet of the ducts and a timed small blast blower is installed outside to supply oxygen so as to form a static aeration system.    USE - As a solid waste compost fermenter (claimed).    ADVANTAGE - The fermenter solves the problem of blocking and damaging air ducts during the process of loading and unloading operations of the static aeration fermenting organic fertilizer; is cost-effective, convenient to operate fermenting, complete in sterilization and deodorization without secondary pollution; has high humification; is harmless; has excellent quality products; has high production efficiency; and is easy to popularize.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of solid waste compost fermentation tank section.    Vent groove (1)    Air ducts (2)    Branch pipe (3)    Bottom floor (4)    Side wall (5)
NOVELTY - A gas purification apparatus (100) comprises separation membrane (6) which separates source gas into purified gas and off-gas, cleaning unit to clean off-gas isolated by separation membrane and to absorb carbon dioxide, and off-gas return line (L1) which returns off-gas cleaned by cleaning unit to upstream of separation membrane. The gas purification apparatus purifies gas which has methane as main component and comes from source gas which has methane and carbon dioxide as main component.    USE - A gas purification apparatus for purifying gas with methane (claimed).    ADVANTAGE - The gas purification apparatus can effectively purify gas with high methane concentration. Installation space, amount of water, and number of pumps can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas purification apparatus. (Drawing includes non-English language text).    Compressor (2)    Water removal apparatus (3)    Separation membrane (6)    Gas purification apparatus (100)    Off-gas return line (L1)
NOVELTY - Removing contaminants, from a carbon dioxide feed stream, comprises: (a) providing carbon dioxide feed stream comprising contaminants at first pressure of 12-40 bar; (b) removing high boiling contaminants from compressed gaseous stream by scrubbing, absorption or adsorption to provide at least a carbon dioxide rich stream; (c) reducing pressure of carbon dioxide rich stream to second pressure which is at least 1 bar lower than the first pressure; (d) distilling carbon dioxide rich stream under second pressure obtained in step (c); and (e) providing contaminant depleted carbon dioxide stream.    USE - The method is useful for removing contaminants, preferably hydrocarbons from carbon dioxide feed stream (claimed).    ADVANTAGE - The method removes multiple contaminants from a carbon dioxide feed stream without the need for catalytic incineration at a lower cost.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the method of removing contaminants from carbon dioxide feed stream.
NOVELTY - The system has heater that heats biogas generated from organic waste e.g. livestock excretion, food waste or sewage disposal plant sludge with constant temperature. A water circulation heating switch is provided to circulate cooling water in the heater for heat-exchanging with biogas and to condense the biogas.    USE - Biogas concentration purification system.    ADVANTAGE - Since water circulation heating switch is provided to circulate cooling water in heater for heat-exchanging with biogas and to condense the biogas, the moisture in the biogas can be eliminated effectively. The system is provided with simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas concentration purification system.
NOVELTY - A 5-(4-bromobutyl)-N-(but-3-enyl)dodec-11-enamide (I) or its derivative, is new, where the compound (I) is effective against bacterial and viral pathogens.    USE - For manufacturing biologically active agent and pharmaceutical composition against bacterial and viral pathogens such as Mycobacterium tuberculosis, Bacillus subtilis, Bacillus pumilus, Bacillus cereus, Staphylococcus aureus, and Acinetobacter baumanii, and Human Immuno Deficiency Virus (HIV) (claimed).    ADVANTAGE - The compound is effective against multiple drug resistant and extensively drug resistant strains of Mycobacterium tuberculosis; and shows good activity against Streptomycin, Isoniazid, Rifampicin, and Ethambutol (SHRE) sensitive and SHRE resistant strains of Mycobacterium tuberculosis. The process of producing the compound (I) is a simple process and does not require complex laboratory set-up. Therefore, the process of production of compound (I) is economically viable. The compound (I) is a natural product, and is produced through naturally occurring microorganisms. Thus, the compound (I) itself or the process of producing the compound are eco-friendly and does not pose any threat to environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) preparation of the compound (I); 2) a composition (C1) comprising the compound (I) (0.1-50 mu g/ml) along with additives, excipients and adjuvants; 3) new actinomycete strain with accession no MTCC 5597 useful for producing the compound (I); 4) a biologically active agent comprising the compound (I), where the agent is effective against bacterial and viral pathogens; 5) a kit comprising the compound (I) or the composition (C1) along with an instruction manual.
NOVELTY - A xerogel catalyst comprises nickel-metal-alumina composite.    USE - Xerogel catalyst is used for manufacturing methane (claimed).    ADVANTAGE - The methane efficiently formed using the xerogel catalyst has improved conversion ratio.    DETAILED DESCRIPTION - A xerogel catalyst comprises nickel-metal-alumina composite (Ni-M-Al, where M is iron, cobalt, nickel, cerium, lanthanum, molybdenum, cesium, yttrium and magnesium). INDEPENDENT CLAIMS are included for the following:    (1) manufacture of xerogel catalyst, which involves forming aluminum precursor sol, fabricating aluminum precursor sol, mixing nickel precursor and nickel-metal-alumina sol, forming the nickel-metal-alumina sol, and mixing water, nickel-metal-alumina sol and alcohol solution with nickel-metal-alumina gel, aging and drying; and    (2) manufacture of methane, which involves performing hydrogenation process of nickel-metal-alumina catalyst and carbon monoxide under hydrogen and nitrogen.
NOVELTY - Methanol is made to contact with water in presence of catalyst and oxygen-containing gas is supplied to obtain reactant gas, and hydrogen gas is separated from the reactant gas. The supply of oxygen-containing gas is temporarily stopped using copper oxide/aluminum oxide catalyst.    USE - Manufacture of hydrogen gas.    ADVANTAGE - The hydrogen gas is manufactured at constant rate for a long period of time using catalyst having excellent durability.
NOVELTY - A biomass carbonizing furnace comprises a combustion chamber (5) having a feeding port (7), a discharging port (8) and a pyrolysis gas outlet (12); and a carbonization chamber (4) set above the combustion chamber and having a periphery provided with a heat transmission jacket.    USE - A biomass carbonizing furnace.    ADVANTAGE - The biomass carbonizing furnace saves energy, reduces fuel consumption, and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass carbonizing furnace.    Carbonization chamber (4)    Combustion chamber (5)    Feeding port (7)    Discharging port (8)    Pyrolysis gas outlet (12)
NOVELTY - Agricultural waste pyrolysis furnace comprises outer tube, inner tube, discharging port connected with outer tube, fire grate, discharge port, air outlet pipe, furnace cover arranged in opening of inner cylinder, feed inlet, and gas inlet. The inner two sides corresponding to side is provided with air outlet. The fire grate is arranged on inner cylinder and discharge hole. The outer tube forms annular passage with inner cylinder.    USE - Agricultural waste pyrolysis furnace.    ADVANTAGE - The agricultural waste pyrolysis furnace provides high conversion efficiency, and is suitable for agricultural waste comprehensive transformation in village or town factory. It has simple structure, easy to operate, and low cost.    DETAILED DESCRIPTION - Agricultural waste pyrolysis furnace comprises outer tube, inner tube, discharging port connected with outer tube, fire grate, discharge port, air outlet pipe, furnace cover arranged in opening of inner cylinder, feed inlet, and gas inlet. The inner two sides corresponding to side is provided with air outlet. The fire grate is arranged on inner cylinder and discharge hole. The outer tube forms annular passage with inner cylinder. The air outlet pipe is arranged on outer cylinder and connected with air vent pore to form gas extracting channel. The furnace cover has external cone shape provided with cloth. The furnace also includes distributing component for distributing plate assembly comprising motor and rotating shaft which is provided at center of furnace cover. The outer cylinder comprises annular water jacket having inner and outer walls. The side walls of annular water jacket are respectively provided with upper and lower inlet and outlet, while outer side face is provided with insulating layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of agricultural waste pyrolysis furnace.
NOVELTY - The method involves cooling a supply stream (4) for producing a cooled stream, and sending a part of the cooled stream to a fractionating column (6). Container stream (8) is drawn-off from the column where the container stream is enriched in methane with respect to the supply stream. Oxygen enriched stream (14) is drawn-off from the column with respect to the supply stream. Recycling stream (9) in the form of liquid is sent to a top of the column, where the recycling stream includes liquid, which is enriched in methane with respect to the supply stream.    USE - Method for cryogenic separation of methane in a supply stream containing oxygen and nitrogen, i.e. biogas, coming from a non-dangerous waste storing installation using a cryogenic separation apparatus (claimed) for purifying the biogas.    ADVANTAGE - The recycling stream enriches the composition of methane inside the fractionating column so as to avoid the risk of explosion inside the fractionating column.    DETAILED DESCRIPTION - The supply stream contains 3-35 percentage of oxygen and/or nitrogen.    An INDEPENDENT CLAIM is also included for an apparatus for cryogenic separation of methane rich feed containing oxygen in a supply stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for cryogenic separation of methane from carbon dioxide, oxygen and nitrogen.    Supply stream (4)    Fractionating column (6)    Container stream (8)    Recycling stream (9)    Oxygen enriched stream (14)
NOVELTY - The method involves cooling a supply flow i.e. supply gas (4), to produce a cooled gas flow, and transferring a portion of the cooled gas flow to a distillation column (6). A flow i.e. liquid (12), enriched in methane with respect to the supply flow is drawn from the distillation column. A flow (19) enriched in oxygen with respect to the supply flow, is drawn from the distillation column. A nitrogen-enriched flow (21) is transferred from a storage container (16) to a lower part of the distillation column for participation in distillation.    USE - Method for cryogenic separation of a methane enriched supply flow i.e. methane enriched supply gas, from carbondioxide, oxygen and nitrogen contained in biogas obtained from a non-dangerous waste storage facility, to obtain a purified biogas.    ADVANTAGE - The nitrogen-rich flow is sent from the storage container to the lower part of the distillation column for participation in the distillation, thus ensuring that operation of the distillation column is performed outside a flammable range.    DETAILED DESCRIPTION - The supply flow contains 65-97 percentage of methane, 3-35 percentage of total nitrogen and/or oxygen, and 95 percentage of nitrogen. An INDEPENDENT CLAIM is also included for an apparatus for cryogenic separation of a methane enriched supply flow containing oxygen and nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified schematic view illustrating a method for cryogenic separation of a methane enriched supply flow from carbondioxide, oxygen and nitrogen.    Supply gas (4)    Distillation column (6)    Methane enriched liquid (12)    Storage container (16)    Oxygen enriched flow (19)    Nitrogen-enriched flow (21)
NOVELTY - The apparatus (10) has an electrolysis cell (12) that contains anode and cathode. The anode and cathode are in electrical communication with power source (40). The electrolysis cell has one aperture for introduction of a fluid to undergo electrolysis and another aperture for the removal of gases. A condensation hood (70) is arranged within the electrolysis cell. A pump (58) is in fluid communication with the aperture for the removal of gases. The pump has sufficient capacity to reduce the pressure in the electrolysis cell to less than 0.1 atmosphere.    USE - Apparatus for electrolyzing water into hydrogen for generating power used as fuel in internal combustion engine e.g. diesel engine of vehicle. Can also be used in power generation for commercial building, home and portable equipment.    ADVANTAGE - The electrolysis cell under vacuum is maintained by increasing the gas generation and lowering the input power requirements, thus the electrolysis efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis apparatus.    Electrolysis apparatus (10)    Electrolysis cell (12)    Power source (40)    Pump (58)    Condensation hood (70)
NOVELTY - A catalyst comprises metal complex containing cobalt, iron or copper as a metal component, and nitrogen-containing polycyclic compound as ligand.    USE - Catalyst is used for electrochemical oxidation of hydride e.g. borohydride compound of alkali metal for direct fuel cell used in motor vehicle, mobile telephone and personal computer, and hydrogen-producing apparatus (all claimed).    ADVANTAGE - The catalyst is economical, and has excellent activity. The fuel cell formed using catalyst has excellent electric power generation efficiency, and reduced consumption of hydride.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) direct fuel cell, which has catalyst as anode pole, and uses borohydride as fuel; and    (2) hydrogen-producing apparatus (1), which has an ion-permeable separation membrane (4) arranged between anode-side electrode (2) and cathode-side electrode (3). The solution containing hydride and hydroxide is supplied to the anode-side electrode, and the cathode-side electrode is arranged opposite to the anode-side electrode. The hydrogen is generated by reductive reaction of proton using catalyst as anode-side electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the hydrogen-producing apparatus.    Hydrogen-producing apparatus (1)    Anode-side electrode (2)    Cathode-side electrode (3)    Ion-permeable separation membrane (4)    External circuit (5)
NOVELTY - Anaerobic reactor comprises water inlet pipe, water/gas dispersing device, support frame, biological belt, air inlet pipe, sludge discharge port and air outlet pipe. The support frame has spider net shaped structure distributed in center of circle with radial direction and located at upper part of reactor. The biological belt is double spiral belt, where the one end of double spiral belt is fixed on holder, and other end is free floating in water.    USE - The anaerobic reactor is useful in treatment of waste water and extraction of biogas energy from waste water.    ADVANTAGE - The reactor improves volume rate of gas production, maximizes distribution of bacteria in entire fermentation tank, and saves construction cost.    DETAILED DESCRIPTION - Anaerobic reactor comprises water inlet pipe, water/gas dispersing device, support frame, biological belt, air inlet pipe, sludge discharge port and air outlet pipe. The support frame has spider net shaped structure distributed in center of circle with radial direction and located at upper part of reactor. The biological belt is double spiral belt, where the one end of double spiral belt is fixed on holder, and other end is free floating in water. The water/gas dispersing device is equipped at bottom of the reactor, where the one end of tube is connected with water inlet pipe, and other end is connected with air inlet pipe.
NOVELTY - A solar-powered waste reducing device comprises a biodegradable waste degradation chamber. The degradation chamber comprises a waste inlet, a water drainage groove, and an accumulator; and is provided with a leachate back spraying pipeline. The leachate back spraying pipeline is provided with liquid return hopper and connected with a treatment box. The treatment box contains microbial catalyst.    USE - Solar-powered waste reducing device.    ADVANTAGE - The device provides biological catalyst for accelerating decomposition rate of waste.
NOVELTY - Device comprises storage box, electromagnet main body, electromagnet iron core and a connecting rod.    USE - The device is useful for processing garbage additive.    ADVANTAGE - The device is simple and convenient.    DETAILED DESCRIPTION - Device comprises storage box, electromagnet main body, electromagnet iron core and a connecting rod, where the storage box comprises a box body and a storage box panel, the lower part of the box body is set with a discharge spout, the electromagnet main body is arranged under a side wall of the box body, the electromagnet main body and the electromagnet iron core are connected, the electromagnet iron core is connected with one end of the connecting rod, and the other end of the connecting rod is provided with a connecting rod seat movable matched with the discharge spout at lower part of the box body.
NOVELTY - The fermentor comprises a can-body (1), a feeding pipe (7), a discharging pipe (3), an exit pipe (9) connected with the can-body, a storage pool, a slag processing device, a biogas purifying device, a heating pipe (13), a heating boiler, manholes and a thermometer. A lower part of the feeding pipe is connected with the discharge pipe. One side of the can-body is connected with the storage pool through the feeding pipe. Other side of the can-body is connected with the slag processing device through the discharging pipe. The exit pipe is positioned on a top of the can-body.    USE - The fermentor is useful in biogas engineering.    ADVANTAGE - The fermentor exhibits high production efficiency, has simple structure, and is convenient to use.    DETAILED DESCRIPTION - The fermentor comprises a can-body (1), a feeding pipe (7), a discharging pipe (3), an exit pipe (9) connected with the can-body, a storage pool, a slag processing device, a biogas purifying device, a heating pipe (13), a heating boiler, manholes and a thermometer. A lower part of the feeding pipe is connected with the discharge pipe. One side of the can-body is connected with the storage pool through the feeding pipe. Other side of the can-body is connected with the slag processing device through the discharging pipe. The exit pipe is positioned on a top of the can-body. The heating pipe is arranged on the can-body. The thermometer is placed on a heating boiler. An upper circulating pipe and a lower circulating pipe are connected with a circulating pump. A feeding valve is positioned on the feeding pipe. A discharging valve is positioned on the discharge pipe. An exit valve is positioned on the exit pipe. A stop valve is positioned on the heating pipe.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a fermentor.    Can-body (1)    Discharging pipe (3)    Feeding pipe (7)    Exit pipe (9)    Heating pipe. (13)
NOVELTY - A concentration pool comprises a fermentation tank, a concentration tank (1) connected to the fermentation tank, a biogas slurry pipe connected to the concentration tanks, a conveying pump (2) connected to the bottom part of the concentration tanks, a biogas pipe (3) connected to outlet of the conveying pump, and a feeding pipe.    USE - A concentration pool for irrigating farmland.    ADVANTAGE - The concentration pool has simple structure and long service life, is safe and reliable, has high efficiency in solid-liquid separation, and produces residue that can be used for producing organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a concentration pool.    Concentration tank (1)    Conveying pump (2)    Biogas pipe (3)    Hanger (6)
NOVELTY - The device has clapboard whose bottom portion is fixed on tank bottom plate. The upper portion of clapboard is staggered with parallel port and the tank casing. A mixing blade is fixed on stirring shaft. The stirring motor is connected with stirring shaft in tank casing. The feeding port is provided with side of clapboard corresponding to can portion. The discharge hole is provided on side outside can portion. The feeding opening is connected with liquid conveying pipe on discharging opening. The exhaust pipe is provided on side wall of inspection well.    USE - Biogas fermentation device used in vertical cylindrical pot.    ADVANTAGE - The problem related to miniaturization, low concentration, high construction cost, high operation cost, halfway reaction and abnormal production of biogas in winter of biogas pool can be solved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fermentation device used in vertical cylindrical pot.
NOVELTY - The auger type extractor comprises an engine, a clutch, an auger, and an absorption device. The auger is connected with the clutch through a connecting shaft. An air outlet of the engine is connected with the absorption device. The absorption device comprises an absorption container that is filled with an adsorbent.    USE - Used as an auger type extractor.    ADVANTAGE - The auger type extractor has simple structure, and can be economically manufactured with improved performance, long service life and less energy consumption in an environmentally friendly manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an auger type extractor.    Engine (1)    Clutch (2)    Connecting shaft (3)    Auger (4)    Absorption container. (6)
NOVELTY - A biogas pool discharging device comprises a motor (1); an upper transmission gear (2) fixed on output shaft of the motor; a lower transmission gear; a conveying belt (3) having a chain structure, and connected to upper transmission gear and lower transmission gear; hoppers (4); a connecting rod (5); a connecting rod length adjusting mechanism; a discharging port; and a supporting seat.    USE - A biogas pool discharging device.    ADVANTAGE - The device has quick and effective discharge performance, reduces labor intensity, eliminates manual operation, has simple structure, can adjust its length according to actual marsh gas pool size, and has strong adaptability.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biogas pool discharging device.    Motor (1)    Upper transmission gear (2)    Conveying belt (3)    Hoppers (4)    Connecting rod (5)
NOVELTY - The system has output filter (1) which is connected with DC-AC converter (2). The DC-AC converter and DC-DC converter (3) are connected in parallel to each other. A switch (5) is provided for controlling smart battery monitoring system (SBMS) intelligent storage battery group monitoring module (4) during off state. The storage battery group (6) is connected with parallel circuit. The AC-DC circuit (8) and DC-DC circuit (9) are connected in parallel to each other. AC-DC circuit and DC-DC circuit are connected to polymer hydrogen fuel battery (11).    USE - Hydrogen generating system.    ADVANTAGE - The power harmonic wave and commutation gap in the hydrogen generating system can be reduced. The power electronic element can be protected from main power supply peak current.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating system. (Drawing includes non-English language text)    Output filter (1)    DC-AC converter (2)    DC-DC converter (3)    SBMS intelligent storage battery group monitoring module (4)    Switch (5)    Storage battery group (6)    AC-DC circuit (8)    DC-DC circuit (9)    Polymer hydrogen fuel battery (11)
NOVELTY - The apparatus has a flotation tank filled with brown coal, hard coal and biomass. A reservoir bag is provided with a pump e.g. dredging pump. A mixture collector is installed in a particle separator. A rotating belt grill is provided with a mesh. An injection system is retained on the separator. The flotation tank is provided with a trigger. The trigger regulates liquid level in the flotation tank.    USE - Apparatus for recovery coke breeze from a slag removal system in a power boiler.
NOVELTY - The method of culturing Cordyceps militaris, comprises mixing fresh worm grass entity with alcohol (72-78%) and then soaking for 3-5 minutes to sterilize and cleaning by sterile water, cutting an outer layer of body, removing, from the outer layer of body, a white tissue of the culture medium for 8-15 days, and growing fuzzy mycelium strains by open culture entity in natural environment. The strain is added to the surface of pupa, and germinating the pupa active surface for parasitic living.    USE - The method is useful for culturing Cordyceps militaris.    ADVANTAGE - The method is capable of safely and energy efficiently culturing the Cordyceps militaris in an environmental friendly manner.    DETAILED DESCRIPTION - The method of culturing Cordyceps militaris, comprises mixing fresh worm grass entity with alcohol (72-78%) and then soaking for 3-5 minutes to sterilize and cleaning by sterile water, cutting an outer layer of body, removing, from the outer layer of body, a white tissue of the culture medium for 8-15 days, and growing fuzzy mycelium strains by open culture entity in natural environment. The strain is added to the surface of pupa, and germinating the pupa active surface for parasitic living. The culture medium comprises potato (70-85 wt.%), potassium (5-12 wt.%), dihydrogen phosphate (1-2 wt.%), magnesium sulfate (0.5-1 wt.%), agar (5-12 wt.%) and peptone (3-6 wt.%).
NOVELTY - The facility has evaporation gas collector (200) for collecting non-condensing evaporation gas generated in heat degradation room (130) of pyrolyzer. The jet drier (300) utilizes non-condensing evaporation gas collected by evaporation gas collector as fuel, for spraying processing water separated from effluent or precipitate/segregation. The solid material dryer (400) dries the sludge collected from jet drier or the sludge separated from precipitate/segregation. The wall (131) is made of silicon carbide material.    USE - Wastewater treatment facility.    ADVANTAGE - The energy source of the jet drier and solid material dryer can be improved at low cost. The solid waste, effluent including the solid content of food, and combustible waste can be processed effectively, thus protecting the environment from pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the wastewater treatment facility. (Drawing includes non-English language text)    Heat degradation room (130)    Silicon carbide wall (131)    Evaporation gas collector (200)    Jet drier (300)    Solid material dryer (400)
NOVELTY - Acid soil continuous cropping organic fertilizer for peanut using Peking Euphorbia root powder, comprises: livestock and poultry excrement stack of organic fertilizer (990 parts), Beijing large Morinda officinalis medicinal material powder (1 part), and plant endophytic fungus (9 parts).    USE - Used as acid soil continuous cropping organic fertilizer for peanut.    ADVANTAGE - The acid soil continuous cropping organic fertilizer provides a higher yield (200-500 kg/acre i.e. more than 15%) at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the acid soil continuous cropping organic fertilizer, comprising: providing livestock excrement, and aerobic fermentation composting organic fertilizer; crushing Beijing large Morinda officinalis medicinal material powder into the obtained mixture; and then using the fermentation plant endophytic fungi to obtain endophytic fungus solid fermentation products containing livestock excrement composting organic fertilizer.
NOVELTY - Method for the industrial waste biofiltration sludge management involves fermetation
NOVELTY - Method for manufacturing pour point depressant, involves (a) producing propanediol by fermenting glycerol using microbial strains, (b) producing 2-methyl-2-propen-1-ol from the propanediol by dehydration reaction, (c) producing ester by reacting the above-mentioned 2-methyl-2-propen-1-ol with carboxylic acid by esterification reaction, and (d) mixing the obtained ester and alkylbenzene preferably 5-12C alkylbenzene to obtain product, where the glycerol is a by-product produced during biofuel production.    USE - The method is useful for manufacturing pour point depressant.    ADVANTAGE - The method enables manufacturing pour point depressant having significantly reduced pour point. The method enables effective utilization of glycerol by-product produced during biofuel production, hence processing cost of glycerol is reduced and manufacturing cost of the biofuel is also reduced.    DETAILED DESCRIPTION - Method for manufacturing pour point depressant, involves (a) producing propanediol by fermenting glycerol using microbial strains, (b) producing 2-methyl-2-propen-1-ol from the propanediol by dehydration reaction, (c) producing ester of formula: CH2=C(CH3)-COOR by reacting the above-mentioned 2-methyl-2-propen-1-ol with carboxylic acid of formula: R'COOH by esterification reaction, and (d) mixing the obtained ester CH2=C(CH3)-COOR and alkylbenzene preferably 5-12C alkylbenzene to obtain product, where the glycerol is a by-product produced during biofuel production.    R'=5-12C alkyl, oxyalkyl or cyanoalkyl.    N.B: R is not defined in the claims or disclosure.
NOVELTY - Composition obtained by the creation of a low molecular weight hydrocarbon fluid exhibiting mainly oligomerized pentenes mainly comprised of 2-methyl-2-butene subunits and related plant isoprenoids composed of 2-methyl-1-butene subunits and other hydrocarbons from Euphorbia tirucalli biomass prepared by extraction and refinement in making the same composition through the creation of solvent permeable batting mat and a multi-phase solvent extraction, is claimed.    USE - The composition is useful as producing Phytoleum composition (claimed).    ADVANTAGE - The composition is simple, and can be obtained with high yield.
NOVELTY - Method for microbial degradation of nitrobenzene in industrial sewage, involves (a) culturing e.g. Pseudomonas, Stenotrophomonas maltophilia, Acinetobacter baumannii and Bacillus in bacterial growth medium to form microbial aggregates, (b) acclimating the obtained microbial aggregates using bacterial growth medium containing nitrobenzene, (c) expanding the acclimated microbial aggregates, and (d) feeding the bacterial culture into intermittently aired sequencing batch reactor (SBR) containing to-be-treated industrial sewage.    USE - The method is useful for degrading nitrobenzene in industrial sewage using microorganisms.    ADVANTAGE - The microorganisms have strong bioactivity and long survival time, exhibit resistance to impact loads in inlet water quality and completely treats wastewater.    DETAILED DESCRIPTION - Method for microbial degradation of nitrobenzene in industrial sewage, involves (a) culturing Pseudomonas, Stenotrophomonas maltophilia, Acinetobacter baumannii, Aquaspirillum, Acidovorax avenae, Alcaligenes faecalis, and Bacillus in a bacterial growth medium to form microbial aggregates, (b) acclimating the obtained microbial aggregates using bacterial growth medium containing 100 mg/L of nitrobenzene, (c) expanding the acclimated microbial aggregates, and (d) feeding the bacterial culture into intermittently aired sequencing batch reactor (SBR) containing to-be-treated industrial sewage (0.1%).
NOVELTY - Organic fertilizer comprises breaking turf, chinaberry seeds, deacetylated chitin with low molecular weight and fermented organic fertilizer into powder using 80-120 meshes and then mixing uniformly to obtain a mixture, controlling the moisture below 10% and the temperature of 18-32 degrees C, adding Bacillus subtilis(0.5-1 kg/ton) into the mixture and then mixing, and standing the mixture for 3-5 days to obtain the finished product, where the weight ratio of the turf to the chinaberry seeds, the deacetylated chitin and the fermented organic fertilizer is 40:5-2:53.    USE - The organic fertilizer is useful for controlling root-knot nematodes in soil (claimed). No biological data given.    ADVANTAGE - The organic fertilizer improves the soil quality in an economical manner.
NOVELTY - Biological bacterium fertilizer obtained by mixing sludge mud fitting with town sewage treatment factory sludge handling agricultural soil having water content of 75-80%, dehydrated sludge in urban sewage plant urban domestic sludge and conditioner, stirring, and performing a high temperature aerobic compost fermenting the compost product by screening and drying after the special microorganism strain, is claimed.    USE - Used as biological bacterium fertilizer. No biological data given.    ADVANTAGE - The process can provide rich organic nutrition for crops, improves the nutrition absorption and disease resistance of crops and solves the problem of sludge treatment of urban domestic sewage.
NOVELTY - Preparing organic fertilizer involves: weighing following raw materials (mass.%) poultry excrement (25-35), sludge (15-25), drug dregs (25-35) and straws (15-25), after classifying and air-drying the raw materials, separately crushing the raw materials, then mixing the materials uniformly, then fermenting materials by liquid compound strain, piling materials in wedge shape until the materials are 1-1.2 m high and 1.8-2.2 m wide; pelletizing completely fermented mixture; drying and sterilizing completely pelletized mixture, then packaging mixture.    USE - For preparation of organic fertilizer (claimed).    ADVANTAGE - The method treats sludge, and the organic matters contained in the sludge can satisfy the requirements of the fertilizer; fully uses the drug dregs, saves the resources, saves the cost, and takes the excrement as a fertilizer for solving the problem on pollution.    DETAILED DESCRIPTION - Preparation of organic fertilizer involves: weighing following raw materials (mass.%) poultry excrement (25-35), sludge (15-25), drug dregs (25-35) and straws (15-25), after classifying and air-drying the raw materials, separately crushing the raw materials, then mixing the materials uniformly according to weight ratio, then fermenting the materials by a liquid compound strain, piling the materials in a wedge shape until the materials are 1-1.2 m high and 1.8-2.2 m wide, where the fermenting temperature is 55-70 degrees C; pelletizing the completely fermented mixture; drying and sterilizing the completely pelletized mixture, then packaging the mixture for obtaining the product. The sludge contains 15-20% of organic matters in terms of the state of a dry base.
NOVELTY - Dry cow dung powder as an organic fertilizer, comprises (in wt.%) dry cow dung powder (78-90), organic matter (8-20), and an adhesive (1-3).    USE - The dry cow dung powder as an organic fertilizer is useful in chili planting, wheat planting, and corn planting (all claimed).    ADVANTAGE - The dry cow dung powder as an organic fertilizer: improves soil organic matter and soil fertility; reduces the amount of chemical fertilizers; improves soil structure; and exhibits a high stable quality and is economical.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing dry cow dung powder, comprising (i) collecting fresh cow dung and airing at an outdoor, dehydrating the air-dried cow dung using a dung dehydrator, drying the dehydrated dung in an oven and crushing the dung after drying, to obtain dry cow dung powder, (ii) mixing the dry cow dung powder obtained in the step (i) with organic matter according to mass ratio, to obtain organic fertilizer mixture, (ii) adding the adhesive according to mass percentage, to the mixture obtained in the step (ii), and (iii) uniformly mixing and granulating in an extrusion granulator or a disc granulator; and    (2) use of the dry cow dung powder as an organic fertilizer in: chili planting, where the dry cow dung powder is applied one time as a base fertilizer, deep plowing for 10-20 cm during applying the fertilizer in an amount of 50-100 kg/acre; wheat planting, where the dry cow dung powder is applied as the base fertilizer, in an amount of 80-100 kg/acre; and corn planting, comprising planting corn in a straight row, and applying the dry cow dung powder as the base fertilizer, in an amount of 100-150 kg/acre.
NOVELTY - The fertilizer comprises raw materials including 3 parts by weight (pbw) of urea, 34 pbw of monoammonium phosphate, 5 pbw of potassium sulfate, 53 pbw of danty and 5 pbw of bentonite. The fertilizer is prepared by taking the raw materials and then prilling via a disc, where a mass ratio of the nutrient fertilizer including nitrogen, phosphorus pentoxide and potassium oxide is 5-7:15-20:3-4. The addiction of the fertilizer has a total mass of 3-5 wt.%.    USE - The fertilizer is useful for alfalfa in saline-alkali soil and non saline-alkali soil with medium grade soil fertility (claimed). No biological data given.    ADVANTAGE - The fertilizer simply provides the alfalfa with high yield and quality in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing fertilizer.
NOVELTY - Removing moss-algae in field, comprises spraying liquid fertilizer with water into the field, where the prepared liquid fertilizer comprises copper sulfate (100-200 g), 35% algaecide (80-150 g), 50% trichloroisocyanuric acid (40-60 g), dry sand (3-7 kg) and water (1-1.5 kg).    USE - The method is useful for removing moss-algae in field.    ADVANTAGE - The method has simple removal process; uses copper sulfate, algaecide and trichloroisocyanuric acid as liquid fertilizer, which can eradicate moss-algae from the paddy fields; does not cause pollution to the environment, safe for aquaculture animals, and does not produce any toxic effects.
NOVELTY - The artificial grass comprises a strip-shaped main body. The main body is connected with a connecting rope, and comprises a main plate and a main film. The main film has a specific gravity of less than water and is made from hard, non-toxic and high molecular polymer. The main plate has a thickness of three quarters phase. A contact surface of the main plate and the film are tightly connected.    USE - The artificial grass is useful for sewage purification.    ADVANTAGE - The cost-effective artificial grass exhibits light weight and long service life, and prevents environmental pollution in river, fountain and pond thus improving water quality.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of an artificial grass.    Main plate (1)    Main film (2)    Connection rope. (3)
NOVELTY - Highly-selective absorbent molecular sieve-based composite material for microalgae biodiesel purification, prepared by loading metal cations capable of adsorbing fatty acids on HY-type molecular sieve by ion exchange technique, where purified biodiesel is obtained using the molecular sieve sieve-based composite material, and the ion exchange technique includes performing ion exchange in a nitrate solution with 20-40% weight percentage of metal ions and HY-type molecular sieve at 90-98 degrees C under refluxing conditions for 2-6 hours and continuously for 2-4 times.    USE - The composite material is useful for microalgae biodiesel purification.    ADVANTAGE - The molecular sieve-based composite material has high-selectivity, does not introduce ionic impurities, can be regenerated and is obtained by simple and economical method.
NOVELTY - The machine for transforming manure particles, is claimed, where the particle size is determined according to different manure.    USE - The machine is useful for transforming manure particles.    ADVANTAGE - The machine is capable of easily, economically and rapidly transforming the manure particles with less consumption of energy in an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for transforming manure particles.
NOVELTY - Producing a microbial organic fertilizer comprises: (i) inoculating Phanerochaete chrysosporium broth with rapeseed culture until maturity, where the amount comprises (in parts by weight): P. chrysosporium broth (2-3), and rapeseed (10-15), maintaining the moisture content at 40-50%, incubating the mixture at 35-39 degrees C under aerobic conditions for 2-7 days; and (ii) adding wettable powders comprising (in parts by weight): bentonite (0.5-0.75) and Bacillus thuringiensis (0.005-0.015), to the culture obtained in step (1), uniformly mixing, boiling and drying.    USE - The method is useful for producing microbial organic fertilizer.    ADVANTAGE - The fertilizer: is produced in a simple and easy manner, has a soil amelioration effect, regulates the availability of nutrient supply of the soil by adjusting the soil ecological micro-environments with improved utilization rate, and has prolonged effect on the soil.    DETAILED DESCRIPTION - Producing a microbial organic fertilizer comprises: (i) inoculating Phanerochaete chrysosporium broth with rapeseed culture until maturity, where the amount comprises (in parts by weight): P. chrysosporium broth (2-3), and rapeseed (10-15), maintaining the moisture content of the mixture at 40-50%, incubating the mixture at 35-39 degrees C under aerobic conditions for 2-7 days; and (ii) adding wettable powders of bentonite (0.5-0.75 parts by weight) and Bacillus thuringiensis (0.005-0.015 parts by weight) to the rapeseed culture with P. chrysosporium obtained in step (1), uniformly mixing, boiling and drying.
NOVELTY - Natural complex nutrient solution, comprises 1.5-2.5 parts by weight (pbw) of fermentation liquor of asplenium antiquum nidus base, 2.5-3.5 pbw of fruit peel, 1.5-2 pbw of potato powder, and 0.1-0.25 pbw of amino acid, where the nutrient solution is obtained by mixing fermentation liquor of asplenium antiquum nidus base with fruit peel and fermenting for 2-4 days, adding potato meal and fermenting for 1-3 days, and adding amino acid and then filtering for 2 days.    USE - The natural complex nutrient solution is useful for tropical epiphytic flowers for improving the stress resistance and stimulating the growth metabolism of grown plant. No biological data given.    ADVANTAGE - The natural complex nutrient solution easily favors the growth of the root, rapidly accelerates the growth of plantlet and prolongs the flowering phase, and can be economically prepared in an environmental friendly manner.    DETAILED DESCRIPTION - Natural complex nutrient solution, comprises 1.5-2.5 parts by weight (pbw) of fermentation liquor of asplenium antiquum nidus base, 2.5-3.5 pbw of fruit peel, 1.5-2 pbw of potato powder, and 0.1-0.25 pbw of amino acid, where: the nutrient solution is obtained by mixing fermentation liquor of asplenium antiquum nidus base with fruit peel and fermenting for 2-4 days, adding potato meal and fermenting for 1-3 days, adding amino acid and then filtering for 2 days; and the fermentation liquor of Asplenium antiquum nidus base is obtained by leaching 500-1000 g of trophoplasm composed of nodule aerial root of Asplenium antiquum nidus base and humus with sterile water to obtain 2-3 L of leacheate, adding 200-40 g of potato meal and culturing for 1-3 days, then transferring the product to a stirrer bed having rate of 120 revolutions per minute (rpm) and temperature of 25-27 degrees C, vibrating and culturing for 14-16 days, discharging the fermented mixture and then filtering to obtain a filtrate.
NOVELTY - A green vegetable organic fertilizer comprises (pts.wt.) mushroom residue (350-450), corncob (75-150), bagasse (75-150), seed cake (150-250), cottonseed hull (150-250), and microbial inoculum (10-20).    USE - Green vegetable organic fertilizer.    ADVANTAGE - The fertilizer has high nutrition, and can increase cabbage yield by 20-40% while providing vegetables having compact leaves.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the organic fertilizer, comprising:    (A) crushing mushroom residue into small particles and drying to water content of 20%, then drying bagasse to water content of 20%, pulverizing and sieving through 10-20-mesh sieve, crushing corncob into 10-20 mesh, crushing cottonseed hull into 10-mesh powder, and crushing seed cake into 20 mesh;    (B) uniformly mixing the materials, adding water into mixed material, adjusting pH to 7.4, and fermenting for 20 days; and    (C) drying until water content is less than 20 wt.% to obtain powder product.
NOVELTY - The method comprises: (A) grinding a oil cake of flax seed, rapeseed cake, oil-tea-cake, and tung oil cake under the size of 2 mm, grind the corncob under the size of 10 mm, and grind the biogas residue under the size of 20 mm; (B) mixing the grinded organic wastes, rice bran, enzymatic microorganism, and microelement fertilizer; (C) cooling the well-fermented material; and (D) drying the material until the moisture content (less than 30%), at last the finished product can be measured and packaged.    USE - The method is useful for preparing organic fertilizer or bio-organic fertilizer by using agricultural organic wastes. Tests details are described but no results given.    ADVANTAGE - The method provides highly-efficient and high-quality bio-organic fertilizer in an economical and environmentally friendly manner, improves the quality and safety of agricultural products, and improves soil quality and protect environment.    DETAILED DESCRIPTION - The method comprises: (A) grinding a oil cake of flax seed, rapeseed cake, oil-tea-cake, and tung oil cake under the size of 2 mm, grind the corncob under the size of 10 mm, and grind the biogas residue under the size of 20 mm; (B) mixing the grinded organic wastes, rice bran, enzymatic microorganism, and microelement fertilizer according to a mass ratio for 5-10 minutes, adding water to keep the moisture content 55-65%, then stacking the mixed material in strips with width (2-3 m) and height (1.2-1.5 m), processing the hypoxia fermentation for 2 days, and then turning the step at 55-75 degrees C for at least 5 days; (C) cooling the well-fermented material on the ground for 1-2 days, then stacking the material in heaps with height (3-6 m), turning the step again after 10-15 days and pilling continuously for 10-15 days; and (D) drying the material until the moisture content (less than 30%), at last the finished product can be measured and packaged.
NOVELTY - Improving stability of bio-oil using an additive, comprises adding acetone into bio-oil.    USE - The method is useful for improving the stability of bio-oil using an additive.    ADVANTAGE - The method is economical with simple process, does not require expensive equipment or stringent conditions, efficiently improves the oil stability, and reduces the bio-oil viscosity. The bio-oil obtained from the method can be stored for more than 35 days at 40 degrees C.
NOVELTY - Device comprises digester containing chambers and bioblock, where the methane gas is produced by supplying organic materials in order to inside of digester of chamber 12 from chamber 1 including bioblock in which bacteria inhabits, and digestive environment among chambers and bacteria are not mixed in precipitate discharge process by preparing unit which independently discharges precipitate formed in digesting process at lower of the chambers.    USE - The device is useful for discharging deposit in multi-stage anaerobic digester.
NOVELTY - Producing ultra pure ammonia comprises: (i) introducing the raw material ammonia into a rectifying tower controlled at 60 degrees C under the pressure 1.3-1.5 Pa and removing light components and part of the impurities including water; (ii) passing through an oil and water removing device controlled at 50-55 degrees C under the pressure 1.2-1.3 Pa to obtain ammonia with purity 99.9995%; (iii) passing through the terminal purifying device controlled at 40-50 degrees C under the pressure 1-1.2 Pa and removing water and impurities, condensing and storing in a ammonia tank.    USE - The method is useful for producing ultra pure ammonia.    ADVANTAGE - The method: is simple; reduces energy consumption by more than 40%; and the purity of the product is more than 99.99999%.    DETAILED DESCRIPTION - Producing ultra pure ammonia comprises: (i) introducing the raw materials of ammonia into a rectifying tower controlled at 60 degrees C under the pressure 1.3-1.5 Pa and removing light components and part of the impurities including water, where the purity of ammonia is greater than or equal to 99.995%, the water content is less than or equal to 100 parts per million, and the total amount of light components is less than 100 parts per billion during cold recycling; (ii) passing through an oil and water removing device controlled at 50-55 degrees C under the pressure 1.2-1.3 Pa to obtain ammonia with purity 99.9995%, and ensuring that the water content is 100 parts per billion before passing through a terminal purifying device; (iii) passing through the terminal purifying device controlled at 40-50 degrees C under the pressure 1-1.2 Pa and removing water and impurities, condensing and storing in an ammonia tank.
NOVELTY - Artificial wetland spherical ceramsite matrix comprises kaolin and sludge in a mass ratio of 0.60-0.70:1.    USE - The matrix is useful for treating domestic sewage, industrial and agricultural waste water and polluted surface water.    ADVANTAGE - The matrix is highly efficient in removing chemical oxygen demand, and nitrogen, total phosphorus and other pollutants in the sewage without matrix blockage, and the treated sewage is comparable with sewage discharge standards grade A of urban sewage treatment plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the ceramsite matrix, comprising: (a) removing impurities and granules from the final coagulated sludge in a water treatment plant, preparing the coagulated sludge into a paste, and drying the sludge at 105 degrees C; (b) uniformly mixing 0.60-0.70 kg of kaolin per kg of the treated dry sludge, regulating the moisture content of the sludge to 60-65%, and preparing the sludge into spherical ceramsite with the granule sizes of 15-18mm and 25-28mm; and (c) preheating the ceramsite at 200 degrees C for an hour, and sintering at 600-700 degrees C for 120-150 minutes.
NOVELTY - An absorption-promoting organic fertilizer comprises (pts.wt.) organic fertilizer (40-50), urea (30-40), humic acid (10-15), wheat bran (20-30), straw ash (15-25), calcium carbonate (3-8), trace element fertilizer (0.3-0.5), and potash fertilizer (2-5).    USE - Absorption-promoting organic fertilizer used for improving crop lodging resistance, disease resistance and drought resistance.    ADVANTAGE - The fertilizer can enhance crop absorption rate and reduce damage to the soil, and has simple preparation method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising:    (A) adding organic fertilizer, urea, straw ash and wheat bran into a stirrer so as to fully mix;    (B) adding humic acid, calcium carbonate, trace element fertilizer and potash fertilizer into the stirrer, uniformly mixing, adjusting water content of mixture to 45-50%, and pH value to 5.5-6.5;    (C) performing primary fermentation to the mixture for 4-5 days at 45-55 degrees C; and    (D) carrying out secondary fermentation for 8-10 days at 55-65 degrees C to obtain the fertilizer.
NOVELTY - Preparation of diammonium hydrogen phosphate slow release fertilizer, involves: preparing bio-carbon through hydrothermal method; absorbing diammonium phosphate using bio-carbon; and forming calcium alginate film on the bio-carbon to obtain the diammonium hydrogen phosphate slow release fertilizer.    USE - For preparing diammonium hydrogen phosphate slow release fertilizer (claimed) for agricultural field.    ADVANTAGE - The method is simple, meets environment friendly requirement, and is suitable for industrial production.
NOVELTY - The fertilizer comprises 580-620 parts by weight (pbw) of peanut oil residue degradation product, 380-420 pbw of peanut straw, and 2.5-3.5 parts of microorganism bacterium agent. The peanut oil residue degradation product is prepared by taking Bacillus subtilis and Yarrowia lipolytica as strain, and preparing the Bacillus subtilis fermentation liquid (40-70 pbw) and the Yarrowia lipolytica fermentation liquid (50-70 pbw) and then adding into 250-600 pbw of peanut oil residue.    USE - The fertilizer is useful for organic peanut. No biological data given.    ADVANTAGE - The fertilizer effectively increases the peanut yield, and improves the peanut quality.    DETAILED DESCRIPTION - The fertilizer comprises 580-620 parts by weight (pbw) of peanut oil residue degradation product, 380-420 pbw of peanut straw, and 2.5-3.5 parts of microorganism bacterium agent. The peanut oil residue degradation product is prepared by taking Bacillus subtilis and Yarrowia lipolytica as strain, respectively preparing the Bacillus subtilis fermentation liquid (40-70 pbw) and the Yarrowia lipolytica fermentation liquid (50-70 pbw) and then adding into 250-600 pbw of peanut oil residue, regulating the solution with a moisture content of 45-55 wt% and a pH value of 6.5-7.0, fully mixing and then controlling the solution at a temperature of 35-40 degrees C for 6-8 hours, and heating the solution at 100 degrees C for 25-35 minutes. An INDEPENDENT CLAIM is included for a method of preparing fertilizer.
NOVELTY - Safe processing of marigold ferment crushed waste solution, comprises (i) using bio-bacteria based on 0.1-0.3% of water-absorbent material, diluting bio-bacteria using water or waste solution, (ii) mixing diluted bio-bacteria and waste solution, adding into water-absorbent material until the moisture content is 40-70%, and (iii) stacking mixture in step (ii) and fermenting at 45-70 degrees C, turning the mixture stack, and then the fermenting the mixture at 45-70 degrees C, turning and then repeating fermentation until the moisture content is less than 20%, and milling to obtain the organic fertilizer.    USE - The method is useful for safe processing of marigold ferment crushed waste solution.    ADVANTAGE - The method solves the high chemical oxygen demand and biological oxygen demand of waste liquid discharge pollution problems; has simple preparation process; produces product, which is used as fertilizer; is easy to operate; and is suitable for industrialized production.
NOVELTY - An organic fertilizer or biological organic fertilizer comprises (wt.% dry basis) straw (10-20), rice bran (25-30), rapeseed meal (25-35), sugar plant filter mud (5-20), bagasse ash (5-10), and bacterial enzyme (0.1).    USE - Organic fertilizer or biological organic fertilizer used for rice (claimed), rape and sugarcane.    ADVANTAGE - The fertilizer is safe, green and capable of enabling rice, rape and sugarcane to return absorbed nutrient component to land to gradually recover soil fertility, can reduce use of agricultural fertilizer, and has reduced production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer or biological organic fertilizer, comprising:    (A) crushing straw into 5-10 cm, crushing rice bran, rapeseed meal and bagasse ash to below 5 mm, and crushing sugar plant filter mud to below 10 mm;    (B) mixing crushed materials and enzyme for 5-10 minutes, adjusting water content to 55-65%, stacking at height of 0.5-1.5 m, then performing anoxic fermentation for 2 days, turning each pile one time, and controlling temperature to 55-75 degrees C and fermenting for more than 5 days;    (C) putting fermented material on the ground, piling to 3-6 m high and cooling for 1-2 days, and continuously to stacking for 10-15 days; and    (D) controlling water content of pile to less than 30%.
NOVELTY - An integrated aerobic fermentation device comprises a fertilizer fermenting chamber provided with a hollow spiral transmission rod on an axis inside. One end of the spiral transmission rod is opened, and the other end is closed. Air outlets are arranged on the spiral transmission rod. Hollow blades are provided with air outlets side by side and are reversely installed on the spiral transmission rod. A refuse leachate collecting pipe is installed on bottom of the fermenting chamber and connected to a wastewater disposing device. A deodorizing pipe is on top of the fermenting chamber.    USE - Integrated aerobic fermentation device used for processing solid waste in rural areas (claimed).    DETAILED DESCRIPTION - An integrated aerobic fermentation device comprises a fertilizer fermenting chamber provided with a hollow spiral transmission rod on an axis inside. One end of the spiral transmission rod is opened, and the other end is closed. Air outlets are arranged on the spiral transmission rod. Hollow blades are provided with air outlets side by side and are reversely installed on the spiral transmission rod. The hollow blades correspond to the air outlets on the spiral transmission rod. A refuse leachate collecting pipe is installed on bottom of the fertilizer fermenting chamber and connected to a wastewater disposing device. A deodorizing pipe is installed on top of the fertilizer fermenting chamber and connected to a condensing tower via a draught fan. The condensing tower is connected to a biofilter via an odor gas pipe. The biofilter is connected to the opened end of the spiral transmission rod via an aerator. The condensing tower is connected with the wastewater disposing device via a distilled water pipe. An effluent pipe of the wastewater disposing device is connected to the fertilizer fermenting chamber.
NOVELTY - Organic composite soil comprises (pts.vol.) aged Agaricus bisporus leftover (3), current Agaricus bisporus leftover (3), needle mushroom leftover (3), and additives comprising carbonized bran or plant ash (0.4), pearlite (0.2), and vermiculite (0.4). The composite soil is further added with 0.1-0.5 wt.% of composite fertilizer, synergist, and dwarfing agent. The organic materials in the raw material are piled, fermented and decomposed for 30-60 days, and the materials are uniformly mixed with other materials to form the organic composite soil.    USE - Organic composite soil used for rice (claimed) to accelerate seedling growth.    DETAILED DESCRIPTION - Organic composite soil comprises (pts.vol.) aged Agaricus bisporus leftover (3), current Agaricus bisporus leftover (3), needle mushroom leftover (3), and additives comprising carbonized bran or plant ash (0.4), pearlite (0.2), and vermiculite (0.4). The composite soil is further added with 0.1-0.5 wt.% of composite fertilizer, synergist, and dwarfing agent. The aged Agaricus bisporus leftover is leftover after naturally stacking for more than 1 year. The organic materials in the raw material are piled, fermented and decomposed for 30-60 days by using high-temperature decomposing agent or effective microorganism (EM) preparation, and after drying and breaking, the materials are uniformly mixed with other materials to form the organic composite soil. The organic composite soil has water content not greater than 50%, organic matter content not less than 40%, total moisture content of 2.2-2.8%, pH value of 5.5-7, electrical conductivity (EC) not greater than 3, and granularity not greater than 5 mm, where there are 55-60% of 2-4 mm of granularity.
NOVELTY - A granular biological organic fertilizer comprises (pts.wt.) nutritional organic material (400-650), microbial agent (5-10), inorganic fertilizer (0-200), kaolin (0-250), and peat (0-200). The nutritional organic material comprises yeast fermentation broth waste liquid and rice bran at weight ratio of 0.8-1.2:1.2-0.8. The microbial agent comprises Bacillus laterosporus powder, zeolite powder and bentonite at weight ratio of 1:0.3-0.7:0.7-0.3.    USE - Granular biological organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the granular biological organic fertilizer, comprising: (A) preparing nutritional organic material by mixing yeast fermentation broth waste liquid and rice bran, keeping temperature of the mixture at 60-65 degrees C, stacking and fermenting for 10-15 days; (B) preparing microbial agent by uniformly mixing Bacillus laterosporus powder, zeolite powder and bentonite; and (C) uniformly mixing nutritional organic material, microbial agent, inorganic fertilizer, kaolin and peat, pelletizing the obtained mixed material, drying at 100-150 degrees C, and then screening to obtain finished product.
NOVELTY - A polyunsaturated fatty acid is prepared by performing transesterification reaction on microbial oils fermented and extracted by oleaginous microorganisms, and obtaining fatty acid methyl ester or fatty acid ethyl ester; adding extracting agent to fatty acid methyl ester or fatty acid ethyl ester, uniformly and fully mixing and reducing, filtering and separating solid and liquid phases; reducing temperature of liquid phase, heating, filtering and separating solid and liquid phases; rotatably evaporating liquid phase, and recovering solvent.    USE - Method for preparation of polyunsaturated fatty acid (claimed).    ADVANTAGE - The method has low cost, high yield of polyunsaturated fatty acid, simple reaction apparatus and easy large-scale application.    DETAILED DESCRIPTION - Polyunsaturated fatty acid is prepared by:    (A) performing transesterification reaction on microbial oils fermented and extracted by oleaginous microorganisms, and obtaining fatty acid methyl ester or fatty acid ethyl ester;    (B) adding 1-8 times extracting agent to fatty acid methyl ester or fatty acid ethyl ester, uniformly and fully mixing and reducing at - 15-(- 45) degrees C, heating for 8-12 hours, filtering and separating solid and liquid phases;    (C) reducing temperature of liquid phase at - 50-(- 90) degrees C, heating for 5-10 hours, filtering and separating solid and liquid phases; rotatably evaporating liquid phase, and recovering solvent to obtain polyunsaturated fatty acid; and    (D) combining filtered solid phase, and obtaining microbial diesel.
NOVELTY - Use of biodiesel is claimed for producing drilling fluid.    USE - The biodiesel is useful for producing drilling fluid (claimed), which is used for replacing crude oil and diesel oil, and for developing biodiesel drilling fluid system.    ADVANTAGE - The biodiesel drilling fluid has good lubricating effect, temperature resistance and low sulfur content, and reduced discharge of sulfur dioxide and sulfide, is free of aromatic alkane, hence it does not cause pollution and damage to environment, and easily biodegradable, and thus environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) drilling fluid comprising (in g): organic soil (3-10), organic lignite coal (1-15) and asphalt (3-10)/100 ml of biodiesel; and    (2) method of producing drilling fluid, involves adding organic soil, organic lignite coal and asphalt in the biodiesel and stirring evenly.
NOVELTY - Method for isolating heparin from cattle, involves using cattle liver as raw material, crushing the raw material, placing the raw material in an extract kettle, adding solvent, extracting using supercritical carbon dioxide, collecting the extract, adding ethyl acetate to the extract, stirring the extract, concentrating the filtrate, subjecting the concentrated filtrate to high speed counter-current chromatograph, collecting the decompressed and concentrated product and freeze-drying the product.    USE - The method is useful for isolating heparin from cattle (claimed).    ADVANTAGE - The method is rapid and environmentally-friendly, and consumes less energy.    DETAILED DESCRIPTION - Method for isolating heparin from cattle, involves using cattle liver as raw material, crushing the raw material to 20-60 meshes, placing the raw material in an extract kettle, adding extraction solvent, extracting the mixture using supercritical carbon dioxide, collecting the extract, adding ethyl acetate to the extract, stirring the extract, filtering the extract, concentrating the filtrate, subjecting the concentrate to high speed counter-current chromatograph, using normal hexane-ethyl acetate-methanol-water solvent system, where the upper phase is immobile phase and the lower phase is mobile phase, collecting the decompressed and concentrated product and freeze-drying the product to obtain bovine heparin.
NOVELTY - Method for extracting asimilobine, involves crushing Annona reticulata leaves, ammonifying crushed leaves, extracting the leaves using supercritical carbon dioxide, adding activated carbon, filtering the decolored extract, concentrating the extract, dissolving extract in acidic water, filtering the extract, diluting filtrate using alkaline alcohol solution, concentrating the extract, crystallizing the extract, dissolving the crystal using acetone, filtering the solution, cooling the solution to crystallize, filtering out the crystal and drying the crystal.    USE - The method is useful for extracting asimilobine in crystal form (claimed).    ADVANTAGE - The method is simple, environmentally-friendly and suitable for large-scale production.    DETAILED DESCRIPTION - Method for extracting asimilobine, involves (a) crushing Annona reticulata leaves into 20-40 meshes, ammonifying the crushed leaves for 2-6 hours, adding the ammonified leaves into extraction kettle, extracting the leaves for 2-4 hours using supercritical carbon dioxide and using methanol as entrainer and analyzing the obtained extract, (b) adding activated carbon (0.8-1 vol.%) for decolorizing the extract, filtering and concentrating the decolored extract, (c) dissolving the extract in acidic water, filtering the extract using cation exchange resin, washing the filtrate using deionized water till the filtrate becomes neutral, diluting the filtrate using alkaline alcohol solution, reducing pressure, concentrating the filtrate, regulating pH to 10-11, crystallizing the filtrate and filtering out the crystal, and (d) refluxing and dissolving the crystal using acetone, filtering the solution when it is hot, cooling the solution to crystallize, filtering out the crystal and drying the crystal.
NOVELTY - A magic fish organic soil comprises vinegar residue and cassava residue which are fermented and composted, carbonized bran or plant ash, and peat. Volume ratio of fermented vinegar residue to fermented cassava residue to carbonized bran or plant ash to peat is 2-4:4-6:0.5-1:1-2. The organic soil has water content of less than or equal to 30%, total porosity of 65-95%, organic content of greater than or equal to 20%, total nutrient content of 1-3%, specific gravity of 0.2-0.8 g/cm3, electrical conductivity value of 1-3 mS/cm, pH of 5.8-7.5, and particle size of 0.1-3 mm, where more than 60% of particles have size less than 1 mm.    USE - Magic fish organic soil.    ADVANTAGE - The organic soil is light in weight, full in nutrients and moderate in water content, and can keep the activity of the roe.
NOVELTY - Pad material with strain of organism, which is isolated from joint application by non-reactive breeding method comprising padding and sterilizing a strain adding the pad material and strain and padding to produce fermentation bed, and providing and sterilizing Chinese green planting trees to replace the isolation belt between adjacent barn, is claimed.    USE - The material is useful as food additive and in sewage treatment.    ADVANTAGE - The material improves the feeding environment, increases the breeding income, and reduces the feeding cost and the breeding risk and provides a strong guarantee of obtaining a high quality non-reactive product.    DETAILED DESCRIPTION - Pad material with strain of organism, which is isolated from joint application by non-reactive breeding method comprising padding and sterilizing a strain adding the pad material and strain and padding to produce fermentation bed, where the mass ratio of the pad material and the strain is 1000:1, the pad material is 50-100 billion weight of viable bacteria per strain, the padding with strain comprises 4-5 parts of EM bacteria (generally comprises Bacillus, saccharomycetes, actinomycetes, Azotobacter, cellulose-decomposing bacteria and lactic acid bacteria), 2-3 parts of potassium and 3-4 parts of photosynthetic bacterium preparation; and providing and sterilizing Chinese green planting trees (honeysuckle) to replace the isolation belt between adjacent barn, is claimed.
NOVELTY - A leaching method of plum fruit leach liquor involves pressing the pulp of ripe plum fruit into uniform slurry, adding organic solvent to leach the leach liquor, heating the leach liquor at less than 100 degrees C, centrifuging, taking out the supernatant to obtain the plum fruit leach liquor.    USE - As leaching method of plum fruit leach liquor; for preparing bacteriostatic agent, where the bacteriostatic agent is used in fungistasis (claimed). Also for preventing some fungal diseases, and other crops.    ADVANTAGE - The leaching method involves use of high efficiency extraction method of dipping of bacteriostatic active ingredient in tissue culture so that the culture medium reduces pollution probability; improves seedling survival rate; is capable of realizing green pollution-free production; and does not produce danger in agriculture planting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bacteriostatic agent is prepared by the leaching method.
NOVELTY - Marsh gas purifying tower comprises a regular hexagonal prism-shaped tower body. The tower body can also be designed into the shape of a cylinder, a prism and/or a pyramid. The tower is divided into a main purifying tower, a secondary purifying tower and a sedimentation tank.    USE - Used as a marsh gas purifying tower.    ADVANTAGE - The marsh gas purifying tower completely removes impurities of biogas, prevents utilization of corroding objects to filter the biogas; meets the standard requirements for complete purification of biogas; and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the marsh gas purifying tower.
NOVELTY - A multihole honeycomb spongy biological bed comprises spongy cuboid or cube (1a); limber holes (1) arranged in honeycomb shape, where section of each limber hole is polygon or round; and a mass of small holes set in the spongy cuboid or cube without limber holes, where porosity is 3-200 PPI. Within the holes is sludge (3) which is used for culturing bacteria and containing the biological bacteria group. Distance of two adjacent polygons or rounds is 2-200 mm. Aperture of each limber hole or opposite side spacing of the polygon is 5-100 mm. Longest side of each cuboid or cube is 100-2200 mm.    USE - A multihole honeycomb spongy biological bed used in sewage system.    ADVANTAGE - The spongy material and the multihole honeycomb structure are most suitable to the adhesion and growth of the sludge, and after the sewage treatment, the ratio surface is not reduced dramatically. The regular hexagon multihole honeycomb structure provides the biggest ratio surface for contacting the bacteria with the sewage, the highest use ratio, and high sewage movability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for assembly method of the biological bed used in the sewage system, comprising stacking cuboids or cubes to be a big cuboid or cube, connecting the limber holes of the upper and lower cuboid or cube head-on so that the sewage can flow smoothly; and connecting 3/4 of the big cuboids or cubes to be the biological bed bunch by rebar, rope or pipe, lifting and fixing in cesspit. As the big cuboid or cube of the biological bed is assembled, the water flowing direction is the same to or turning 90 degrees of the installation direction of the drain holes of the adjacent big cuboid or cube.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the multihole honeycomb spongy biological bed.    Limber holes (1)    Cuboid or cube (1a)    Sludge (3)
NOVELTY - Heavy metal ion in sewage is adsorbed using waste yeast by washing waste yeast with deionized water for 2-3 times, centrifuging, collecting thallus, drying at 80 degrees C, and grinding into fine powder; treating waste yeast fine powder with sodium hydroxide (NaOH), hydrochloric acid (HCl) or absolute ethyl alcohol, washing with deionized water, and drying; adding waste yeast powder in domestic sewage to prepare waste yeast solution, and adsorbing via oscillation; and filtering, and measuring absorbance of heavy metal ion in the filtrate.    USE - Method of adsorbing heavy metal ion in sewage using waste yeast (claimed).    ADVANTAGE - The method has low cost and simple operation, does not need complex equipment, and can enhance adsorption rate of heavy metal ions in sewage.    DETAILED DESCRIPTION - Adsorption of heavy metal ion in sewage using waste yeast comprises:    (A) washing waste yeast with deionized water for 2-3 times, centrifuging for 10 minutes at 3500 revolutions/minute (rpm), then collecting thallus, drying at 80 degrees C, cooling and grinding into fine powder, and drying;    (B) treating the waste yeast fine powder with NaOH, HCl or absolute ethyl alcohol, then washing with deionized water for 3-5 times, drying at 80 degrees C, grinding and sieving through 80-mesh screen;    (C) adding the waste yeast powder in domestic sewage to prepare a waste yeast solution (0.5-5 g/L), adsorbing via oscillation for 15-90 minutes at pH value of 2-7 at 30 degrees C and rotary speed of 120 rpm; and    (D) filtering, measuring absorbance of heavy metal ion comprising hexavalent chromium ion (Cr6+), copper ion (Cu2+), and lead ion (Pb2+) in the filtrate, and calculating adsorption rate.
NOVELTY - Device comprises a induced draft fan (2), a material receiving tank (3), a water inlet (4), a water outlet (5), a water sprinkler (6), an exhaust port, a liquid returning outlet, an inlet, a recovery tower and a circulating pump. The recovery tower is externally provided with the induced draft fan, the water inlet, the water outlet, and the circulating pump. The tower wall is provided with the inlet, the exhaust port, the liquid returning outlet and a drain port. The recovery tower is internally provided with a water spraying support, the water sprinkler and the material receiving tank.    USE - The device is useful for recycling dry powder of the amino acid e.g. lysine.    ADVANTAGE - The device is simple and ecofriendly, saves water (up to 80%) and energy, consumes less electricity, avoids the risk of explosion and blockage of recovered bag caused by stopping maintenance and replacing bags; and is suitable for tryptophan, phenylalanine and other amino acids.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the device.    Induced draft fan (2)    Material receiving tank (3)    Water inlet (4)    Water outlet (5)    Water sprinkler (6)
NOVELTY - Scenedesmus microalgae mutant strain (I), is new, which is obtained by an UV mutagenesis of wild Scenedesmus microalgae 0301A, having quicker growth speed.    USE - (I) is useful for: producing fish and shrimp bait and/or feed for livestock; fixing carbon dioxide and/or preparing biodiesel; and producing astaxanthin and treating sewage (all claimed).    ADVANTAGE - (I) improves higher oil and/or astaxanthin yield in an economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: a method for producing biodiesel and astaxanthin, and for treating sewage comprising cultivating (I).
NOVELTY - Method for preparing biological hydrogen production system, involves filtering, depositing and cleaning sludge from sewage treatment plants, aerating and culturing the product in reactor, adding basic conditioning agent to reactor for controlling pH of the solution, adding oxidation-reduction potential agent to the product to control the oxidation-reduction of the solution, and reacting the obtained product.    USE - The method is useful for preparing biological hydrogen production system (claimed).    ADVANTAGE - The method is rapid and has excellent stability.    DETAILED DESCRIPTION - Method for preparing biological hydrogen production system, involves (a) filtering, depositing and cleaning sludge from sewage treatment plants, adding the product into reactor, and aerating and culturing the product at room temperature for 10 days, (b) adding water in sugar solution, and adding agricultural nitrogen phosphorus compound fertilizer to obtain mixed solution, and (c) adding the mixed solution into the reactor, adding basic conditioning agent to reactor for controlling pH of the solution to 4-4.3, adding oxidation-reduction potential agent to the product to control the oxidation-reduction of the solution to -240 mV to -280 mV, processing the product at 34-36 degrees C for 6 hour and reacting the obtained product.
NOVELTY - Cleaning technique for extracting and purifying tabersonine in Voacango africana stapf seeds comprises: (i) drying V. africana stapf seeds, crushing, filling in an extracting reactor and extracting through supercritical carbon dioxide extraction to obtain yellow oily liquid with tabersonine; (ii) washing the oily liquid, combining acid water liquid, adding alkali and extracting by low polarity organic solvent; and (iii) directly loading the extract liquid on a chromatography column, eluting, collecting eluent and vacuum recycling the solvent to obtain tabersonine.    USE - The method is useful for extracting and purifying tabersonine in V. africana stapf seeds.    ADVANTAGE - The method: is eco-friendly, simple, economical and safe, increases the sample yield by 2%, has high controllability and short production period, and produces tabersonine having high purity of more than 98%.    DETAILED DESCRIPTION - Cleaning technique for extracting and purifying tabersonine in Voacango africana stapf seeds, comprises (i) drying V. africana stapf seeds, crushing into 20-40 sieve meshes, filling in an extracting reactor and extracting through supercritical carbon dioxide extraction to obtain yellow oily liquid with tabersonine; (ii) washing the oily liquid through dilute hydrochloric acid, combining acid water liquid, adding an alkali and extracting by low polarity organic solvent; and (iii) directly loading the extract liquid obtained in step (ii) on a chromatography column, eluting by a mixed solvent, collecting eluent and vacuum recycling the solvent to obtain tabersonine.
NOVELTY - Straw branch compression shaping fuel (sic) comprises an upper surface (1) set on an upper cover board stacked compression straw or branches, a bottom plate (4) arranged on the lower surface of a vertical column, and the of the straw or branches is provided with a binding belt.    USE - Used as a straw branch compression shaping fuel (sic).    ADVANTAGE - The device occupies less area, comprises branches per unit volume thus the user does not need to continuously add any fuel, is equivalent to coal fuel, is easy to ignite thus shortens ignition time, reduces the cost of boiler heat supply, can be used as a fuel in urban household heating furnace, and also as heat supply heating boiler with fuel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the straw branch compression shaping fuel (sic).    Upper surface (1)    Stacked compressed straw or branches (2)    Binding belt (3)    Bottom plate (4)
NOVELTY - Device for preparing ammonia based on transition flue gas of power plant gas turbine outlet, comprises a compressed air storage tank and an urea solution tank. Transition flue gas and double-phase flow atomizing nozzles are arranged along the circumferential direction of the transition flue uniformly. The double-phase flow atomizing nozzles are close to the inlet of the transition flue gas. The rear parts of the double-phase flow atomizing nozzle are provided with static mixers. The compressed air tank and urea solution storage tank are connected with the double-phase flow atomizing nozzles.    USE - The device is useful for preparing ammonia based on transition flue gas of power plant gas turbine outlet.    ADVANTAGE - The device is simple, utilizes high temperature pyrolysis urea to produce ammonia, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for preparing ammonia based on transition flue gas of power plant gas turbine outlet.
NOVELTY - A 3-methoxy-4,5-methylenedioxy phenylethylamine or its derivative is prepared by mixing beta -nitrostyrolene derivative (I), acid material and solvent; and subjecting mixture to catalytic hydrogenation in the presence of palladium/carbon catalyst.    USE - Method of preparing 3-methoxy-4,5-methylenedioxy phenylethylamine or its derivative.    ADVANTAGE - The method is low cost and environment-friendly, has high yield, and prepares product having high purity.    DETAILED DESCRIPTION - A 3-methoxy-4,5-methylenedioxy phenylethylamine or its derivative of formula (I) is prepared by mixing beta -nitrostyrolene derivative of formula (I), acidic material and solvent; and subjecting mixture to catalytic hydrogenation in the presence of palladium/carbon catalyst.    R1-R3=alkoxy or methylenedioxy.
NOVELTY - Preparing butyric acid mixed culturing organisms comprises: filtering, depositing elutriating the sludge, adding cane sugar residue, agricultural compound fertilizer and cysteine, ionizing radiating to the active sludge, domestication culturing for 10 days under the room temperature, and then placing in the reactor, adding water and agricultural compound fertilizer into the cane sugar solution and placing the obtained mixed solution in the reactor, controlling the temperature at 34-36 degrees C, where the water power stopping time of the mixed solution is 5-6 hours.    USE - The process is useful for preparing butyric acid mixed culturing organisms for producing hydrogen system (claimed).    ADVANTAGE - The process is simple and capable of rapidly producing hydrogen.    DETAILED DESCRIPTION - Preparing butyric acid mixed culturing organisms comprises: filtering, depositing elutriating the sludge, adding cane sugar residue, agricultural compound fertilizer and cysteine, ionizing radiating to the active sludge, domestication culturing for 10 days under the room temperature, and then placing in the reactor, adding water and agricultural compound fertilizer into the cane sugar solution and placing the obtained mixed solution in the reactor, controlling the temperature at 34-36 degrees C, where the water power stopping time of the mixed solution is 5-6 hours, and the process uses physical and chemical composite processing (cysteine-ionizing radiation) to preprocess the active sludge, which can effectively remove the oxygen in the water, and restrain the growth of aerobic bacteria, and maintain the anaerobic environment of the system.
NOVELTY - Preparing 2,2,2-trifluoro-N-(R)-indan-1-yl-N-prop-2-ynyl-acetamide (III) comprises (a) performing alkylation reaction between 2,2,2-trifluoro-N-(R)-indan-1-yl-acetamide (II) and 3-chloro-propyne or 3-bromo-propyne.    USE - (III) is useful as intermediate for preparing (IV) and (V) (all claimed). (IV) is useful for treating Parkinson's disease. No biological data given.    ADVANTAGE - The process is simple, cost effective and eco-friendly for preparing (III) with high yielding ratio and purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing (R)-indan-1-yl-prop-2-ynyl-amine (IV) comprising the step (a) as above per se and (b) hydrolyzing (III); and    (2) preparing rasagiline mesylate (V) comprising the steps (a) and (b) and performing salifying reaction of (IV) and the methanesulfonic acid.
NOVELTY - DL-pantolactone is synthesized by performing aldol condensation to glyoxylic acid which is neutralized by organic amine with isobutyraldehyde, synchronously contacting a condensation product with hydrogen on a copper(II) oxide/silicon oxide (CuO/SiO2) catalyst in a continuous fixed bed reactor to perform catalytic hydrogenation and dehydration cyclization to prepare DL-pantolactone, and decompressing and distilling to obtain high purity DL-pantolactone.    USE - Method of synthesizing DL-pantolactone (claimed).    ADVANTAGE - The method has simple operation, high yield and mild reaction condition, and is safe and environment-friendly.
NOVELTY - Preparing olive leaf extract involves: extracting dry olive leaf in polar solvent; recycling solvent from extraction liquid; adding water and auxiliary materials and filtering; performing purification by column chromatography of macroporous resin, absorbing filter liquid by the resin, and performing desorption by mixed solution of ethanol and water, and collecting desorption liquid; and recycling the solvent from the desorption liquid, performing vacuum concentration, and drying.    USE - For preparing olive leaf extract (claimed).    ADVANTAGE - The method is simple, provides olive leaf extract having high content of oleuropein at low cost; and is suitable for large-scale production.    DETAILED DESCRIPTION - A method of preparing an olive leaf extract involves: (1) putting the dry olive leaf in the polar solvent for extraction; (2) recycling the solvent from the extraction liquid, and adding water and auxiliary materials, performing water sedimentation, mixing uniformly, standing, pressing, filtering, and merging the filter liquid; (3) performing purification by column chromatography of macroporous resin, absorbing the filter liquid by the macroporous resin, performing desorption by the mixed solution of ethanol and water, and collecting desorption liquid; and (4) recycling the solvent from the desorption liquid, performing vacuum concentration, and drying to obtain the olive leaf extract.
NOVELTY - Synthesis of 4-methyl-5-formyl thiazole comprises reacting methyl acetoacetate with ethanol under protection of bromine gas (sic) to obtain 2-amino-4-methyl-thiazole-5-carboxylic acid methyl ester (I); reacting compound (I) with sodium dihydrogen phosphate, sodium nitrate and sulfuric acid to obtain 4-methyl-thiazole-5-carboxylic acid methyl ester (II) and reacting compound (II) with potassium borohydride, lithium chloride, sodium hypochlorite, and sodium bromide to obtain 4-methyl-5-formyl thiazole.    USE - Synthesis of 4-methyl-5-formyl thiazole used as cefditoren pivoxil intermediate.    ADVANTAGE - The method has simple operation, has no pollution, and provides high product yield.
NOVELTY - Extraction and preparation of camptothecin are performed by using alkaline solution to ultrasonic auxiliary extracting technology.    USE - Method for extraction and preparation of camptothecin (claimed).    ADVANTAGE - The method has low production cost and high yield, and is environment-friendly.
NOVELTY - Generating quercetin comprises adding hyperin standard product to 30-70% ethanol at a pH of 4-8 and heating the system to 40-70 degrees C; and adding naringinase to the system and performing reaction for 30 hours.    USE - The quercetin is useful for treating cardiovascular diseases. No biological data given.    ADVANTAGE - The process provides quercetin with high conversion efficiency and without pollution.
NOVELTY - The process comprises taking safflower seeds, adding anhydrous ethanol as extracting agent with solid to liquid ratio of 1:3 into safflower seed, extracting the mixture using extracting tank at 80 degrees C for 2.5-3.5 hours, filtering the extract, evaporating the filtrate, adding ethanol solution with concentration of 80% into filtrate, dissolving the mixture with normal hexane to extract, standing and separating the extract, adding methanol phase and then evaporating, adding ethyl acetate into mixture, dissolving the mixture with water, and standing and separating the mixture.    USE - The process is useful for extracting 5-hydroxytryptamine derivatives, which are useful for inhibiting tumor. No biological data given.    ADVANTAGE - The process is capable of easily and rapidly extracting the 5-hydroxytryptamine derivatives with high purity and improved extraction rate and without toxicity.    DETAILED DESCRIPTION - The process comprises taking safflower seeds, adding anhydrous ethanol as extracting agent with solid to liquid ratio of 1:3 into safflower seed, extracting the mixture using extracting tank at 80 degrees C for 2.5-3.5 hours, filtering the extract, evaporating the filtrate, adding ethanol solution with concentration of 80% into filtrate, dissolving the mixture with normal hexane to extract, standing and separating the extract, adding methanol phase and then evaporating, adding ethyl acetate into mixture, dissolving the mixture with water, standing and separating the mixture, extracting ethyl acetate phase, evaporating the extract to dry, and obtaining 5-hydroxytryptamine derivatives.
NOVELTY - Controlling and recycling distributed duck farming pollution comprises (a) reducing the emission of pollutant source, (b) breeding earthworm in the dry duck manure after composting, (c) performing marsh fermentation to the duck waste water and precipitating and discharging the manure wastewater into a reed field for purifying after precipitation; and (d) setting an area comprising aquatic plant and animals for digesting nitrogen and phosphorus in the duck manure at ecological interception area at the water surface area for duck activities.    USE - The method is useful for controlling and recycling distributed duck farming pollution.    ADVANTAGE - The method: reduces water pollution; improves manure resource utilization and optimizes the breeding environment; provides economic benefit; and is simple and economical.
NOVELTY - Extraction of pure pearl active substance involves preparing natural pearl nanopowder by pure physical method according to CN1943865A; soaking pearl nanopowder in deionized (DI) water, and forcibly and ultrasonically shaking; passing obtained product through ultrafiltration membrane to separate impermeable bioactive component and permeable ionic solution; dehydrating and concentrating the ionic solution, and filtering; and uniformly mixing bioactive component and concentrated solution, dehydrating, drying, and sterilizing.    USE - Method for extracting pure pearl active substance (claimed).    ADVANTAGE - The method is simple to operate, and has low equipment requirement, no pollution and low cost.    DETAILED DESCRIPTION - Extraction of pure pearl active substance involves preparing natural pearl nanopowder with size of less than 100 nm by pure physical method according to CN1943865A to ensure that pearl activity is not damaged; soaking pearl nanopowder in DI water at powder-to-water ratio of 1:50-500, and forcibly and ultrasonically shaking to achieve nanodegradation of pearl nanopowder according to CN1943802A; passing degradation product through ultrafiltration membrane to separate impermeable bioactive component and permeable ionic solution; dehydrating and concentrating separated ionic solution at less than 60 degrees C, and filtering to remove most of calcium ions (Ca2+) and carbonate ions (CO32-) which are deposited as calcium carbonate sediments to obtain dehydrated and concentrated solution; and uniformly mixing bioactive component and concentrated solution, dehydrating, drying, and sterilizing to obtain extract of pure pearl active substance. The pearl active substance comprises residual organic component, trace elements and small amount of calcium carbonate remaining after removal of calcium carbonate.
NOVELTY - Urea is purified by (A) taking urine passes through first, second and third grade crystallizer, and removing crystal of first and second level crystallizer temperature section, of crystallization temperature section; (B) desalinating water dissolved in hot crystal by continuous stirring; and (C) controlling temperature, cooling and crystallizing solution to obtain the product.    USE - Method for purifying urea (claimed).    ADVANTAGE - The method is simple and efficient. Operation is convenient and practical, safe and environment-friendly.
NOVELTY - A cyanuric chloride derivative (I) is new.    USE - Cyanuric chloride derivative (I) used as green chemical insecticide.    ADVANTAGE - The cyanuric chloride derivative has high selectivity and is safe.    DETAILED DESCRIPTION - A cyanuric chloride derivative of formula (I), is new. An INDEPENDENT CLAIM is included for a preparation of (I).
NOVELTY - Humic acid is extracted by sending percolation membrane bioreactor and nanofiltration membrane intercepted landfill leachate to nanofiltration system and ultrafiltration system.    USE - Method for extracting humic acid used in preparing fertilizer (claimed).    ADVANTAGE - The extraction method is economical, has simple flow and device, requires less area, and does not cause secondary pollution.
NOVELTY - A garden waste is processed by classifying the collected garden waste, grass, leaf, and needle the raw material to be used without grass and wood plant waste volatile fragrance; crushing and secondary fine crushing; crushing and mixing garden waste powder, cotton seed cake powder, corn flour, bran, grass carbon, and fertile soil at a ratio of 60-80:5- 8: 6-10: 2-20:4-8:20-40; adding water to 25-30% of the total weight; adjusting pH value to 7.5-8.5; sterilizing; adding Streptomyces; and fermenting at 26-32 degrees C for 5-8 days.    USE - Method for processing of garden waste used as garden waste fertilizers for the production of seed treatment (claimed).    ADVANTAGE - The main raw material is agriculture and forestry waste. The waste resource utilization reduces the cost for producing active carbon through solid product ferment seed treatment agent product, and generates the higher economic benefit.
NOVELTY - Preparation of antofine comprises immersing Cynanchum komarovii material fine powder into alkali alcohol for 2-6 hours, adding to extraction kettle, using supercritical carbon dioxide (CO2) extraction, dissolving extract using 3% hydrochloric acid aqueous solution, filtering solution, extracting filter liquid using chloroform, taking chloroform layer, recovering and drying chloroform to obtain crude product; and separating antofine from crude product using high-speed counter current chromatograph, collecting target component, concentrating and drying.    USE - Method of preparation of antofine (claimed).    ADVANTAGE - The method is simple, has low pollution, and is suitable for industrial production, and produces antofine with high in purity.    DETAILED DESCRIPTION - Preparation of antofine comprises immersing Cynanchum komarovii material fine powder into alkali alcohol for 2-6 hours, adding to extraction kettle, using supercritical CO2 extraction, dissolving extract using 3% hydrochloric acid aqueous solution, filtering solution, extracting filter liquid using chloroform, taking chloroform layer, recovering and drying chloroform to obtain crude product; and using ammonia solution of n-hexane-chloroform-methanol with pH of 8.5 as solvent system, separating antofine from crude product using high-speed counter current chromatograph, collecting target component, concentrating and drying target component to obtain high-content antofine.
NOVELTY - Microwave auxiliary extraction of swainsonine involves naturally drying Astragalus strictus, passing through 30-50 meshes sieve, adding petroleum ether in Astragalus strictus, ultrasonically degreasing Astragalus strictus with petroleum ether, recycling petroleum ether, using methyl alcohol as solvent, soaking, performing microwave extraction for 10-30 seconds at microwave output power of 120-460 W to obtain extraction liquid, with weight volume ratio of Astragalus strictus to methyl alcohol at 1:10-20 (g/ml).    USE - Method of microwave auxiliary extraction of swainsonine (claimed).    ADVANTAGE - The method has high extraction efficiency, less energy consumption, low cost and less pollution.
NOVELTY - Pre-processing biomass comprises removing impurity from biomass, cleaning, and crushing into powder; adding clean water, and naturally freezing; defrosting; stirring, grinding, adding enzyme or other hydrolysis to hydrolyze cellulose and hemicellulose, and filtering, where filtrate is used for ethanol fermentation, and filter residue is primary lignin.    USE - Method for pre-processing biomass used for producing cellulose, hemicellulose, and lignin products (claimed).    ADVANTAGE - The method has reduced cost, is environment-friendly, and improves biomass ethanol fermentation pre-processing.
NOVELTY - An catechin gallic acid ester (ECG) monomer is separated and purified by providing green tea raw material, adding 7 BV ethyl acetate after gamma -heating, recycling ethyl acetate, concentrating an extraction liquid, spraying, and drying to obtain a total catechin; and adding pure water to dissolve the total catechin product configured to material solution of 3% (w/v) concentration, separating and purifying by macroporous absorption resin column using desorbing solvent, e.g. ethanol.    USE - Method for the separation and purification of ECG monomer (claimed).    ADVANTAGE - The method is simple and low cost, has short production period, and meets requirements of environment protection and safety.    DETAILED DESCRIPTION - Separation of purification of ECG monomer comprises:    (A) providing green tea raw material, adding 7 BV ethyl acetate after gamma -heating, recycling ethyl acetate, concentrating an extraction liquid, spraying, and drying to obtain a total catechin;    (B) adding pure water to dissolve the total catechin product configured to material solution of 3% (w/v) concentration, separating and purifying by macroporous absorption resin column, using desorbing solvent, e.g. ethanol, collecting ethanol desorption fraction, concentrating and recycling ethanol, concentrating the desorbed fraction, centrifuging, spraying and drying to obtain dry product;    (C) adding pure water to dissolve the dry product on column liquid by 3% (w/v) concentration, separating and purifying by macroporous absorption resin column, collecting ethanol desorption, circulating, concentrating and recycling ethanol until alcohol degree is less than 5, using reverse osmosis membrane, and further concentrating centrifugal spray drying; and    (D) drying to obtain the product of 3 times (w/v) 95% ethanol, standing, crystallizing, filtering, freezing, and drying to obtain the crystal product of ECG monomer.
NOVELTY - The device has a main body whose upper part is provided with a stainless steel sealing cover that is fixed to a top part provided with a semi-spherical toughened glass shell. A flammable gas detection sensor and a poisonous gas sensor are fixedly arranged on an engineering vehicle body and connected with a control vehicle through a cable. The flammable gas detection sensor is provided with a methane gas sensor and a gas sensor. The poisonous gas sensor is provided with another gas sensor and a hydrogen chloride gas sensor.    USE - Gas detecting device for an anti-submarine warfare (ASW) sensor sewage pump station sludge cleaning engineering vehicle.    ADVANTAGE - The device allows real-time control of the vehicle, manipulates information according to gas distribution, and utilizes a lower pump station, which can provide information support so as to avoid blind under well damage.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a gas detecting device for an ASW sensor sewage pump station sludge cleaning engineering vehicle.
NOVELTY - n-Amyl formate ester is reacted with 5-fluorocytosin to obtain an amide derivative of 5-fluorocytosin. The amide derivative is reacted with 1,2,3-triacetyl-5-deoxy-D-ribose, to obtain a diacetyl cytosine nucleoside amide derivative. Basic hydrolysis of the product is carried out using sodium hydroxide, to obtain capecitabine.    USE - Preparation of capecitabine.    ADVANTAGE - The method enables convenient control of materials, is economical, and enables recovery of manganese to prevent environmental pollution.
NOVELTY - A butane separating and purifying method involves separating normal butane, isobutene and propane, and adsorbing high purity normal butane with an absorption phase, where the adsorbed high purity normal butane is heated, separated using molecular sieve and subjected to nitrogen purging and normal desorption to obtain pure butane having purity of 99.5-99.8 %.    USE - Method for separating and purifying butane.    ADVANTAGE - The method enables separating and purifying butane in a simple, rapid, convenient and reliable manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for separating and purifying butane. '(Drawing includes non-English language text)'
NOVELTY - The equipment has excretion storage (100) with water level sensor (110) for confirming level of livestock excretions. A kneading section (200) is provided to agitate the livestock excretions. An oxygen ozone supply unit (300) is provided for supplying oxygen and ozone to the livestock excretions. A liquefied fertilizer exhausting unit (400) is provided to eject livestock excretions agitated and supplied with oxygen and ozone to outside of the equipment. A guide duct (500) has oxidizer (510) for igniting gas is installed at upper portion of the excretion storage.    USE - Liquefied fertilizer production equipment for removing odor from livestock excretion, used in stockbreeding farmhouse.    ADVANTAGE - The manufacturing cost of the equipment is reduced and odor can be effectively removed from the livestock excretion. The purification of the excrements can be performed in short period.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the liquefied fertilizer production equipment for removing odor from livestock excretion. (Drawing includes non-English language text)    Excretion storage (100)    Water level sensor (110)    Kneading section (200)    Oxygen ozone supply unit (300)    Liquefied fertilizer exhausting unit (400)    Guide duct (500)    Oxidizer (510)
NOVELTY - Method of producing synthetic gasoline, involves (a) reacting methane (59%) with carbon monoxide (41%) in presence of catalyst, and (b) circulating the methane with carbon monoxide at constant temperature of 300-350 degrees C and constant pressure of 450-500 psi. The catalyst comprises 2/3 of pulverized sodium salt, and 1/3 of pulverized ferric oxide.    USE - The method is useful for producing synthetic gasoline, synthetic diesels and carbon monoxide and hydrogen gas (all claimed).    ADVANTAGE - The method enables cost-effective production of clean gasoline and diesels as cost of natural gas is very low.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of producing synthetic diesels, involves performing the above-cited steps (a) and (b); and    (2) method of producing carbon monoxide and hydrogen gas, involves subjecting the 50% methane and 50% oxygen gas to partial combustion, and circulating the mixture in a vacuum chamber.
NOVELTY - The system has plasma gas separator (20) that generates hydrogen and oxygen from water. A fuel mixer (30) mixes the generated hydrogen and oxygen with fertile fuel and external air. A gasholder (35) that is installed between plasma gas separator and fuel mixer stores hydrogen and oxygen gas. An engine (40) generates power by using the fertile fuel supplied from fuel mixer. A gas generating agent apparatus controls quantity of water supplied to plasma gas separator and controls generation rate of hydrogen and oxygen gas at the plasma gas separator.    USE - Engine system for vehicle.    ADVANTAGE - The performance of the engine can be improved. The combustion quality of the fuel can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the engine system. (Drawing includes non-English language text)    Water tank (10)    Plasma gas separator (20)    Fuel mixer (30)    Gasholder (35)    Engine (40)
NOVELTY - The gas reactor comprises a drying zone (6), carbonization zone (7) and pyrolysis zone (8) for preparing biomass feedstock for gasification. The biomass feedstock for gasification enters the counter-current gasification zone (15) and a co-current gasification zone (17) after passing through drying zone (6), carbonization zone (7) and pyrolysis zone (8) of the gas reactor. The gas reactor is constructed to operate in a combined mode or in a selected mode of counter-current gasification and co-current gasification. A breaker shaft assembly (16) with shaft arrangements (30) and paddle breakers (31) are placed in between the counter-current gasification zone (15) and co-current gasification zone (17). Rotating grates (22) and screw conveyer assembly (12) are placed below the co-current gasification zone (17) to discharge the ash produced in the gas reactor. The thermo-chemical gas reactor works under diverse conditions with regards to feed, shape, size, moisture levels, bulk density and operated on all types of biomass to convert them to a tar free gas by removing ash and particulate in the proficient manner. Image 0/10
NOVELTY - A preprocessor of herbal biomass is obtained by spin-drying herbal biomass, hydrating and further spin-drying using pressing water-removal device (10). The preprocessor preprocesses herbal biomass before utilizing herbal biomass as fuel, gasification raw material and carbide raw material.    USE - Preprocessor is used for preprocessing herbal biomass derived from coconut oil empty fruit bunch and king grass used as fuel, gasification raw material and carbide raw material.    ADVANTAGE - The preprocessor reduces the potassium content in the herbal biomass by preventing trouble in operation of combustion furnace and fouling smell generated from exhaust heat-recovery boiler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preprocessing method of herbal biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of preprocessor. (Drawing includes non-English language text)    Steam heating apparatus (1)    Shell-release apparatus (2)    Pressing water-removal device (10)    Pressing spin-drying portion (11,13)    Hydration portion (12)
NOVELTY - The method comprises dispensing biomass into thin sheets of ground biomass, subjecting the thin sheets to ramps of temperature, selectively collecting various groups of compounds as they are released from the thin sheets, chopping biomass, where a first biomass is produced, loading the first biomass into an input hopper (49) via one of biomass reaction compartments, dehydrating and pulverizing the first biomass, heating the first biomass further to release low boiling point bio-compounds and pyrolysis fragments, and scraping residual carbon and a biochar.    USE - The method is useful for fractioning biomass into a crude oil.    ADVANTAGE - The method is capable of effectively fractioning the biomass into the crude oil with high throughput and yield and enhanced purity.    DETAILED DESCRIPTION - The method comprises dispensing biomass into thin sheets of ground biomass, subjecting the thin sheets to ramps of temperature, selectively collecting various groups of compounds as they are released from the thin sheets, chopping biomass, where a first biomass is produced, loading the first biomass into an input hopper (49) via one of biomass reaction compartments, dehydrating and pulverizing the first biomass, heating the first biomass further to release low boiling point bio-compounds and pyrolysis fragments, and scraping residual carbon and a biochar from one of the of biomass reaction compartments into an exit hopper (63), where a next biomass reaction compartment is loaded with a second biomass while the first biomass is dehydrated. The ramps of temperature are incremented over a range of times, pressures, or local working gas compositions.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a biomass fractionator system.    Input hopper (49)    Transfer plate mechanism (50)    Disc (53)    Gas venting system (61)    Exit hopper. (63)
NOVELTY - System comprises: a biomass load and dump station for receiving ground biomass into the system; a heated pulverizing processing station for compressing ground biomass; a biochar dumping station for collecting residual carbon and biochar; and a many biomass reaction compartments, where the biomass reaction compartments carry ground biomass from station to station.    USE - The system is useful: for biomass fractioning (claimed); for producing bio-intermediate compounds along with syngas, biochar and biothels; and for producing long chain dehydrated sugars, lignin derived aromatics, lipid based oils, carbohydrate based furans, shorter hydrocarbons, oxygenates comprising butane, butanol, acetone, acetaldehyde, aldehyde, methane, methanol and syngas components comprising hydrogen, carbon monoxide, and carbon dioxide.    ADVANTAGE - The system: provides improved fractionator yield by way substantial changes in temperature, and local gas composition at various processing stations; maximize production of high purity carbon; facilitates multiple fractionating stations within a pressure vessel which operates below atmospheric pressure, in open air, and at elevated pressures.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of load and dump station for ground biomass.    Disc (1)    Hopper (9)    Control bar (12, 12A)    Airlock (15)    Pressure bulkhead (16)
NOVELTY - The system of biomass reaction compartments for carrying ground biomass from a station to a station in a biomass fractionator, comprises a disc (1) having chambers and smooth or coated top surface configured to accommodate seals between stations.    USE - The system is useful in biomass reaction compartments for carrying ground biomass from a station to a station in a biomass fractionator.    ADVANTAGE - The cost-effective system of biomass reaction compartments simply carries the ground biomass from the station to the station in the biomass fractionator thus ensuring high throughput for the biomass fractionator.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of biomass reaction compartments.    Disc (1)    Oval configuration (4)    Oval track (5, 6, 7)    Interconnection hinges. (8)
NOVELTY - Renewable heating oil composition derived from the thermochemical conversion of a cellulosic biomass, comprises hydrocarbons having an oxygenated component present in an amount so that the renewable heating oil composition has an oxygen content of less than 30 wt.%, and a non-oxygenated component having an aromatic content of greater than 40 wt.%.    USE - The renewable heating oil composition is useful as a fuel for a furnace, boiler or stove (claimed).    ADVANTAGE - The renewable heating oil composition has a improved stability parameter of less than 30 (preferably less than 1) cp/hour, less corrosiveness and higher heating value of greater than 10000 btu/lb.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the renewable heating oil composition derived from the thermochemical conversion of a cellulosic biomass, comprising (a) converting at least a portion of the cellulosic biomass material in an oxygen-poor environment in the presence of a catalyst material at 200-1000 degrees C to produce a reaction product stream containing the renewable heating oil composition, and (b) separating the renewable heating oil composition from the reaction product stream so that the heating oil composition has a heating value of greater than 10000 btu/lb, without an oxygen-removing hydrotreatment step
NOVELTY - Production of fatty acid alkyl esters from a fatty acid feedstock containing free fatty acids, comprises: providing a reaction mixture that comprises the fatty acid feedstock, a lower alcohol, and a lipolytic enzyme; and allowing the reaction mixture to react under formation of fatty acids alkyl esters, where a gas flow is passed through the reaction mixture and then passed through a volume of lower alcohol, before recirculating it through the reaction mixture.    USE - The process is useful to produce biodiesel using microbial enzymes.    ADVANTAGE - The process produces high yield of lower alkyl esters of fatty acids with lower alcohol consumption and less number of sources and without any additional products in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production system for processing the reaction mixture, comprising one or more enclosed reaction vessels, where each reaction vessels (1) comprise at least one first gas inlet (2) and first gas outlet (3), one or more gas wash tanks (5) comprising a gas wash liquid (4), where each gas wash tank contains at least one second gas inlet and outlet, and comprising one or more gas pumps capable of delivering a gas flow by the first gas inlet through the reaction vessels, discharged by the first gas outlet and the second gas inlet through the gas wash liquid, and discharged by the second gas outlet, before recirculating to the gas inlet into the reaction vessels.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of production system for processing a reaction mixture.    Reaction vessel (1)    First gas inlet (2)    First gas outlet (3)    Second gas inlet (4)    Gas wash liquid (5)    Gas wash tank. (6)
NOVELTY - The method comprises providing an internal combustion engine with a liquid fuel such as ethanol fuel consisting of alcohol fuel and diesel. The liquid fuel has a flash point temperature of higher than 25 degrees F, and nano-sized zinc oxide particles (0.01-100 ppm) to lower the flash point temperature compared to a same liquid fuel without the nano-sized zinc oxide particles. The nano-sized zinc oxide particles (90 wt.%) have a size of 5-10 nm. The nano-sized zinc oxide particles have a surface area of 150-600 m2/g, and a spherical shape.    USE - The method is useful for improving cold starts of an internal combustion engine including an Otto-cycle engine, a diesel engine, a rotary engine and a gas turbine engine.    ADVANTAGE - The method efficiently improves the cold starts of the internal combustion engine by reducing or minimizing retarding friction and viscosity effect between pistons of the engine and cylinder walls.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for increasing an engine speed by 10% and an exhaust gas temperature of an internal combustion engine; and    (2) a method for lowering a flash point temperature of a liquid fuel consisting of alcohol fuel and diesel.
NOVELTY - The modifier has a raw fuel supply pipe (35) that contains an upper extending unit (35e) which is extended upwards rather than the modifier main portion (4). A U-shaped unit (35c) blocks the back flow of water from the modifier main portion and water vapor in upper extending unit.    USE - Modifier installed in storage container of solid oxide type fuel cell system.    ADVANTAGE - The back flow of the water vapor from raw fuel supply pipe can be prevented. The efficiency, operability and reliability of the modifier can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the fuel cell system. (Drawing includes non-English language text)    Modifier main portion (4)    Drain pipe (16)    Raw fuel supply pipe (35)    U-shaped unit (35c)    Upper extending unit (35e)
NOVELTY - The device has a receiving vessel (2) for accommodating biomass (M). An outlet of receiving vessel is connected to a transport device (7). A heating reservoir (20) is provided for heating a reaction mixture fed in receiving vessel to cracking temperature (T). A downstream mixer pump (24) is connected to outlet side (23) of heating reservoir. A return line (34) is extended from a lower portion of the intermediate container (31) to upper portion heating reservoir. The intermediate container is connected with a final stage container (72) through a feed line (82).    USE - Device for performing thermal treatment of biomass using biological residue substance such as wood chip, leave, rapeseed cake, sugar residues, beer or liquor, solids from the oil-extraction, meat and bone meal, cellulose from paper production, cake from feed production for animals, straw of wheat, barley or other grains.    ADVANTAGE - The thermal treatment of biomass can be performed easily in simple manner at low cost, without any loss of liquid component.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the device for performing thermal treatment of biomass.    Receiving vessel (2)    Transport device (7)    Heating reservoir (20)    Outlet side (23)    Downstream mixer pump (24)    Intermediate container (31)    Return line (34)    Final stage container (72)    Feed line (82)    Biomass (M)    Cracking temperature (T)
NOVELTY - A plate portion unit is installed in interior of plate portion. Another plate portion is spaced apart from inner surface of main hole and inner spacing portion is installed with plate portion. Front and rear covers (50,60) are installed in front and rear sides of tube portion and plate unit is fixed with certain space from inner side of main hole. A water supply hole (70) is formed in front cover for supplying water to electrolyte space formed between plate portion units. A gas discharge hole (80) is formed in front cover for discharging mixture of hydrogen and oxygen.    USE - Apparatus for producing mixture of hydrogen and oxygen.    ADVANTAGE - Since the hydrogen and oxygen produced in bubble shapes from the electrodes can be easily separated, the effective area of the electrodes in which electrolysis occurs is increased and electrolyte efficiency can be enhanced. The electrolysis of water can be more actively performed by changing the physical properties of the surface of the plate portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of production apparatus.    Cooling unit (20)    Front cover (50)    Insulation bracket (55)    Rear cover (60)    Water supply hole (70)    Gas discharge hole (80)
NOVELTY - The cell has a single, high mass, generally rod-shaped cathode (100) and a single, low mass, generally helical anode (101) that are arranged about a common axis. The surface area of the cathode and anode are equal. A conducting unit conducts heat that is generated at the cathode away from the cell. The heat conducting unit has a non-insulated, heat conducting disc in contact with the end of the cathode, to conduct heat away from the cathode via a heat conducting insulated conduit to larger, insulated, heat conducting disc which is in contact with a heat sink.    USE - Hydroxy generator cell for internal combustion engine of vehicle (claimed).    ADVANTAGE - The heat energy is conducted away from the cell instead of raising the temperature of the electrolyte. The stability of the cell is improved and thus, the efficiency, reliability and longevity can be enhanced. The thermal stability of hydroxy gas production in a supplemental hydrogen fuel cell is improved and hence, the working life of the cell can be extended by reducing degradation of the cathode during operation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing hydrogen and oxygen gases for supplementing fuel intake of internal combustion engine; and    (2) method for improving fuel economy and/or reducing emission of pollutants of engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of dual mass helix array fitted in a cell.    Cathode (100)    Anode (101)    Screw fitting (102)    Support fitting (103)    Screw cap (206)
NOVELTY - A composite type two phase anaerobic digestion reaction device comprises acid phase anaerobic traverse baffle reactor; and methane flow fixed bed anaerobic reactor. The upper flow fixed bed anaerobic reactor is provided with reaction chamber fixed carrier of a flow anaerobic sludge blanket.    USE - A composite type two phase anaerobic digestion reaction device.    ADVANTAGE - The reaction device allows acid producing phase and methane to be separated, which effectively prevents acid to be blocked. It improves yield and efficiency, and processing efficiency and operation stability of the system. It is convenient to control and prolongs the average residence time of the sludge to achieve efficient organics and target improving methane yield.
NOVELTY - A combined group overlapped biomass generation electric chemical extracting joint device comprises sealed furnace body (1), where furnace is provided with combustion unit. Combustion unit comprises combustion chamber (2), where lower part of combustion chamber is provided with feeding cavity (3). Bottom of feeding cavity is provided with feeding rail (31). Feeding rail is provided with carbon box (34). Lower part of combustion chamber is equipped with clamped carbon box and preventing carbon box form opening upwards.    USE - Combined group overlapped biomass generation electric chemical extracting joint device.    ADVANTAGE - The device has continuous and automatic production process, has high production efficiency, controllable process, and good effect. It has good separating effect and high coefficient of recovery. The raw materials are easily separated.    DETAILED DESCRIPTION - Combined group overlapped biomass generation electric chemical extracting joint device comprises sealed furnace body (1), where furnace is provided with combustion unit. Combustion unit comprises combustion chamber (2), where lower part of combustion chamber is provided with feeding cavity (3). Bottom of feeding cavity is provided with feeding rail (31). Feeding rail is provided with carbon box (34). Lower part of combustion chamber is equipped with clamped carbon box and preventing carbon box form opening upwards. Carbon tank is connected with feeding track equipped with lifting carbon box. One side of combustion unit is provided with gas collecting pipe. Gas collecting pipe is connected with carbon tank opposite to the interface of one side of air inlet hole. Combustion chamber is at least provided with three processing layer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating the combined group overlapped biomass generation electric chemical extracting joint device.
NOVELTY - A tar collecting device comprises pipe, tar collecting tank and smoke pipe. The device includes tar collecting pool and smoke box storing tar collecting pool of periphery wall of smoke box. The device is provided with clapboard. Clapboard at top and two sides are respectively connected with top and side wall of smoke box of bottom baffle plate. The clapboard separates smoke storage box into smoke chamber and inner chamber.    USE - Tar collecting device for biomass carbonizing furnace.    ADVANTAGE - The device has simple structure, convenient operation, and low cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a tar collecting device.
NOVELTY - A guide device comprises cylindrical shell body, where two ends of which are provided with cover. Center of shell vertical to surface of the side part is provided with inlet orifice. The center of shell vertical to surface of the lower side part is provided with outlet. Shell is provided with rotating shaft along axial direction. Two ends of rotating shaft are respectively arranged at central part of cover, where one end of rotating shaft is connected with driving device. Rotating shaft is provided with blades, and at least two blades to material inlet and material outlet partition.    USE - A guide device used for biomass carbonizing furnace.    ADVANTAGE - The device prevents outer air entering coking chamber from material inlet and material outlet of carbonization chamber, thus ensuring oxygen-free or oxygen-poor environment of carbonization chamber and effectively improving biomass raw material in effect and carbonization quality when carbonizing.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a guide device.
NOVELTY - A conical fixed bed biomass continuous pyrolysis device comprises combustion chamber (1), shell (2), L-shaped heat exchange pipe (4), bed tube plate (3), biomass storage bin (7), and material pipe (9). Combustion chamber is provided at lower part of pyrolysis device shell. Plenum is arranged on upper part of pyrolysis device shell on outer side of shell pyrolysis device. Top of combustion chamber is provided with conical-tube plate. L-shaped heat exchange pipe is connected with conical-tube plate.    USE - Conical fixed bed biomass continuous pyrolysis device.    ADVANTAGE - The device has uniform temperature increasing speed, high heat utilization rate and high thermal efficiency. The device has simple and reliable structure, and has long service life.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a conical fixed bed biomass continuous pyrolysis device.    Combustion chamber (1)    Shell (2)    Bed tube plate (3)    L-shaped heat exchange pipe (4)    Biomass storage bin (7)    Material pipe (9)
NOVELTY - Siloxane contained in biogas is absorbed in an absorber and removed. Hydrogen sulfide contained in biogas is reacted with metal oxide and removed as metal sulfide. Oxygen contained in biogas as impurity is reacted with copper-zinc oxide and removed as cupric oxide. Carbon dioxide contained in biogas is separated by pressure swing adsorption method and methane is concentrated and collected.    USE - Recovery of methane from biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recovery system of methane.
NOVELTY - Method for obtaining renewable energy, involves crushing fallen leaves and processing the crushed powder.    USE - The method is useful for obtaining renewable energy.    ADVANTAGE - The method utilizes waste material as raw material.
NOVELTY - Composition comprises creation of a low molecular weight hydrocarbon fluid exhibiting mainly oligomerized pentenes mainly comprised of 2-methyl-2-butene subunits as well as related plant isoprenoids composed of 2-methyl-1-butene subunits and other hydrocarbons from woody biomass prepared by the steps of a process for the extraction and refinement in making the same composition of matter through the creation of a solvent permeable particle and a multi-phase solvent extraction system.    USE - The composition is useful for producing wood phytolium (claimed) and as a petroleum substitute.    ADVANTAGE - The composition can be produced at high yield in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing wood phytolium, comprising extracting and refining in making the composition through the creation of a solvent permeable woody biomass particle and a multi-phase solvent extraction system.
NOVELTY - A cyclohexene adsorption agent consists of beta -type zeolite. The molar ratio of silicon dioxide and aluminum dioxide in the zeolite is 20-400.    USE - Cyclohexene adsorption agent for adsorbing cyclohexene (claimed) contained in fuel gas, town gas, liquefied petroleum gas, gasoline and kerosene, used for manufacturing hydrogen used as fuel for polymer electrolyte fuel cell and solid oxide type fuel cell.    ADVANTAGE - The adsorption agent has excellent adsorption characteristics with respect to cyclohexene.
NOVELTY - The plasma reactor (1) comprises several plasma generation electrodes (2) that are arranged for extending the direction of the exhaust gas flow, according to the generation of plasma reactions. A dielectric material (3) is arranged between plasma generation electrodes. The magnetic electrode (2g), permanent magnet and electromagnet are arranged for generating magnetic field in the direction that faces the airflow in the gas flow direction.    USE - Plasma reactor for processing exhaust gas containing discharged from diesel engine of motor vehicle, and factory, and industrial plant, etc.    ADVANTAGE - The particulate matter collection performance of the plasma reactor can be improved, due to exertion of force that moves the particulate tinged with the electric charge by the plasma along the direction facing airflow of exhaust gas. The size and weight reduction of the plasma reactor can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the plasma reactor.    Plasma reactor (1)    Plasma generation electrode (2)    Magnetic electrode (2g)    Dielectric material (3)    Particulate matter (PM)
NOVELTY - Producing bio-organic fertilizer with wheat flour comprises: (a) adding water into edible flour to prepare flour pulp, and obtaining wet gluten and starch milk; (b) adding molasses and strain into the gluten; (c) activating completely yeast in 30-40 minutes, activating completely amylase; (d) collecting and liquefying starch milk, obtaining liquefied liquid with sugar content of 15-16%, accessing the strain, fermenting and culturing to obtain fermenting liquid; and (e) spraying fermenting liquid on the raw material, granulating and drying to obtain flour refined bio-organic fertilizer.    USE - The method is useful for producing bio-organic fertilizer with wheat flour.    ADVANTAGE - The method: produces bio-organic fertilizer which is capable of improving the soil nutrient; increases the fertilizer utilization rate; environment friendly and protects the ecological environment.    DETAILED DESCRIPTION - Producing bio-organic fertilizer with wheat flour comprises: (a) adding water into edible flour to prepare flour pulp, and obtaining wet gluten and starch milk; (b) adding molasses and strain into the gluten, where the molasses is capable of providing enough oxygen and carbon source for enlarging the bacterial colony in the process of fermenting; (c) activating completely in 30-40 minutes via yeast in the environment at 30 degrees C after wheat powder yeast paste is formed, activating completely amylase in 80-90 minutes, where the activity of the yeast and the activity of the amylase are capable of retaining for 40 hours; (d) collecting and liquefying the obtained starch milk, obtaining liquefied liquid with sugar content of 15-16%, accessing the strain, fermenting and culturing to obtain fermenting liquid with large bacterial colony and good bacteria; and (e) spraying the fermenting liquid on the raw material prepared earlier, granulating and drying to obtain flour refined bio-organic fertilizer.
NOVELTY - Method for producing organic fertilizer using municipal sludge, involves mixing wet sludge having 40-60% water content with carrier, subjecting the mixture to stacking fermentation for 15-30 days, crushing the fermented mixture and packaging the crushed mixture.    USE - The method is useful for producing organic fertilizer using municipal sludge obtained after treatment of urban sewage.
NOVELTY - A pleuromutilin fermentation liquid used in the production plant nutrient, where the secondary fermentation liquid after removal of pleuromutilin, is mixed with nutritive element to form plant nutrient    USE - As pleuromutilin fermentation liquid used in production plant nutrient (claimed).    ADVANTAGE - The side pleuromutilin fermentation liquid rich in nutrition in the fermentation liquid contains a large amount of quick-acting nitrogenphosphorus-potassium, trace elements, of amino acid and polysaccharide, can be used as plant growth nutrient substances, improves promoting the growth and yield. The main raw material is cheap and the material is. At present, the side pleuromutilin fermentation liquid discharged as waste water, and the product is as the main raw material, large amount, the cost is low; provides high yield, simple operation. The side pleuromutilin degradation bacteria for degrading the pleuromytilin high production efficiency, in the ferment liquid of pleuromutilin content of liquid chromatograph cannot be detected level so as to make the product has no environmental risk of antibiotic. The product fertilizer effect, which not only provides a nitrogen, phosphorus and potassium elements, but also provides microelement, amino acid and polysaccharide material to make the nutrition more balanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing method of pleuromutilin fermentation liquid production plant nutritional agent, where the seeding side in the pleuromutilin fermentation liquid pleuromutilin degrading strain, after 1- 10 days, to obtain fermentation liquor for removing the side pleuromutilin, and then the ferment liquid with nutrient substance to obtain the liquid plant nutrient fluid, and then making the yeast liquid with nutrient substance, then adding absorbent material, then air-drying or drying to obtain the solid plant nutrient fertilizer.
NOVELTY - Organic fertilizer for crops comprises (in parts by wt): organic fertilizer raw material (30-40), ammonium sulfate (30-40), diammonium phosphate (5-15), humic acid (10-15), straw ash (15-25), bran (8-12), calcium powder (3-8), amino acids (3-5), trace element fertilizer (0.3-0.5), microbial agent (0.3-0.8), potassium fertilizer (2-5) and granulating agent (0.5-0.8).    USE - Used as an organic fertilizer for crops.    ADVANTAGE - The fertilizer: provides improved lodging resistance, disease resistance and drought resistance to the crops; ensures high absorption capacity, high yield, and simple preparation; and does not damage soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the organic fertilizer, comprising (i) weighing organic fertilizer raw material, bran, ammonium sulfate, diammonium phosphate and straw ash according to the weighed amount, adding into a mixer and uniformly mixing, (ii) adding humic acid, calcium powder, amino acid, trace element fertilizer, microbial agent and granulating agent to the mixture obtained from the step (i), uniformly mixing, adjusting water content of the mixture to 45-50%, and pH to 5-6.5, (iii) performing primary fermentation of the mixture obtained from the step (ii) for 4-6 days at 45-55 degrees C, and (iv) performing secondary fermentation of the mixture obtained from the step (iii) for 9-11 days at 55-65 degrees C.
NOVELTY - Microbial organic fertilizer comprises (in mass.%) mature rapeseed cake fertilizer (50-60), bentonite (25-35), Phanerochaete chrysosporium liquid (10-14) and Bacillus thuringiensis water dispersible powder (0.5-1).    USE - The organic fertilizer is useful in agricultural production e.g. tobacco leaf production (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the application of the microbial organic fertilizer in agricultural production, comprising using the organic fertilizer as a base fertilizer or whole fertilizer, applying, where the amount covering per acre is 15-30 kg, and the microbial organic fertilizer is not mixed with any chemical fertilizer.
NOVELTY - Removing organic waste by fish, vegetables and earthworm, comprises removing the organic waste by earthworms, precipitating and filtering by a dynamic biomembrane, and biologically producing the product and purifying the product, where the pollutant of the organic wastewater or the domestic organic waste is recycled by plants, animals and microorganisms in an aquatic animal such as fish, plate, such as vegetables, and earthworm circulating ecological system, no pollutant is discharged, no greenhouse gases is discharged, the pollution is eliminated.    USE - The method is useful for removing organic waste by fish, vegetables and earthworm.    ADVANTAGE - The method is capable of economically, removing organic waste with high energy consumption.    DETAILED DESCRIPTION - Removing organic waste by fish, vegetables and earthworm, comprises: removing the organic waste by earthworms, precipitating and filtering by a dynamic biomembrane, biologically producing the product and purifying the product, where the pollutant of the organic wastewater or the domestic organic waste is recycled by plants, animals and microorganisms in an aquatic animal such as fish, plate, such as vegetables, and earthworm circulating ecological system, no pollutant is discharged, no greenhouse gases is discharged, the pollution is eliminated, the harvested fish, shrimps, vegetables, melons and fruits and earthworms are green food or organic food, and are high-quality raw materials for dietary therapy.
NOVELTY - An alcohol-based fuel comprises (wt.%) methyl alcohol (70-98), water (0.1-28), glycerol (1.5-4.5), ammonia-ammonium chloride buffering solution (0.2-1), and hydroxyl ethylidene bisphosphonic acid (0.05-2). The alcohol-based fuel is divided into two layers during heating where the upper surface layer comprises paraffin oil and having a thickness of more than 0.5 (preferably 1.5) cm.    USE - An alcohol-based fuel.    ADVANTAGE - The fuel has high flash point, and has slow corrosion effect on applied device.
NOVELTY - Low-carbon methanol diesel fuel comprises (in parts weight): vegetable-oil (10-50), methanol (30-50), cetane number improver (5-15), desulfurization heavy benzene (10-28), n-butanol (5-12), diesel oil (1-5) and catalytic additive (0.3-0.8).    USE - The low-carbon methanol diesel fuel is used in motive power machines e.g. buses, trucks, excavators and generators and in boilers, furnaces and aluminum products and baking which requires high burning.    ADVANTAGE - The low-carbon methanol diesel fuel is less-corrosive, prevents loss of power and replaces existing 0# negative 10# diesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing low-carbon methanol diesel fuel, which involves adding the above mentioned components in pressure free container through metering pump, heating the mixture in electric static mixture at 20-30 degrees C , circulating the mixture for 1-3 hours and filtering the mixture.
NOVELTY - Method for cultivating Grifola frondosa, involves adding G.frondosa to bag containing culture medium, where water content of the medium is 61-62%, and gap between the culture medium and bag is minimum, inoculating the product into culture chamber, and culturing the product at 22-25 degrees C, under relative humidity of 60-70%, until the carbon dioxide concentration reaches 2000 parts/million (ppm).    USE - The method is useful for cultivating G.frondosa.    ADVANTAGE - The method environmentally-friendly provides high yield with excellent quality.
NOVELTY - High molecule-inorganic hybridized film is formed by doping polyoxyethylenepoly caprolactam block multipolymer with metal-organic complex formed of transition metal ion including oxidizing ferric ion and copper, where the mass fraction of the hybrid membrane block copolymer is 55-60 %mass and the mass fraction of the polycaprolactam segment block copolymer is 40-45 %mass.    USE - The high molecule-inorganic hybridized film is useful for gas separation, preferably carbon dioxide/methane separation (claimed).    ADVANTAGE - The hybrid film shows high selectivity with respect to carbon dioxide/methane, and standard selectivity can reach 70 or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing the high molecule-inorganic hybridized membrane, which involves (a) adding polyoxyethylene-poly hydantoinate block copolymer to 65-755 of ethanol solution at 75-80 degrees C, refluxing the solution for 0.5-4 hours, and cooling the solution to room temperature to obtain a polyoxyethylene-poly hydantoinate block copolymer solution (25 %mass), (b) adding polyoxyethylene-caprolactam solution block copolymer to the dopamine hydrochloride powder, obtaining ferric ion and copper ion with respect to dopamine hydrochloride at ratio of 1:(0.5-20), stirring the powder uniformly, and preparing film solution, (c) adding the prepared film liquid into the polyfluortetraethylene culture dish, drying the product at room temperature to obtain the polyoxyethylene-caprolactam block multipolymer, and (d) coating the solution on the film surface, drying the polysulfone ultrafiltration film surface at room temperature to obtain the surface layer.
NOVELTY - Sugar-derived compound (I-II) is new.    USE - Sugar-derived compound used for preparing composition, for use in pharmaceutical, cosmetic, and agrochemical domains, as well as security domain to combat bioterrorism and for use as cleaning material (all claimed).    ADVANTAGE - The sugar-derived compound ensures enhanced tensioactive property and antimicrobial activity against Bacillus species, particularly against Bacillus anthracis, and can be synthesized in an eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - Sugar-derived compound of formulae (I-II) is new.    R=H or methyl;    X=S or H (sic);    Y'=H or F;    n=1 or 2; and    m=10.    An INDEPENDENT CLAIM is also included for a method for preparing sugar-derived compound.
NOVELTY - A methanol gasoline comprises (pts.wt.) gasoline (40-90), methanol (60-10), cosolvent (0.5-8), and modifier (0.01-5). The cosolvent is prepared by mixing propyl alcohol, neopentyl glycol, pentaerythritol, isopropanol, tertbutanol, naphtha, diethyl ether, ethylene glycol, and/or oleic acid. The modifier comprises (pts.wt.) alcohol solvent (40-80), corrosion inhibitor (0.1-20), anti-swelling agent (0.1-10), and lubricant (0.05-3).    USE - A methanol gasoline used for vehicle (claimed).    ADVANTAGE - The gasoline can be directly utilized on vehicles using gasoline as fuel without modifying an engine, has high octane number, has good compatibility, and has strong dynamic property.
NOVELTY - An additive comprises (vol.%) a solvent (60-70) compounded from alcohol, alcohol ether, ester, and acetone; an ignition agent (24.4-30) compounded from aliphatic hydrocarbon, aromatic hydrocarbon, and methyl tertbutyl ether; a combustion improver (4-6) compounded from nitro and nitrate; a corrosion inhibitor (1-3) compounded from phenols and greases; and a catalyst and an antioxidant stabilizer.    USE - An additive for an M50 methanol gasoline fuel (claimed).    ADVANTAGE - The additive prolongs service life of an oil pump, guarantees no deterioration and no delamination of the gasoline for a long time, and improves poor startability and dynamic property.
NOVELTY - Production of sludge biomass environment-friendly fuel comprises conveying the sludge into a pretreatment tank; adding a deodorizer and a fungicide, and agitating uniformly; conveying the pre-treated sludge into a reaction tank; adding a modifier, a sulfur-fixing agent and a heavy metal stabilizer, reacting uniformly and then adding broken biomass; performing advanced dehydration of the modified sludge; and breaking deeply dehydrated sludge cake and then drying.    USE - A production method of sludge biomass environment-friendly fuel.    ADVANTAGE - Compared with prior art, the method realizes minimization, harmlessness, stabilization and reutilization of the sludge, and effectively resolves secondary pollution of the sludge. The obtained biomass environment-friendly fuel is capable of replacing boiler coal, effectively solving the energy shortage problem and making up for the sludge treatment cost.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart illustrating the production method of sludge biomass environment-friendly fuel (Drawing includes non-English language text).
NOVELTY - A feeding spiral conveyor (1) is located in case (2). The biomass is entered into the case by air sealingdevice (3). A stirring rod element is located in the bin (4). One end of the stirring rod element is connected with a bin wall by a bolt. The stirring rod is connected with the bent stirring rod by a guide rail. The connecting rod (6) is welded on the stirring rod. A variable frequency motor (8) drives a gear box (7), to provide power for the spiral conveyor. Air sealing device ensures the feeding amount of material. The case and the gear box are fixed on a base (9) by a bolt.    USE - Spiral feeder for performing rapid pyrolysis of fluidized-bed biomass.    ADVANTAGE - The efficiency, operability and reliability of the spiral feeder can be improved.    DETAILED DESCRIPTION - The lower end of a bent stirring rod is contacted with a blade of the air sealing device to provide power for the stirring rod element by the rotation of the air sealing device. The spring unit pushes the stirring rod element to the blade, when the material is stirred by the upward and downward movement of the stirring rod element to avoid the bridging and hanging phenomena.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the spiral feeder.    Feeding spiral conveyor (1)    Case (2)    Air sealing device (3)    Bin (4)    Connecting rod (6)    Gear box (7)    Variable frequency motor (8)    Base (9)
NOVELTY - A simulated biodiesel oil comprises (wt.%): methyl myristate (0.5-2), methyl palmitate (20-30), methyl stearate (5-10), methyl oleate (35- 45), methyl linoleate (18-25) and methyl linolenate (1-3).    USE - Simulated biodiesel oil.    ADVANTAGE - The biodiesel oil has improved reliability of low temperature fluidity. The method has mild conditions, is environment-friendly, has simple and easy to control process, and easy to obtain materials, and is easy for constructing.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of simulated biodiesel oil which comprises providing fatty acid methyl ester of each monomer and adding to beaker, placing beaker in a thermostatic water cabinet having temperature of 50 degrees Cand stirring at stirring rate of 100 revolutions/minute for 10-20 minutes to obtain simulated biodiesel oil; and    (2) use of single factor method to test influences of components of simulated biodiesel oil on condensation point of simulated biodiesel oil which comprises regulating content of one component with single factor method, keeping proportion of other components unchanged and preparing biodiesel oil having different component contents; and testing condensation points of the biodiesel oil having different component contents.
NOVELTY - Additive comprises (vol.%) cosolvent consisting of alcohol, ester and ketone (30-40), igniting agent consisting of hydrocarbon and ether (50-64), combustion improver consisting of nitro and nitrate (4-6), and catalyst, corrosion inhibitor, and antioxidant stabilizer (remainder).    USE - Additive used for pure methanol fuel (claimed).    ADVANTAGE - The additive provides hydrophobic effect and certain protection on engine device, thus prolonging service life of oil pump. The antioxidant stabilizer, igniting agent and combustion improver can effectively solves problems of poor starting property and power property when pure methanol is used as car fuel; while ensuring that methanol system will not go bad for extended period. The additive has abundant raw material sources, simple production, and convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of additive in pure methanol fuel by adding additive to methanol fuel and stirring uniformly, in which additive is 4-10 vol.% of methanol.
NOVELTY - Additive comprises (%) mutual solvent composed of alcohols, glycol ethers, and esters (50-60); initiating combustion agent consisting of aliphatic hydrocarbons, aromatic hydrocarbons and methyl tert-butyl ether (30-40); combustion improver consisting of nitro and nitrates (4-6); corrosion inhibitor composed of phenols and grease (1-4); and catalyst and antioxidant stabilizer (remainder), in which amount of additive used in methanol gasoline fuel is 2-5%.    USE - Additive used for M30 methanol gasoline fuel.    ADVANTAGE - The additive improves service life of oil pump, effectively ensure that gasoline and methanol system will not deteriorate and layer for extended period, and effectively solves problems that stability and power performance are bad. It has simple process and convenient to use.
NOVELTY - Plant-based fuel and fermented soil are utilized to produce solid fuel by adding fermented soil and water to plant fuel powder to stir, processing mixture to be solid fuel via a forming device and airing, and water is stopped, and mixture can be kneaded to be lumps; and obtaining fermented soil by mixing, stacking and fermenting dried sludge, ash powder and plant fuel residue for 90-150 days, or mixing and fermenting dried sludge, ash powder, construction garbage powder and plant fuel for 90-150 days.    USE - Method for the utilization of plant-based fuel and fermented soil to produce solid fuel (claimed).    ADVANTAGE - The method does not pollute the environment, destroy the ploughs, produce waste residues, e.g. coal ash, and not produce smoke from burning coal, thus making air in rural areas to be fresh and the environment to be clean.    DETAILED DESCRIPTION - Utilization of plant-based fuel and fermented soil to produce solid fuel comprises adding fermented soil and water to plant fuel powder to stir, processing the mixture to be solid fuel via a forming device and airing, and water is stopped, and mixture can be kneaded to be lumps; and obtaining fermented soil by mixing, stacking and fermenting dried sludge, ash powder and plant fuel residue for 90-150 days, or by mixing and fermenting dried sludge, ash powder, construction garbage powder and plant fuel for 90-150 days, and ash powder is residual ash after burning the solid fuel, and weight ratio of plant fuel powder to fermented soil is 150-300:1000.
NOVELTY - Preparation of a pig manure fuel comprises mixing a pig manure optionally treated by solid-liquid separation with coal and/or crushed straw, pressing and molding the mixture, and air-drying the mixture at normal temperature or baking the mixture.    USE - Method for the preparation of a pig manure fuel (claimed).    ADVANTAGE - The pig manure has no obvious odor after being processed, and can be stored for a long time. The pig manure fuel achieves full combustion, and is free from toxic and harmful gas during the combustion process. The method eliminates the pollution of the pig manure in a large-sized pig farm to the environment. The heat energy produced by combustion can be used for warming the pig farm. The residue after combustion is rich in potassium, phosphorus, and trace elements, which can be applied to fertilizing the farmland.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a pig manure fuel.
NOVELTY - Preparation of granular biomass fuel comprises mixing (wt.%) pig manure (60-90), biomass sawdust (10-30), and charcoal (1-30); dehydrating the mixture; and granulating.    USE - Method for the preparation of a granular biomass fuel (claimed).    ADVANTAGE - The method removes odor of the manure and reduces the fire point of the prepared fuels by adding the biomass sawdust and charcoal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a granular biomass fuel.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the fly ash floatation device.    Storing device (1)    Distributing device (2)    Cylinder (3)    Gas dispersing device (4)    Floating device (5)
NOVELTY - Preparation of biodiesel in ionic liquid comprises setting up experimental reflux device; adding certain amount of purified and dried catalyst and castor oil into reactor; dissolving sodium hydroxide into methanol; adjusting stirring rate; setting reaction temperature for starting to react materials; reacting for certain time; stop reacting; decompressing and distilling to remove extra methanol; and subjecting product to gas chromatography.    USE - Preparation of biodiesel in ionic liquid.    ADVANTAGE - The method uses acetate ionic liquid that integrates catalysis with function of solvent during reaction process, thus solving defect that traditional solid base catalyst cannot be recycled. The ionic liquid has low cost, provides high yield, and can be repeatedly use. The method reduces production cost of biodiesel, and has simple and clean production process. The experiment indicates that yield of fatty acid methyl ester can reach 93.4%. The biodiesel product is energy saving and environment friendly.
NOVELTY - A distributive vegetable oil is produced by mixing vegetable at raw oil, low carbon alcohol with pyridinium trifluoromethanesulfonate ionic liquid catalyst with weight ratio of low carbon alcohol to raw oil of 1:2-1:6, where additional ionic liquid catalyst is 0.3-1% by total weight of low carbon alcohol and material oil.    USE - Method for transesterification production of distributive vegetable oil (claimed).    ADVANTAGE - The method improves yield of vegetable oil, and provides light and simple device, and, convenient for timely processing of dispersed material.    DETAILED DESCRIPTION - Transesterification production of distributive vegetable oil comprises:    (A) mixing vegetable at raw oil, low carbon alcohol with pyridinium trifluoromethanesulfonate ionic liquid catalyst with weight ratio of low carbon alcohol to raw oil of 1:2-1:6, where additional ionic liquid catalyst is 0.3-1% by total weight of low carbon alcohol and material oil;    (B) heating the mixture at 60-80 degrees C, stirring and reacting for 3-5 hours;    (C) standing the reacted material for 1-3 hours, separating the reaction material into heavy and light phase, separating the lower heavy material and the light material to obtain raw glycerol containing alcohol;    (D) standing the heavy material for 10-60 minutes and cooling, settling the catalyst on the bottom, and the residue is raw glycerol containing alcohol; adding warm water at 40-60 degrees C to the light phase material, where additional amount of warm water is 30-50% of the total weight of the material, introducing air while water washing and stirring, and water washing for 15-30 minutes; and    (E) standing the water washed material for 15-30 minutes to obtain heavy and light phase; pumping the light phase material to a drier and drying to obtain the vegetable oil.    An INDEPENDENT CLAIM is included for a device for distributive vegetable oil transesterification production.
NOVELTY - A bio-diesel from fresh rice bran is prepared by adding fresh rice bran to upper layer of a reaction kettle; adding methanol solution of sodium ethoxide with 0.5 wt.% of that of rice bran oil to lower layer of reaction kettle, and connecting upper and lower layers of reaction kettle by a filter screen film; and adding solvent/methanol mixed solvent with 6-8 times of that of the rice bran oil, heating at 50-70 degrees C for refluxing, extracting oil, and performing ester exchange reaction for 2-4 hours.    USE - Method for the preparation of bio-diesel from fresh rice bran (claimed).    ADVANTAGE - The method allows solvent to convert interface reaction in ester exchange reaction into homogeneous phase reaction, provides increased reaction speed, protects fatty acid methyl ester, avoids oxidization, provides improved performance, and lowers energy consumption, and cost.    DETAILED DESCRIPTION - Preparation of bio-diesel from fresh rice bran comprises:    (A) adding fresh rice bran to upper layer of a reaction kettle;    (B) adding methanol solution of sodium ethoxide with weight of 0.5% of that of rice bran oil to lower layer of reaction kettle, and connecting upper and lower layers of reaction kettle by a filter screen film;    (C) adding solvent/methanol mixed solvent with 6-8 times of that of the rice bran oil, heating at 50-70 degrees C for refluxing, extracting oil, performing ester exchange reaction for 2-4 hours, and ending reaction; and    (D) flashing to recycle alcohol/solvent mixed liquid, distilling the product under decompression condition, and gathering fraction at 0.098 MPa and at 140-230 degrees C to obtain bio-diesel.
NOVELTY - The rabeprazole sodium comprises rabeprazole sodium, stabilizer, pH value regulator, and pharmaceutically acceptable auxiliary materials.    USE - The rabeprazole sodium is useful for preparing injection, which is useful for treating gastric ulcer, duodenal ulcer, gastroesophageal reflux disease, helicobacter pylori infection and Zollinger-Ellison syndrome (claimed), where the injection is intramuscular injection and intravenous injection. No biological data given.    ADVANTAGE - The rabeprazole sodium can be simply and economically produced with high bioavailability and reliability in an environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing rabeprazole sodium for injection; and    (2) a method for detecting rabeprazole sodium.
NOVELTY - Extraction of jasminoidin comprises crushing jasmine, extracting, absorbing extract solution by porous absorbing resin, rinsing resin, collecting rinsing solution, condensing and drying, with porous absorbing resin comprising ADS-21 type or ADS-17 type or ADS-7 type, or ADS-F8 type strong polar porous absorbing resin.    USE - Method for extracting of jasminoidin (claimed).    ADVANTAGE - The method takes water and ethanol as extracting solvent, does not have solid residue or process wastewater, is environment-friendly process with good product quality and suitable for industrial production.
NOVELTY - An oxiracetam is refined by adding oxiracetam crude product to mixed solvent of absolute ethyl alcohol, phosphoric acid and glacial acetic acid; heating up to 78-82 degrees C; refluxing; adding active carbon; refluxing, filtering to obtain colorless clean solution; stirring and separating the crystal for 10-12 hours at 5-10 degrees C; and centrifuging and drying to obtain oxiracetam fine product.    USE - Method for refining an oxiracetam (claimed).    ADVANTAGE - The method has simple operation and is environmentally friendly, and provides oxiracetam fine product having 99.9% purity and impurity of less than 0.1%.
NOVELTY - Preparation of sesamin comprises grinding sesame, adding 60-80% ethanol, refluxing twice, mixing extracts, and concentrating to obtain extract; sampling extract, adsorbing macroporous resin columns, eluting ethyl acetate-methanol mixed solution in gradients, collecting sesamin fraction, recovering reagent to minute extension, and reserving crystallization; and processing coarse crystallization in anhydrous ethanol, boiling, recrystallizing for 2-3 times, filtering and drying at low temperature to obtain product.    USE - Method for preparing sesamin (claimed).    ADVANTAGE - The method has low cost and high yield and produces product with high purity and low in carbon and environment-friendly.
NOVELTY - Salicylaldehyde Schiff alkali double-core cobalt coordination compound (I) is new.    USE - Compound (I) used in preparing medicine for treating human chronic myeloid leukemia (claimed).    ADVANTAGE - Compared with common platinum type and 5-fluorouracil anticancer medicines, the compound (I) has high anticancer activity and product yield, good fat solubility and stability, low production cost, and simple and pollution-free preparation method.    DETAILED DESCRIPTION - Salicylaldehyde Schiff alkali double-core cobalt coordination compound of formula (I) is new. An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Invention relates to a novel method of producing hydrochlorides of amine-derivatives of adamantane of general formula: , where R=H, CH3; n=0, 1. According to the disclosed method, biologically active compounds such as, for example, hydrochlorides of 1-aminoadamantane (R=H, n=0) (amantadine) and 1-amino-3,5-dimethyl-adamantane (R=CH3, n=0) (memantine) are obtained, which are used in the chemical and pharmaceutical industry to prepare medicinal agents for treating Parkinson's disease, Alzheimer's diseases, neurodegenerative diseases, glaucoma etc. The method involves reaction of adamantane carboxylic acid with thionyl chloride at its boiling point for 1.5 hours in molar ratio 1:1.1 respectively, to form an acyl chloride of adamantane carboxylic acid, which reacts with sodium azide in anhydrous toluene at its boiling point in molar ratio 1:1:15-20 respectively for 1.5-2 hours, followed by addition of concentrated hydrochloric acid and holding the reaction mass for 1 hour and extracting the end product.    USE - Chemistry.    ADVANTAGE - Method is more technologically effective and ecologically clean and enables to obtain a large number of homologues of hydrochlorides of amine-derivatives of adamantane with quantitative output of 92-95%. 4 ex
NOVELTY - Bioethanol obtaining method involves preliminary raw material treatment. Green raw material is collected and crushed, and fluid is obtained. Yeast or special alcohol bacteria are added to the obtained fluid. Fermentation process is performed during 3-5 days. Distillation is performed so that crude alcohol is obtained, and after that, rectification of crude alcohol is performed so that final product - bioethanol is obtained. In addition, as raw material for obtaining bioethanol there used is wild or domestic hogweed containing 17-31% of saccharose of budding phase to flowering phase.    USE - Power industry.    ADVANTAGE - Reduction of use of cultures of food purpose as initial components for obtaining bioethanol; restricting the spread and harmfulness of hogweed as aggressive invasive type of plants. 1 cl, 1 dwg, 1 ex
NOVELTY - Production of briquettes, where the biofuel briquettes are fabricated from almond shells, comprises: collecting shells; washing of almond shells; drying almond shells with tube air, keeping them in a uniform moisture value of 1-2%; and briquetting of almond shells in briquetting machines for the formation of a briquette.    USE - The method is useful for producing biocombustible briquettes (claimed).    ADVANTAGE - The method makes it possible considerably to optimize the process for producing solid biocombustible briquettes, resulting in an end-product of higher quality for use as fuel in various types of equipment and combustion system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a briquette biofuel obtained by the process above.
NOVELTY - A solid-state fuel is refuse-derived fuel obtained by mixing fly-ash modified material containing aluminum compound, silicon compound and/or aluminum-silicon compound.    USE - Solid-state fuel e.g. refuse paper and plastic fuel and refuse derived fuel.    ADVANTAGE - The solid-state fuel suppressed adhesiveness of clinker and generation of corrosion.
NOVELTY - The apparatus has modifier (20) to generate fuel gas using source gas containing hydrocarbon. A modification-catalyst containing ruthenium is provided with storage chambers (202,203), such that pressure loss during inflow of source gas into chamber (203) is higher than that during inflow of source gas into chamber (202). The carbon contained in source gas is precipitated in chamber (202). The inflow of source gas to chamber (203) is increased autonomously because when flow path where source gas passes along catalyst vicinity in chamber (202) becomes narrow, flow resistance increases.    USE - Fuel cell apparatus for generating electric power.    ADVANTAGE - The fuel cell apparatus can use up the modification catalysts for switching the flow path of gas, without the need of drive unit. The temperature of the storage chambers is maintained efficiently, thus the modification performance of the modifier can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the modifier.    Modifier (20)    Storage chambers (202,203)    Inflow port (207)    Communication hole (209)    Outflow port (214)
NOVELTY - Gas permeable ceiling of a bio-gas container (1), comprises a circumferential side wall, and a surface element (6) that spans an interior of the container. The surface element is formed as a close-meshed textile network or fabric.    USE - Used as a gas permeable ceiling of a bio-gas container.    ADVANTAGE - The mounting of the ceiling is simple, fast, and economical, and the ceiling ensures an improved quality of the produced bio-gas.    DESCRIPTION OF DRAWING(S) - The figure 1 shows a schematic top view of the ceiling with the bio-gas container. The figure 2 shows a schematic perspective view of the material of the ceiling in a larger scale.    Bio-gas container (1)    Support (3)    Surface element (6)    Reinforcing element (7)    Covering (10)
NOVELTY - Hexose and/or pentose are made to react with reaction system containing two layers of aqueous solution layer and organic-solvent layer, in presence of acidic catalyst to obtain 2-furaldehyde compound. The aqueous solution layer comprises aqueous solution containing salt (I) of alkali metal and phosphoric acid.    USE - Manufacture of 2-furaldehyde compound. Uses include but are not limited to synthetic intermediate for pharmaceutical, agrochemical, fragrance and liquid fuel, monomers for polymer, and raw material for manufacturing furan resin, furan and solvent e.g. tetrahydrofuran.    ADVANTAGE - The method economically and efficiently provides 2-furaldehyde compound with reduced corrosion of reaction apparatus and energy consumption.    DETAILED DESCRIPTION - Hexose and/or pentose are made to react with reaction system containing two layers of aqueous solution layer and organic-solvent layer, in presence of acidic catalyst to obtain 2-furaldehyde compound. The aqueous solution layer comprises aqueous solution containing salt of formula: MaH(3-a)PO4 (I) of alkali metal and phosphoric acid.    M=alkali metal;and    a=0.2-0.95.
NOVELTY - The apparatus (10) has photovoltaic generator (100) which light-receives and generates electromotive force in the state immersed in aqueous solution. Main case consists of semiconductor that is provided with pn junction surface. The main case is equipped with the interface layer (200,300) formed in the light-receiving surface with translucency, reflection preventing property, and electroconductivity, and covers the light-receiving surface of main case. The interface layer is film provided with water resistant solution property.    USE - Photovoltaic apparatus for hydrogen-producing apparatus (claimed).    ADVANTAGE - The photovoltaic generator generates the electromotive force stably with few components can be realized effectively. The resistivity of the apparatus can be reduced. The cost can be reduced by reducing complex tools.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for photovoltaic apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the photovoltaic apparatus. (Drawing includes non-English language text)    Photovoltaic device (10)    Photovoltaic generator (100)    Semiconductor layers (110p,110n)    Interface layers (200,300)
NOVELTY - A forward osmosis membrane (10) comprises: a porous support layer (110); a thin film (120) formed on one side of the porous support layer; and nanomaterials (130) dispersed in the porous support layer and the thin film.    USE - As forward osmosis membrane (claimed) in a variety of applications such as forward osmosis-based wastewater reclamation, seawater and brackish water desalination, bioenergy production, food and pharmaceutical processing, and power generation.    ADVANTAGE - The forward osmosis membrane provides improved water permeability, salt rejection, and fouling resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for forming (M1) the forward osmosis membrane involving forming the porous support layer by phase inversion of a polymer solution; forming the thin film by interfacial polymerization of monomers in a liquid on the porous support layer; and dispersing the nanomateriais in at least one of the porous support layer and the thin film.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic cross-sectional diagram of a forward osmosis membrane in flat sheet form.    Forward osmosis membrane (10)    Support layer (110)    Dense top layer (111)    Porous bottom layer (112)    Pores (113)    Thin film (120)    Nanomaterials (130)
NOVELTY - Fuel composition comprises: a hydrocarbon derived from a biological source containing plant oil and/or animal fat, where the hydrocarbon and fuel composition is at least substantially free of oxygen.    USE - The fuel composition is useful: as aviation fuel in aircrafts (airplanes and helicopters); as cold weather fuel for ground transportation vehicles (trucks, automobiles and railroads); and as a replacement for heating oil to heat houses.    ADVANTAGE - The fuel composition exhibits a low cloud point, thus used in cold temperature environments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fuel composition comprising: reacting a compound derived from the biological source with water to form free fatty acid; subjecting the free fatty acid to Kolbe electrolysis in the presence of an electrolyte; and removing an oxygen-containing carboxyl group from the free fatty acid to form the hydrocarbon.
NOVELTY - The method comprises collecting plant materials of waste branches, fallen leaves, weeds, bush branches and crops straw in a fruit garden and collecting people and livestock manure, digging cross ventilate ditches on the fruit garden land, paving large branches on the ventilate ditches to prevent substances to block the ventilate ditches, paving 800-1000 kg of plant materials on the plane of the ventilate ditches, uniformly spraying 40-50 kg of people and livestock manure and then paving 800-1000 kg of plant materials, and repeatedly paving and spraying for 5-30 layers.    USE - The method is useful for composting natural fertilizer for kiwi fruit. No biological data given.    ADVANTAGE - The method is capable of simply composting the natural fertilizer with high quality in an environmentally friendly manner.    DETAILED DESCRIPTION - The method comprises collecting plant materials of waste branches, fallen leaves, weeds, bush branches and crops straw in a fruit garden and collecting people and livestock manure, digging cross ventilate ditches on the fruit garden land, paving large branches on the ventilate ditches to prevent substances to block the ventilate ditches, paving 800-1000 kg of plant materials on the plane of the ventilate ditches, uniformly spraying 40-50 kg of people and livestock manure and then paving 800-1000 kg of plant materials, repeatedly paving and spraying for 5-30 layers, adding water to dryness of the plant materials while paving and spraying, and covering with light-proof black plastic film. The ditches have depth of 8-1 cm and width of 12 cm. An edge of the black plastic film contacting with the ground is compressed by mud and sealed. The compost in the black plastic film generates high temperature and are fermented and changed into powder mud, after 3-8 months.
NOVELTY - A multi-enzyme traditional Chinese medicine organic fertilizer is produced by mixing (%) rice husk meal (30), humic acid (30), plant ash (19), bone meal (10), medical stone (3), Chinese herbal medicine (3), sugar syrup (2), saccharomycetes (1), and strain (2) comprising 20% of effective microorganisms (EM) strain, 10% of diethyl aminoethyl hexanoate (DA-6) and 10% of Bacillus subtilis.    USE - Method of producing multi-enzyme traditional Chinese medicine organic fertilizer (claimed).
NOVELTY - Enzyme (I) for catalyzing diacyl glycerol to acidylate, comprising amino acid sequence of SEQ ID NO: 1 (comprising a fully defined 724 amino acid sequence as given in the specification) and an amino acid sequence in a substituted, deletion or addition of one or more amino acids, is new.    USE - (I) is useful in the field of biodiesel production (claimed) and in genetic engineering microalgae.    ADVANTAGE - (I) improves the production of the genetic engineering microalgae better, and greatly reduces the production cost of the biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a nucleotide coding (I); and    (2) a recombinant plasmid for expressing (I).
NOVELTY - A free water flushing and free discharge ecological toilet comprises degradation biochemical reactor. A biochemical reactor shell (1) is two parallel cylinder, where two ends of waist body (2) comprises annular sealed container in cylinder and are respectively provided with spiral conveying stirring device (3). One end of cylinder is provided with motor and variable speed transmission device, and other end is provided with door (9). Biochemical reactor is provided above pedestal pan or squatting pan. Cylinder has opening hole and connected to lower outlet of pedestal pan or squatting pan.    USE - Free water flushing and free discharge ecological toilet.    ADVANTAGE - The toilet has simple structure, is compact, has reliable connection and large volume, and has light weight, and good sealing performance. It has also good heat-insulating property, saves energy, and ensures toilet without obstacle and easy to use.    DETAILED DESCRIPTION - Free water flushing and free discharge ecological toilet comprises degradation biochemical reactor. A biochemical reactor shell (1) is two parallel cylinder, where two ends of waist body (2) comprises annular sealed container in cylinder and are respectively provided with spiral conveying stirring device (3). One end of cylinder is provided with motor and variable speed transmission device, and other end is provided with door (9). Biochemical reactor is provided above pedestal pan or squatting pan. Cylinder has opening hole and connected to lower outlet of pedestal pan or squatting pan. Connecting pipe and exhaust fan in cylinder are filled with biological base material. Other end of first air outlet hole (7) is provided in cylinder side.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view illustrating a free water flushing and free discharge ecological toilet.    Biochemical reactor shell (1)    Waist body (2)    Spiral conveying stirring device (3)    First air outlet hole (7)    Door (9)
NOVELTY - Method of processing sewage sludge using diatomite absorbent, involves mixing diatomite, sewage sludge and calcium oxide, stirring the mixture uniformly, fermenting the mixture, subjecting the mixture to extrusion and granulation, drying or dehydrating the particles using stainless steel rotary kiln, sintering the particles and cooling the particles, where the dehydration is performed at 80-600 degrees C, drying is performed at 80-600 degrees C, high-temperature drying (sintering) is performed at 800-1250 degrees C and cooling is performed at 200-400 degrees C.    USE - The method is useful for processing sewage sludge.    ADVANTAGE - The method is simple and cost-effective as the sewage absorbent (diatomite) can be used repeatedly in sewage treatment process.    DETAILED DESCRIPTION - Method of processing sewage sludge using diatomite absorbent, involves mixing (in %) diatomite (35-43), sewage sludge (55-64) and calcium oxide (1-2), where the sludge contains water of less than 70%, stirring the mixture uniformly, fermenting the mixture for 10-15 days, subjecting the mixture to extrusion and granulation to obtain particles of 2-5 cm, where shape of the particles is spherical or gravel shape, drying or dehydrating the particles using stainless steel rotary kiln, sintering the particles and cooling the particles, where the dehydration is performed at 80-600 degrees C for 18-22 minutes, drying is performed at 80-600 degrees C at 18-22 minutes, high-temperature drying (sintering) is performed at 800-1250 degrees C for 18-20 minutes and cooling is performed at 200-400 degrees C for 18-20 minutes. The diatomite comprises silicon dioxide (more than 55), aluminum oxide (6-10), magnesium oxide (0.6-2.5), potassium oxide (0.01-1.2), calcium oxide (0.9-6) and sodium oxide (1.2), where the size of diatomite is 50-200 meshes.
NOVELTY - The organic fertilizer comprises 5 parts by weight (pbw) of castor bean, 5 pbw of bitter almond, 2 pbw of garlic, 2 pbw of radix sophorae flavescentis, 10 pbw of bone, 20 pbw of dry leaves and straws, 30 pbw of chicken manure and human excreta, 23 pbw of cattle, sheep and pig manures, 3 pbw of plant ash, and 25 pbw of castor-oil plant stem leaf decoction. The dry leaves comprise dry pine needles. The bone comprises pig bone, cattle bone, sheet bone or chicken bone. The castor-oil plant stem leaf decoction is formed by soaking the dry castor-oil plant stem leaf with water.    USE - The organic fertilizer is useful for controlling underground insect damage. No biological data given.    ADVANTAGE - The organic fertilizer improves the disease resistance of the crops, can be easily and economically prepared with high nutritional value and quality in a safe manner, and effectively promotes the microorganism of the soil.    DETAILED DESCRIPTION - The organic fertilizer comprises 5 parts by weight (pbw) of castor bean, 5 pbw of bitter almond, 2 pbw of garlic, 2 pbw of radix sophorae flavescentis, 10 pbw of bone, 20 pbw of dry leaves and straws, 30 pbw of chicken manure and human excreta, 23 pbw of cattle, sheep and pig manures, 3 pbw of plant ash, and 25 pbw of castor-oil plant stem leaf decoction. The dry leaves comprise dry pine needles. The bone comprises pig bone, cattle bone, sheet bone or chicken bone. The castor-oil plant stem leaf decoction is formed by soaking the dry castor-oil plant stem leaf with 8-10 times of the weight of the water for 30-40 hours and then boiling the mixture using high fire. An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer.
NOVELTY - Treatment of city sludge comprises dehydrating sludge from a sewage treatment plant, mixing with chaff, and uniformly stirring, where the water content of sludge after dehydration is 75-80%, and the sewage comprises (pts.wt.) mud (1) and chaff (0.1-0.3); high temperature sterilizing at 90-125 degrees C for 10-30 minutes under stirring; inoculating Metarhizium anisopliae (0.01-0.05) in the mixture, and stirring; aerobic fermenting at 20-50 degrees C for 6-12 days; and naturally cooling to room temperature to obtain a biopesticide containing M. anisopliae (0.61-0.85).    USE - Method for the treatment of city sludge (claimed) used to prepare a M. anisopliae biopesticide used for controlling locust; and fertilizer for dry land crops, seedlings, flowers, and lawn.    ADVANTAGE - The method is inexpensive and safe, and eliminates secondary pollution of sludge.
NOVELTY - Comprehensively using kitchen waste, comprises: (A) pre-processing the kitchen waste; (B) preparing the biodiesel; (C) using water phase; and (D) preparing the protein feed.    USE - The method is useful for comprehensively using kitchen waste (claimed).    ADVANTAGE - The advantages of the method are as follows: the process is simple and easily implemented; the processing cost of the kitchen waste is reduced and energy is saved; the process of using the mixture of A. oryzae and S. cerevisiae to perform co-fermentation is used, the utilization rate of the raw material is high, and once fermentation is finished and no secondary pollution will be generated.    DETAILED DESCRIPTION - Comprehensively using kitchen waste, comprises: (A) pre-processing the kitchen waste: sorting out the collected kitchen waste, adding water, pulping and crushing, then separating by an oil-water separator to obtain the oil phase and water phase; (B) preparing the biodiesel: preparing into biodiesel by the oil phase via ester exchange method; (C) using water phase: sterilizing the obtained water phase and then fermenting, after fermenting, centrifuging and getting the supernate to distil, then the fuel ethanol is obtained, and the centrifuged solid residue is for future use; (D) preparing the protein feed: drying and crushing the centrifuged solid residue, then the protein feed is obtained.
NOVELTY - 8,8,9,9-Tetradeuterium hexadecane is used as tracer to detect a metabolic pathway in a process for producing methane by anaerobic degradation of alkane.    USE - The 8,8,9,9-tetradeuterium hexadecane is used as tracer to detect a metabolic pathway in a process for producing methane by anaerobic degradation of alkane (claimed).    ADVANTAGE - Compared with the prior art, the 8,8,9,9-tetradeuterium hexadecane does not influence the initial activation of alkane and can obtain information of an intermediate metabolite useful for the research on anaerobic degradation mechanism of petroleum hydrocarbon.
NOVELTY - Recombinant Escherichia coli is new, where the preservation number is CGMCC No. 4706.    USE - The recombinant Escherichia coli is useful for producing the cyclic adenosine monophosphate (claimed).    ADVANTAGE - The recombinant Escherichia coli is prepared in a simple, rapid, effective and an environmental friendly manner.
NOVELTY - Extracting buddleoside A from Buddleia davidii, comprises taking Buddleia davidii and crushing in 60-80 meshes, adding the powder into a super-critical extracting kettle at a pressure of 15-30 MPa and temperature of 40-50 degrees C, extracting by super-critical carbon dioxide in a gradient manner, analyzing and collecting the extract, adding the extract into alumina for drying, filling in a column, eluting by anhydrous ethanol and petroleum ether, freezing and crystallizing, and filtering and drying for obtaining the buddleoside A.    USE - The method is useful for extracting buddleoside A from Buddleia davidii (claimed), which is useful for killing insects, and promoting blood circulation. No biological data given.    ADVANTAGE - The method is capable of extracting buddleoside A from Buddleia davidii with improved yield and reduced energy consumption in a large scale, simple, and an environmental friendly manner.
NOVELTY - Preparing N-(2-propargyl)-hydantoin, involves: dissolving N-(2-propargyl)-N-amino carbethoxyacetonitrile into the solvent, adding promoter, dropping alkaline catalyst after being heated to from 20-80 degrees C, and carrying out cyclization reaction while carrying out heat preservation for 1-6 hours; cooling the reaction liquid to room temperature, dropping acid to neutralize pH value to be 6-8, and then decompressing, stilling and removing ethanol as byproduct, separating out crystals after cooling 0-10 degrees C and drying the crystals.    USE - For preparing N-(2-propargyl)-hydantoin (claimed) used as intermediate for synthesizing medicinal, pesticidal, and disinfectant compound.    ADVANTAGE - The preparation method is simple, involves safe operation, provides high yield, and it is low cost method with little waste discharge. The method uses low equipment investment, simple technique, does not need catalyst and is environment-friendly.    DETAILED DESCRIPTION - Preparing N-(2-propargyl)-hydantoin, involves: dissolving N-(2-propargyl)-N-amino carbethoxyacetonitrile into the solvent, adding the promoter, dropping alkaline catalyst after being heated to 20-80 degrees C, and carrying out cyclization reaction while carrying out heat preservation for 1-6 hours; where the molar ratio of the promoter to N-(2-propargyl)-N-amino carbethoxyacetonitrile is 1-10:1, and the molar ratio of alkaline catalyst to N-(2-propargyl)-N-amino carbethoxyacetonitrile is 1-1.5:1; cooling the reaction liquid to room temperature, dropping acid to neutralize pH value to be 6-8, and then decompressing, stilling and removing ethanol as byproduct, starting separating out crystals after cooling to 0-10 degrees C while carrying out heat preservation for 0-10 degrees C until the crystals are not separated, drying the crystals, and obtaining N-(2-propargyl)-hydantoin.
NOVELTY - A 17-(2,4-dichlorophenyl)-11,14-dioxatetracyclo(8.7.0.02,7.012,16)heptadeca-1(10),2(7),3,5,8,12(16)-hexaen-15-one is new.    USE - 17-(2,4-Dichlorophenyl)-11,14-dioxatetracyclo(8.7.0.02,7.012,16)heptadeca-1(10),2(7),3,5,8,12(16)-hexaen-15-one is useful in preparation of medicine for treating cancer (claimed).    ADVANTAGE - The 17-(2,4-Dichlorophenyl)-11,14-dioxatetracyclo(8.7.0.02,7.012,16)heptadeca-1(10),2(7),3,5,8,12(16)-hexaen-15-one has strong activity and high absorption, and is prepared at high yield by simple and environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of 17-(2,4-dichlorophenyl)-11,14-dioxatetracyclo(8.7.0.02,7.012,16)heptadeca-1(10),2(7),3,5,8,12(16)-hexaen-15-one.
NOVELTY - Method involves preliminary acetylation of chitin with acetic anhydride, washing and drying the acetylated chitin in order to reduce degree of deacetylation thereof and, as a result, increase output of the desired product - D(+)-glucosamine hydrochloride when obtaining said product through hydrolysis of acetylated chitin with concentrated hydrochloric acid while heating, followed by evaporation, crystallisation, separation, washing and drying the desired product.    USE - Chemistry.    ADVANTAGE - High output of the desired product while maintaining its high quality; method is more environmentally friendly since pre-treatment of chitin reduces the amount of processing wastes. 1 cl, 2 ex
NOVELTY - The cheer pack for kindling timber fire and grille fire, is claimed, where shredded production residues of wood (1) are filled in pouches made of porous tea bag paper (2) containing a sealing (3) at lower and upper ends and then dipped into hot, liquid candle wax. The production residues of wood have maximum dimensions of 3 x 1 x 1 cm. The pouches, in the inflated state, have a width of 90 mm and a length of 110 mm.    USE - The cheer pack is useful for kindling timber fire and grille fire in fireplaces, furnaces, coal furnaces, stoves and grills.    ADVANTAGE - The cheer pack ensures high burning time and burning intensity and pleasant, light scent of the candle wax.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a cheer pack for kindling timber fire and grille fire.    Wood (1)    Porous tea bag paper (2)    Sealing. (3)
NOVELTY - The method involves feeding the coal and biomass into gasification portion (4) of combustion reactor (2). The water vapor is heated and coal is pressurized at elevated temperature and pressure to generate product gas (8). The filtered product gas (8') and partially oxidized bed material (20) are fed into combustion portion (6) of reactor. The exhaust gas (16) of combustion portion is led to turbine and reduced bed material (22) is led into oxidation reactor (24) fed with air (26) to re-oxidize bed material to recirculation into combustion portion.    USE - Method for gasification and combustion of biomass and coal with partial carbon dioxide separation using combined reactor.    ADVANTAGE - Effective separation of carbon dioxide that allows for efficient sequestration is enhanced. The long-term stability of the materials used in the process and the system are enabled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for gasification and combustion of biomass and coal with partial carbon dioxide separation using combined reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the chemical looping combustion of solid fuels with integrated purification of hot product gas.    Combustion reactor (2)    Gasification portion (4)    Combustion portion (6)    Product gas (8)    Filtered product gas (8')    Exhaust gas (16)    Oxidized bed material (20)    Reduced bed material (22)    Oxidation reactor (24)    Air (26)
NOVELTY - Method for washing hydrogen sulfide and carbon dioxide from a gas obtainable by gasification of carbonaceous biomass, comprises: contacting the gas with a first absorbent solution comprising transition metal ions, where the transition metals comprises copper, zinc, iron and/or cobalt, in acidic aqueous solution; binding hydrogen sulfide to the first absorbent solution; recovering the gas; contacting recovered gas with a second absorbent solution comprising an organic solvent; binding carbon dioxide to the second absorbent solution; and recovering the washed gas.    USE - The method is useful for washing hydrogen sulfide and carbon dioxide from a gas obtainable by gasification of carbonaceous biomass.    ADVANTAGE - The method is capable of effectively washing hydrogen sulfide and carbon dioxide with high purity and less energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing hydrocarbons or its derivatives from biomass raw material comprising (i) gasifying the biomass raw material in the presence of oxygen to produce a gas comprising carbon monoxide, carbon dioxide, hydrogen and hydrocarbons, (ii) optionally a tar reforming step, (iii) optionally removing tar components e.g. naphthalene from the gas, (iv) optionally adjusting the hydrogen to carbon monoxide ratio, (v) washing using the method as above per se, (vi) converting in a synthesis reactor at least a significant part of the carbon monoxide and hydrogen contained in the gas into a product comprising hydrocarbon composition or its derivatives, and (vii) recovering the hydrocarbon or its derivative as the product.
NOVELTY - Making biomass solidified shaping material, involves crushing area of agriculture, forestry wastes, and cotton wood chips in crusher; controlling length of the raw material at 2 mm by small hole filter screen, drying the raw material having water content of less than 20%, putting the crushed raw material for solidifying to form biomass solidified shaping material by small hole, where the diameter of the biomass solidified shaping fuel is controlled at 8 mm on the grain forming machine.    USE - For making biomass solidified shaping material (claimed) useful for industrial boiler and civil furnace.    ADVANTAGE - The method provides biomass solidified shaping material that automatically feed with full combustion; and is quickly started fire.
NOVELTY - The device has a biomass fuel gas making chamber that provides gas spray to combustion chamber. A sealing cone is connected with lever type sealing cone operating rod. A collecting chamber is provided on the lower sealing plate and the feeding port sealing tray. A water receiving plate is provided between the feed port of the sealing disc and the operating rod. A biomass fuel gas making chamber is set at the lower portion of rotary grate. A lower rotating fire grate is provided with a primary wind pipe, lower water seal tank, and the lower sealing plate.    USE - Biomass fuel reflection furnace.    ADVANTAGE - The explosion proof performance and efficiency of the biomass fuel reflection furnace can be improved. The energy consumption of the biomass fuel reflection furnace can be reduced. The biomass fuel reflection furnace is environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass fuel reflection furnace.
NOVELTY - The tower has a rectifying tower body (1) equipped with a lifting tower body (2). A heating tray (7) is arranged at a bottom part of the rectifying tower body. The heating tray is provided with multiple layers. The layers are alternately arranged to form an S-shaped liquid channel. The heating tray is provided with a heat conducting oil inlet (7-3), a heat conducting oil outlet (7-1), a heating pipe tank (7-2), a heating tray baffle (7-4) and a liquid pipe (7-6). Upper and lower sides of the rectifying tower body are connected with an inner wall of a steam channel (9).    USE - Multi-layer vaporizing bio-diesel rectifying tower.    ADVANTAGE - The tower can reduce biodiesel gasification process and improve biodiesel distillation yield. The heating tray reduces liquid layer thickness so as to reduce pressure of surface load of an electric heating tube and temperature of heat conductive oil. The tower can reduce energy consumption. The tower is easy to clean.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a multi-layer vaporizing bio-diesel rectifying tower.    Rectifying tower body (1)    Lifting tower body (2)    Heating tray (7)    Heat conducting oil outlet (7-1)    Heating pipe tank (7-2)    Heat conducting oil inlet (7-3)    Heating tray baffle (7-4)    Liquid pipe (7-6)    Steam channel (9)
NOVELTY - The furnace has a cracking chamber arranged in a furnace body. An air inlet is fixed on an upper part outer wall of the furnace body. A feeding port is arranged at an upper end of the furnace body. A lower side of the furnace body is provided with a furnace door. An upper end of the cracking chamber is provided with an emergency discharging device. A vent hole is formed in an outer wall of the cracking chamber.    USE - Biomass fuel cracking furnace.    ADVANTAGE - The furnace improves burning efficiency of biomass fuel and reduces heat energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fuel cracking furnace.
NOVELTY - The solar energy marsh gas pool comprises a solar energy heat collecting plate (1), a solar water storage tank (3), a circulating water pump (4) and a heat exchanger (7), and a methane fermenting system. The temperature control system comprises a temperature sensor present in solar energy water tank (2), a marsh gas tank and a temperature controller. The methane fermenting system comprises a methane fermenting tank, a methane pool feeding port and a biogas pool discharging port. The temperature control system controls the circulating water pump to open or close.    USE - Used as a solar energy marsh gas pool.    ADVANTAGE - The solar energy marsh gas pool allows to maintain the marsh gas in a relatively constant and stable environment for long period of time without altering its properties and any damage.    DETAILED DESCRIPTION - The solar energy marsh gas pool comprises a solar energy heat collecting plate (1), a solar water storage tank (3), a circulating water pump (4) and a heat exchanger (7), and a methane fermenting system. The temperature control system comprises a temperature sensor present in solar energy water tank (2), a marsh gas tank and a temperature controller. The methane fermenting system comprises a methane fermenting tank, a methane pool feeding port and a biogas pool discharging port. The temperature controller analyzes the solar energy obtained from the temperature sensor in the water storage tank and the marsh gas tank. The temperature control system is provided in the solar energy water storage tank and the biogas fermenting tank, and controls the circulating water pump to open or close.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a solar energy constant temperature.    Solar energy heat collecting plate (1)    Solar energy water tank (2)    Solar water storage tank (3)    Circulating water pump (4)    Heat exchanger. (7)
NOVELTY - Method (M1) for processing cellulose biomass, involves immersing cellulose biomass in solution containing an ionic liquid and an alkali.    USE - The method is useful for processing cellulose biomass which is useful for preparing sugar, alcohol and organic acid (all claimed).    ADVANTAGE - The method has excellent saccharification efficiency and provides high yield of alcohol, sugar and organic acid.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing saccharide from cellulose biomass, involves immersing cellulose biomass in solution containing an ionic liquid and an alkali, and reacting the product with cellulase; and    (2) method (M3) for preparing alcohol or organic acid from cellulose biomass, involves immersing cellulose biomass in solution containing an ionic liquid and an alkali, reacting the product with cellulase and fermenting the obtained product.
NOVELTY - A catalyst comprises (in %mass) manganese carbonate containing silica (10-25), organic binder (6 or less) and ruthenium (0.5-5). The catalyst has surface area of 100-210 m2/g, and pore volume of 0.1-0.6 ml/g.    USE - Catalyst is used for manufacturing hydrocarbon (claimed).    ADVANTAGE - The catalyst efficiently and economically forms hydrocarbon with high conversion ratio and selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst, which involves mixing manganese carbonate containing silica and organic binder, molding the kneaded material, obtaining support, drying at 250 degrees C or less, preparing catalyst precursor and supporting with ruthenium; and    (2) manufacture of hydrocarbon, which involves performing Fisher-Tropsch reaction of gas containing hydrogen and carbon monoxide as main component using catalyst.
NOVELTY - Composition comprises a nanoparticle and a polymer, where the nanoparticle is embedded in the polymer and the polymer is essentially not permeable to oxygen gas and water.    USE - The composition is useful for storing hydrogen (claimed) from molecular hydrogen.    ADVANTAGE - The composition is capable of storing hydrogen in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of storing hydrogen, comprising (a) providing the composition, (b) contacting a molecular hydrogen with the composition, and (c) increasing the temperature of the composition such that the molecular hydrogen is separates from the composition.
NOVELTY - Production of 2-butanol, involves (a) providing a recombinant microbial host cell comprising at least one DNA molecule encoding a polypeptide that catalyzes a substrate to product conversion chosen from (i) pyruvate to alpha -acetolactate, (ii) alpha -acetolactate to acetoin, (iii) acetoin to 3-amino-2-butanol, (iv) 3-amino-2-butanol to 3-amino-2-butanol phosphate, (v) 3-amino-2-butanol phosphate to 2-butanone, and (vi) 2-butanone to 2-butanol, and (b) contacting the host cell with a fermentable carbon substrate in a fermentation medium under suitable conditions.    USE - The method is useful for production of 2-butanol used as biofuel or fuel additive for fuel cells or combustion engines in vehicles, feedstock chemical in plastic industries, and as food-grade extractant in food and flavor industries.    ADVANTAGE - The method is safe, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Production of 2-butanol, involves (a) providing a recombinant microbial host cell comprising at least one DNA molecule encoding a polypeptide that catalyzes a substrate to product conversion chosen from (i) pyruvate to alpha -acetolactate, (ii) alpha -acetolactate to acetoin, (iii) acetoin to 3-amino-2-butanol, (iv) 3-amino-2-butanol to 3-amino-2-butanol phosphate, (v) 3-amino-2-butanol phosphate to 2-butanone, and (vi) 2-butanone to 2-butanol, where the DNA molecule is heterologous to the microbial host cell, and (b) contacting the host cell with a fermentable carbon substrate in a fermentation medium under conditions suitable for 2-butanol production.
NOVELTY - Compost comprises deer horn shaped Ganoderma lucidum having antimicrobial activity.    USE - The compost is useful for controlling soil disease with respect to crops and providing immunopotentiation effect. The crops include ornamental plant, horticultural plant and agricultural plant.    ADVANTAGE - The compost is inexpensive, has excellent stability, and enables to control soil disease simply and easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the compost, which involves mixing components chosen from rice bran, bran, oil cake, brown sugar, sawdust, wood chip, bamboo leaf powder, chip, straw, hay, dried reed, pulp and pulp residue, stirring the obtained mixture, adding water to the obtained mixture, maintaining moisture content of the mixture at 60-80% and pH at 4.5-7.5, packaging the obtained mixture in a rectangular shaped container having sheets such as a plush tick film of the same type in as frame, where the film has height of 10 cm to 1.5 m, depth of 50 cm to 2 m, and thickness of 10-30 cm, sterilizing the packaged product using steam, inoculating deer horn shaped G.lucidum to sterilized product, growing the hypha at 20-30 degrees C, shredding the mycelial mass having size diameter of 1-2 cm, shredding hypha, curing the obtained compost, and mixing the obtained compost at 30-60 degrees C.
NOVELTY - Straw is soaked in water in mass ratio of 1:1-1:3 at 15-90 degrees C for 10-60 minutes. The straw is supplied to a steam-explosion tank maintained at 0.3-2 MPa, preferably 0.5-1 MPa. The straw is supplied to acid hydrolysis tank filled with 0.8-1.6% dilute acid, and hydrolyzed at 75-105 degrees C for 10-60 minutes. The hydrolyzed material is filtered to obtain hydrolyzate. The residue is collected and squeezed to obtain solid. Thus, biomass-based product is produced from straw hemicellulose.    USE - Method for producing biomass-based product from straw hemicellulose.    ADVANTAGE - The biomass-based product is efficiently produced without generating pollutants and waste.    DETAILED DESCRIPTION - Straw is soaked in water in mass ratio of 1:1-1:3 at 15-90 degrees C for 10-60 minutes. The straw is supplied to a steam-explosion tank maintained at 0.3-2 MPa, preferably 0.5-1 MPa, and processed for 1-10 minutes. The straw is then discharged after predetermined time. The straw is supplied to acid hydrolysis tank filled with 0.8-1.6% dilute acid, and hydrolyzed at 75-105 degrees C for 10-60 minutes. The mass ratio of straw to dilute acid is 1:2-1:7. The hydrolyzed material is filtered to obtain hydrolyzate. The residue is collected and squeezed to obtain solid. Thus, biomass-based product is produced from straw hemicellulose.
NOVELTY - A gas hydrate (1) is obtained by reacting raw water containing ion resulting from dissociation of an electrolyte in solution as a substance having gas-hydrate decomposition-suppression effect, with a hydrate-forming substance. Sodium chloride is added as the electrolyte. The concentration of chloride ion in raw water is 0.1-6.5 mol/m3.    USE - Manufacture of gas hydrate of methane gas, natural gas, and carbon dioxide gas.    ADVANTAGE - The method enables manufacture of gas hydrate suitable for long-term storage. The self-preservation of gas hydrate is high. Decomposition of gas hydrate is inhibited. Sodium chloride and calcium chloride are safe, economical, and easy to handle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for storage method of gas-hydrate in a storage tank in which the pressure is atmospheric pressure and temperature is -23 degrees C to less than 0 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the mechanism of self-preservation effect of gas hydrate.    Gas hydrate (1)    Water film layer (2)    Ice film (3)
NOVELTY - An upper panel is arranged on a display screen. A water inlet (4) is provided on left side of the upper panel. A water outlet is connected with tower (18). An air outlet hole (5) is formed on the upper panel. A reaction chamber (13) is provided on the main frame (12). A sealing material outlet is provided on the front panel. A blade is provided on the moving shaft. A main board is connected on the blade.    USE - Organic waste processor.    ADVANTAGE - The efficiency, operability and reliability of the organic waste processor can be improved. The pollution waste and decomposition of bacteria in organic waste processor can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the organic waste processor.    Water inlet (4)    Air outlet hole (5)    Main frame (12)    Reaction chamber (13)    Tower (18)
NOVELTY - A fast pyrolysis method of waste mycelium comprises mixing waste mycelium and inorganic compound at a mass ratio of 100:2-3, drying the mixture at 105 degrees C, granulating the mixture, heating the granules at 100-200 degrees C under anoxytropic condition, and heating further the mixture at 250-600 degrees C for 10-30 minutes to obtain pyrolytic oil and non-condensing gas. The inorganic compound is potassium carbonate, zinc chloride and/or monopotassium phosphate.    USE - A fast pyrolysis method of waste mycelium.    ADVANTAGE - The method reduces pollution.
NOVELTY - A multi-functional biomass conversion furnace comprises a vertical material cabin (2) mounted in a furnace body (1); a material cabin cover (201) mounted at the top of the material cabin; a pyrolysis chamber (202) mounted at the lower part of the material cabin; a furnace grate (4) mounted between the pyrolysis chamber and a combustion chamber located at the bottom of the furnace body; and a heat exchange chamber mounted between the material cabin and inner wall of the furnace body.    USE - A multi-functional biomass conversion furnace.    DETAILED DESCRIPTION - A multi-functional biomass conversion furnace comprises:    (A) a vertical material cabin (2) mounted in a furnace body (1);    (B) a material cabin cover (201) mounted at the top of the material cabin;    (C) a pyrolysis chamber (202) mounted at the lower part of the material cabin;    (D) a furnace grate (4) mounted between the pyrolysis chamber and a combustion chamber located at the bottom of the furnace body;    (E) a heat exchange chamber mounted between the material cabin and inner wall of the furnace body;    (F) an air flow buffering chamber mounted at the upper part of the heat exchange chamber;    (G) an air inlet passage mounted between the bottom of the heat exchange chamber and the combustion chamber;    (H) air holes connected with the air inlet passage and distributed on the wall of the pyrolysis chamber;    (I) a coal outlet mounted on the wall of the furnace body between the heat exchange chamber and the combustion chamber;    (J) a smoke cylinder mounted at the top of the air flow buffering chamber; and    (K) a water inlet and a water outlet mounted on the side wall of the heat exchange chamber.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a multi-functional biomass conversion furnace.    Furnace body (1)    Vertical material cabin (2)    Furnace grate (4)    Material cabin cover (201)    Pyrolysis chamber (202)
NOVELTY - Automatic molding system of biomass flat-die particles comprises a drying part, a crushing part, a material conveying part, a molding part and cooling, drying and separating part. A feeding port is connected with the crushing part and drying part. The feeding port is connected with a discharge hole of the crushing part through the material conveying part and molding part. The discharge hole is connected with the cooling, drying and separating part and molding part.    USE - Used as an automatic molding system of biomass flat-die particles.    ADVANTAGE - The system adopts the integrated automatic control system to realize the multi-section biomass molding the automatic operation, reduces the manual operation, ensures the system to automatically operate under the optimized condition, and has low energy consumption, low labor cost and heat utilization rate of more than 60%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the automatic molding system of biomass flat-die particles.
NOVELTY - A dry fermentation device comprises a fermentation tank (3) provided with an air outlet on its bottom part and a circulating pipe; a heat exchange pipe (9) provided with a grid plate (2) provided with a straw feed inlet (8) and a water supply opening (10) on its lower part; an air outlet main nozzle; a pipe pump; a spiral conveyor; and a gravity settler located on the side of the fermentation tank and connected with inlet of the spiral conveyor.    USE - A dry fermentation device for straws.    ADVANTAGE - The device prevents formation of straw hardening and straw bridging, has improved gas generating rate and recirculation of active sewage, has reduced water consumption, reduces pollution, and assures stable fermentation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a dry fermentation device.    Grid plate (2)    Fermentation tank (3)    Straw feed inlet (8)    Heat exchange pipe (9)    Water supply opening (10)
NOVELTY - The device has a vehicle auxiliary wall plate guardrail (2) that is provided with bridge plate (4), wall plate and transport vehicle (1). Air guide pipe is provided with gas-guide tube valve (9). A petrol power machine (13) is arranged with starting pull rope handle (14). A pulping cover is fixed on pulping self-sucking pump (19). A cutting blade plate that is equipped with driving cutting S-shaped blade. A liquid separator is connected with the suction pipe whose end is movably connected with loose joint (11).    USE - Motor pulping biogas liquid vehicle-mounted draw spraying device.    ADVANTAGE - The problem related to operation of farm marsh gas tank and septic tank urbanization discharging transporting difficult can be solved effectively. The pollution in environment can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the Motor pulping biogas liquid vehicle-mounted draw spraying device.    Transport vehicle (1)    Vehicle auxiliary wall plate guardrail (2)    Bridge plate (4)    Gas-guide tube valve (9)    Loose joint (11)    Petrol power machine (13)    Starting pull rope handle (14)    Pulping self-sucking pump (19)
NOVELTY - An air cleaner comprises cylindrical porous photocatalyst element (7) which is attached to the mounting hole by which the plasma excitation light catalyst unit (2) is formed in the plane electrode (8) and has inner side space which is formed as purification process space (6) in which air circulates, and acicular electrode (14) which produces plasma discharge between the plane electrodes and protrudes in purification process space from one opening part of the porous photocatalyst element.    USE - Air cleaner for refrigerator, shoe cupboard, closet and motor vehicle.    ADVANTAGE - Purification process efficiency is remarkably improved even if low storage small capacity power supply like dry cell is used.    DESCRIPTION OF DRAWING(S) - The drawing shows an enlarged view of the principal part of the air cleaner. (Drawing includes non-English language text).    Plasma excitation light catalyst unit (2)    Purification process space (6)    Porous photocatalyst element (7)    Plane electrode (8)    Acicular electrode (14)
NOVELTY - Methane gas production system comprises four-step digestion tank in which organic waste is successively supplied inside a chamber 12 of the digestion tank, bio-block in which bacteria inhabits and produces methane gas in the respective built in chamber 1, chamber 3 comprising highest organic loading rate digester, chamber 4-6, chamber 7-9, chamber 10-12 inside digester, independent circulating pump which is equipped with multiple recycling pipes, and unit which reversely recirculates fluid in the lower part of each single step digestion tank.    USE - The system is useful for producing methane.    ADVANTAGE - The system improves productivity of methane.    DETAILED DESCRIPTION - Methane gas production system comprises four-step digestion tank in which organic waste is successively supplied inside a chamber 12 of the digestion tank, bio-block in which bacteria inhabits and produces methane gas in the respective built in chamber 1, chamber 3 comprising highest organic loading rate digester, chamber 4-6, chamber 7-9, chamber 10-12 inside digester, independent circulating pump which is equipped with multiple recycling pipes, where the recycling pipes are connected in digestion tank in the chamber 12 as the lower portion of chamber, and unit which reversely recirculates fluid in the lower part of each single step digestion tank.
NOVELTY - The apparatus has a grinder (3) and a feed regulator (4) for feeding the uniformly compressed and dense fuel product into drums to compact the fuel product when loaded into the containers to minimize the air space between the fuel products. The natural lignin is used to bind the torrefied biomass into fuel product, and the natural binder and organic binder (2) are added to completely bind the biomass when the lignin is not sufficient to bind.    USE - Apparatus for converting crushed torrefied biomass into dense fuel product for use in power plant.    ADVANTAGE - The crushed torrefied biomass can be efficiently converted into dense fuel product. The air space between the fuel products in the container can be reduced, and the moisture resistant and high carbon calorific value of the fuel product can be improved. The carbon dioxide emission and global warming when using the fuel product are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for converting crushed torrefied biomass into dense fuel product.    Organic binder (2)    Grinder (3)    Feed regulator (4)    Slaker drum (5)    Hopper (7)
NOVELTY - A core press assembly (130) has an air outlet (136) which is formed in one end of second press assembly (120), and an air channel (131) in which is air is flowed in from outside. The outer periphery of core press assembly is located at constant interval according to inner periphery of first press assembly (110). An elastic material (140) is inserted into air channel and compacted by air outlet when pressure is applied in a state when raw material is filled in space between second press assembly and core press assembly.    USE - Extruding mold for tube production used in fuel cell electrode and filter for atmosphere purification.    ADVANTAGE - The blocked end of the tube can be easily broken away from the core press assembly after molding is performed without deformation. Therefore, productivity can be improved and high- quality tube is produced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the extruding mold.    First press assembly (110)    Second press assembly (120)    Core press assembly (130)    Air channel (131)    Air outlet (136)    Elastic material (140)
NOVELTY - Producing organic fertilizer via biological plant ash and furfural residue, comprises: (a) collecting furfural residue and plant ash, and air-drying to make the water content of 15-20%; (b) mixing, stirring and stacking the ash of furfural residues and plant having a weight ratio of 2.7-3:2.2-2.5, using plastic film or canvas cover for 24 hours at a temperature of 36 degrees C, spreading the mixture, removing the water and crushing into powder with a granularity of 1-2 mm, to obtain the mixed material; and (c) mixing the obtained product with pelleting machine spray granulation.    USE - The fertilizer is useful for improving physical and chemical properties of soil, and crop growth. No biological data given.    ADVANTAGE - The method provides fertilizer in a simple and easy manner.
NOVELTY - Biological soil is produced by collecting biological soil crust, crushing, drying, and sieving to prepare microbiotic particle; collecting epiphytic fungi soft rotten wood, pulverizing, drying, and sieving to prepare rotten wooden meal; collecting plant litter and weeds, and burning to obtain grass peat; and mixing microbiotic particle, rotten wooden meal and grass peat, where the crust is 70-80 wt.% (dry), the rotten wooden meal is 15-25 wt.% and the grass peat is 5 wt.%.    USE - Method of producing biological soil used for restoring and reconstructing vegetation in a mined land (claimed) or useful in cultivating and promoting growth of Indigofera pseudotinctoria.    ADVANTAGE - The method has convenient and simple operation and no ecological risk, and can effectively solve poor mine soil condition (high in manganese ore). The obtained biological soil contains large amount of beneficial organisms, and is rich in nutrients.
NOVELTY - Collecting and integrating biological tar comprises (a) purifying and separating the high temperature hybrid gas containing biological tar gas and biological acetic acid gas, collecting the biological tar and the biological acetic acid in the gas, (b) performing extraction and separation for the collected biological tar to separate out the biological acetic acid, and (c) performing normal pressure distillation and separation for purified biological tar, collecting the distillates and the residue in different temperature ranges for re-conversion utilization.    USE - The method is useful for collecting and integrating biological tar.    ADVANTAGE - The method is capable of collecting and integrating biological tar in a simple and an economical manner.    DETAILED DESCRIPTION - Collecting and integrating biological tar comprises (a) purifying and separating the high temperature hybrid gas containing biological tar gas and biological acetic acid gas by a cooling and still laying method, collecting the biological tar and the biological acetic acid in the gas, (b) performing extraction and separation for the collected biological tar to separate out the biological acetic acid, and (c) directly using the purified biological tar to manufacture the biological tar waterproof paste and the biological adhesive, or performing normal pressure distillation and separation for the purified biological tar, collecting the distillates and the residue in different temperature ranges for re-conversion utilization, where the invention solves the problem that the wastewater containing the biological tar and the biological acetic acid in the existing gasification and carbonization process of the agricultural wastes is discharged into the farmland to generate secondary pollution, and simultaneously collects the waste biological tar to perform conversion utilization to improve the efficiency of the agricultural wastes.
NOVELTY - Preparing industrial creosote of biomass tar, comprises (i) performing atmospheric distillation of anhydrous biomass tar, collecting the fractions; (ii) using sodium carbonate to perform washing of the acid in the industrial creosote, removing acids and separating acid-salt solution, washing the residual matter and removing the aqueous layer; and (iii) adding sodium hydroxide solution, stirring to form a mixed liquid, allowing to stand at 50-60 degrees C, separating neutral oil layer to obtain industrial creosote of biomass tar with 4% neutral oil, removing the 4% neutral oil in phenol salt solution.    USE - The method is useful for preparing industrial creosote of biomass tar.    ADVANTAGE - The method solves the secondary pollution problem of biomass tar during the utilization of the agricultural wastes carbon gasification technology, and improves the economic benefit of the agricultural wastes carbon gasification technology utilization.    DETAILED DESCRIPTION - Preparing industrial creosote of biomass tar, comprises (i) performing atmospheric distillation of anhydrous biomass tar, collecting the fractions of biomass tar at 190-230 degrees C and serving as industrial creosote of biomass tar materials; (ii) using sodium carbonate to perform washing of the acid in the industrial creosote of biomass tar material, removing acids in the raw materials and separating acid-salt solution, washing the residual matter with distilled water and removing the aqueous layer; and (iii) adding sodium hydroxide solution (10-15%), uniformly stirring to form a mixed liquid, allowing to stand at 50-60 degrees C, separating neutral oil layer to obtain industrial creosote of biomass tar with 4% neutral oil, removing the 4% neutral oil in phenol salt solution to obtain industrial creosote.
NOVELTY - Methanol-gasoline composition comprises (in wt.%) methanol (40-55), gasoline (40-55), ethanol (2-5), dimethylbenzene (0.8-1.9) and dicyclopentadienyl iron (0.09-0.19). The composition is prepared by uniformly mixing the above mentioned components.    USE - Used as a methanol-gasoline composition.    ADVANTAGE - The composition has good anti-detonating property and stability; and is non-corrosive, and economical.
NOVELTY - Fermentation storehouse comprises a pedestal, a storehouse body and a ventilation device which are arranged in the storehouse. The storehouse is cylindrical in shape. The ventilation device is provided with a ventilation tube set at the middle of the storehouse body. The ventilation tube penetrates the storehouse body, and extends out of the fermentation storehouse. The upper end of the storehouse body is provided with a top cover. The ventilation tube set at lower part of top cover is provided with a rain shield. The pedestal comprises a brick surrounding wall and a crosspiece.    USE - The storehouse is useful for preparing feed or an organic fertilizer by fermenting dried, ripened or fresh broomcorn, corn, straw, wheat straw, rape, tobacco and bean straw, as a base fertilizer.    ADVANTAGE - The storehouse saves labor energy, promotes in-situ conversion of crop byproducts, is environmental-friendly, and effectively increases the additional value of the agricultural products.    DETAILED DESCRIPTION - Fermentation storehouse comprises a pedestal, a storehouse body and a ventilation device which are arranged in the storehouse. The storehouse is cylindrical in shape. The ventilation device is provided with a ventilation tube which is set at the middle of the storehouse body. The ventilation tube penetrates into the entire storehouse body, and extends out of the fermentation storehouse. The upper end of the storehouse body is provided with a top cover. The ventilation tube set at the lower part of the top cover is provided with a rain shield. The pedestal comprises a brick surrounding wall and a crosspiece which is arranged on the surrounding wall. One side of the pedestal is opened, and provided with a material collecting port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the fermentation storehouse.
NOVELTY - A cleaning fuel is used for micro-emulsifying diesel oil, gasoline and fuel oil boiler.    USE - Cleaning fuel used for micro-emulsifying diesel oil, gasoline and fuel oil boiler.    ADVANTAGE - The method can effectively reduce pollutant emission, has wide fuel source, reduces fuel consumption, protects environment and saves energy and reduces dependency of oil inlet.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (A) producing a clean fuel;    (B) application of ethanol gasoline, high ethanol gasoline modifier, metal, rubber or plastic; and    (C) application of biological diesel ,waste animal and vegetable oil in methyl esterification technique condition of biological diesel and performance.
NOVELTY - Preparation of biomass energy particles comprises mechanically processing and pressing sawdust and/or rice husks at 1:1 volume ratio, where volume ratio of biomass energy particles constituted by sawdust and rice husks is 1:0.5-1:5.    USE - Preparation of biomass energy particles (claimed).    ADVANTAGE - The method has low energy consumption and production cost. Compared with the prior art biomass particle fuel production method, the method can reduce the energy consumption and cost by 20%. The biomass particles do not contain any chemical agent, thus, free from any pollution to the environment during production and use.
NOVELTY - Manufacturing hydrogen and alcohol using anaerobic fermentation system comprises filtering the domestic sewage via screen to remove the solid impurities, diluting the molasses wastewater, adding nitrogen and phosphorus fertilizer, and domesticating under oxygen atmosphere for two weeks; inoculating the domesticated sludge into a continuous flow stirring tank reactor and controlling reaction temperature, and adjusting the chemical oxygen demand (COD) concentration in the reactor using molasses wastewater to 2000-6000 mg/l; and mixing molasses wastewater with domestic sewage and fermenting.    USE - The method is useful for manufacturing hydrogen and alcohol using anaerobic fermentation system.    ADVANTAGE - The method: is simple and yields high productivity easily, has easy separation, and is suitable for industrial production.    DETAILED DESCRIPTION - Manufacturing hydrogen and alcohol using anaerobic fermentation system comprises: (i) filtering the domestic sewage via screen (diameter of 0.5 mm) to remove the solid impurities, diluting the molasses wastewater until the chemical oxygen demand (COD) in the solution is 10000 mg/l, adding nitrogen and phosphorus fertilizer, and domesticating under oxygen atmosphere for two weeks, where the weight ratio of COD, nitrogen and phosphorus is 1000:5:1; (ii) inoculating the domesticated sludge into a continuous flow stirring tank reactor and controlling the reaction temperature at 35-40 degrees C, maintaining the hydraulic retention time for 4-6 hours, and adjusting the COD concentration in the reactor using molasses wastewater to 2000-6000 mg/l; and (iii) mixing molasses wastewater with domestic sewage and fermenting for 24-30 hours to obtain hydrogen and liquid ethanol.
NOVELTY - Preparation of biodiesel comprises providing grease and monohydric alcohol to a reactor and performing ester exchange reaction; distilling the monohydric alcohol from the reacted crude product, where product is divided into mixed ester phase and glycerol phase or water phase; separating the mixed ester phase from the glycerol phase or water phase; returning one part of the mixed ester to the reactor inlet for mixing with grease in the reactor; and respectively distilling the remaining mixed ester and glycerol phase or water phase to obtain high-purity aliphatic ester and glycerol.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method provides biodiesel with low acid value at high yield.
NOVELTY - A plant and animal oil and fats catalytic hydrogenation method involves treating plant and animal oil and fats in hydrogenation reactor in a presence of hydrogen and catalyst under hydrodeoxygenation and olefin saturation reaction to obtain effluent-I. The effluent-I is separated into gas and liquid phase by using high pressure separator, where the liquid phase is fractionated to obtain gas, diesel fraction and unconverted fraction. The diesel and unconverted fractions are recycled in hydrotreating reactor. The diesel fraction is mixed with modified material in the hydrotreating reactor.    USE - Method for catalytic hydrogenation in plant and animal oil and fats for producing high quality diesel.    ADVANTAGE - The method enables providing diesel with high quality and yield.    DETAILED DESCRIPTION - A plant and animal oil and fats catalytic hydrogenation method involves treating plant and animal oil and fats in hydrogenation reactor in a presence of hydrogen and catalyst under hydrodeoxygenation and olefin saturation reaction to obtain effluent-I. The effluent-I is separated into gas and liquid phase by using a high pressure separator, where the liquid phase is fractionated to obtain gas, diesel fraction and unconverted fraction. The diesel and unconverted fractions are recycled in the hydrotreating reactor. The diesel fraction with modified material is mixed in the hydrotreating reactor in the presence of catalyst and hydrogen to obtain effluent-II. The effluent-II is separated into gas and liquid phase by using a high pressure separator. The liquid phase is fractionated to obtain naphtha and diesel oil products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a method for catalytic hydrogenation in plant and animal oil and fats.
NOVELTY - Biomass liquid fuel comprises 80-98 wt.% of biomass pyrolysis oil, 0.5-5 wt.% of polymerization inhibitor, and 0.5-5 wt.% of emulsifier agent.    USE - The biomass liquid fuel is useful for power generation.    ADVANTAGE - The polymerization inhibitor and emulsifying agent can improve storage stability and fluidity of the biomass liquid fuel for a long time.
NOVELTY - A cordycepic acid is prepared by taking out raw materials; adding 15-20 times deionized water; heating to extract for 2-3 times; combining extracting solution to obtain extracting solution; passing extracting solution through ultrafiltration membrane system; and filtered liquid passes through membrane system for removing impurities to obtain nano-filtered liquid; heating nanofiltered liquid to concentrate until relative density is 1.3-1.32, cooling, and crystallizing; and dissolving coarse crystallizations in dehydrated ethanol to crystallize for 2-3 times, and drying to obtain a product.    USE - Method for the preparation of cordycepic acid (claimed).    ADVANTAGE - The method is simple, low cost, good recycling economy, low carbon and environmental protection, and provides high purity product.
NOVELTY - A 3-amino propanesulfonic acid is synthesized by heating and pressurizing 2-propylene-1-sodium sulfonate and liquid ammonia in the presence of a catalyst, subjecting mixture to addition reaction, adding dilute sulfuric acid to acidify, heating and concentrating, filtering while hot, cooling and crystallizing the filtrate, filtering, washing the filter cake, and drying.    USE - Method of synthesizing a 3-amino propanesulfonic acid.    ADVANTAGE - The method is short, concise and environment-friendly; utilizes cheap, safe and easy to obtain raw materials; and reduces production cost.
NOVELTY - Producing Bacillus psychrosaccharolyticus exopolysaccharide, is claimed, where it relates to the microorganism of Bacillus psychrosaccharolyticus, named as HD-3, which is preserved in the China microorganism strain preservation management committee common microorganism centre, and the preservation number is CGMCC No. 4519.    USE - The process is useful for producing Bacillus psychrosaccharolyticus exopolysaccharide, which is useful for producing water as a functional component for absorbing heavy metal ion and antifungal disease fertilizer, where the fertilizers are foliar fertilizer, and drip irrigation or bacterial fertilizer (claimed).    ADVANTAGE - The process is capable of economically producing Bacillus psychrosaccharolyticus with good moisture retention for plant peripheral soil, stem and leaf, and high yield in an environmental friendly manner.
NOVELTY - Dexamethasone palmitate compound (I) is new.    USE - (I) is useful for treating chronic rheumatic arthritis (claimed). No biological data given.    ADVANTAGE - (I) is safe, non-toxic, and inexpensive, and reduces adverse events. (I) can be prepared with high purity and yield in a large scale and an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing (I).
NOVELTY - Disclosed is a microbial transformation process for synthesis of fenofibric acid from fenofibrate using a mesophilic fungus Cunninghamella blakesleeana NCIM 687. The method involves growing fungal culture in a nutrient medium under controlled conditions and pH, adding fenofibrate to the culture separately at 27 degrees C, incubating the mixture for 4 days on rotator shaker (120 revolutions/minute) to obtain fenofibric acid. The culture broth is extracted using ethyl acetate to obtain fenofibric acid (II). The method is ecofriendly simple and economic. The fenofibric acid obtained by the method is active metabolite which is more potent than fenofibrate in treatment of hyperlipidemia and hypertriglyceridemia. Image 0/0
NOVELTY - The woodchip having diameter of 1 cm or less is collected. The collected woodchip is conveyed to iron mill in which pulverization is performed so as to obtain granular material having diameter of 3mm or less by sieving. The collected granular material is blown along with coal dust into a blast furnace or coke oven through a tube, while maintaining heating temperature of 350-450 degreeC within the coke oven or blast furnace of steel manufacturing converter.    USE - Utilization method of woody biomass.    ADVANTAGE - The woody biomass can be utilized easily by simple technique while effectively reducing amount of carbon dioxide- gas generation. The sensible heat of high temperature waste gas in a steel manufacture process is used effectively while ensuring safe operation.    DETAILED DESCRIPTION - The granular material is heated inside the coke oven or blast furnace of steel manufacturing converter for 2-minutes. The separation of granular material is performed by removing the waste gas and carbon content after heating processes.    DESCRIPTION OF DRAWING(S) - The drawing shows the block flow diagram illustrating utilization method of woody biomass. (Drawing includes non-English language text)
NOVELTY - The method involves utilizing a plasma technology unit for burning solid waste. Produced slag and metal is recycled by the plasma technology unit. Mixed gas is flown to a burning combustible gas combustion power generation unit. Electricity energy is generated by a methane carrier gas unit. The methane carrier gas unit is connected with the plasma technology unit and provided a small molecular substance. The small molecular substance is generated by a gas unit. The small molecule substance is separated from a synthesis part. The mixed gas is generated by a burning unit.    USE - Plasma waste heat single recycling method.    ADVANTAGE - The method enables avoiding greenhouse gas emission energy and realizing waste recycling and harmless treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plasma waste heat single recycling system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a plasma waste heat single recycling method.'(Drawing includes non-English language text)'
NOVELTY - The system has multiple catalyst heaters (10) equipped with a fuel tank (15) for supplying a methanol fuel to platinum or palladium catalyst (13). The catalyst heater generates heat when the fuel and oxidizing gas are supplied from the fuel tank to the catalyst. A portion of the gas warmed by the heat supplied to the catalyst is circulated and supplied to the catalyst. The temperature of each portion of a motor vehicle is adjusted using the heat generated by the catalyst heater.    USE - Temperature control system of electric vehicle e.g. car. Can also be used in hybrid vehicle and fuel cell electric vehicle.    ADVANTAGE - The temperature of the motor vehicle can be adjusted efficiently even in a cold region. The fall of the capability of motor vehicle can be prevented. The vehicle can be driven in a comfortable environment. The consumption of electric power can be reduced. The flight range of motor vehicle can be extended. The life of the battery can be prolonged. The catalyst heater is compact and the operation at the time of maintenance can be simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the temperature control system. (Drawing includes non-English language text)    Catalyst heaters (10)    Catalyst (13)    Fuel tank (15)    Filter (16)    Receiving tray (18)
NOVELTY - Making a hierarchical mesoporous carbon comprises: impregnating (S2) a metal salt containing aqueous solution comprising a metal salt and water in an ordered mesoporous silica (OMS); forming an OMS-metal oxide complex by heat treating (S3) the resulting product in a first heat treating process; impregnating (S4) a carbon precursor mixture in the OMS-metal oxide complex; forming an OMS-metal oxide-carbon complex by heat treating the resulting product in a second heat treating process; and etching (S6) the OMS-metal oxide-carbon complex with an acidic or a basic solution.    USE - The hierarchical mesoporous carbon is used as a support catalyst, which is useful in manufacturing fuel cell.    ADVANTAGE - The hierarchical mesoporous carbon has an optimized mesoporous distribution characteristics, and has an increased total pore volume, hence has a significantly improved catalytic activity with reduced catalyst particle content. The hierarchical mesoporous carbon facilitates the supply of fuel and transportation of byproducts in the manufacture of fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the hierarchical mesoporous carbon obtained by the method.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of the method for manufacturing hierarchical mesoporous carbon.    Preparing metal salt containing aqueous solution (S1)    Impregnating metal salt containing solution to OMS (S2)    Heat treating (S3)    Impregnating carbon precursor mixture (S4)    Etching with acidic or basic solution (S6)
NOVELTY - A sewage-treatment apparatus consists of a biological reactor (1) to which activated sludge is supplied, a unit (5) for measuring nicotinamide adenine dinucleotide (NADH) value in the biological reactor, an aerator (3) for supplying oxygen to the biological reactor, and a controller (4) for controlling the aerator by setting the measured NADH value as a parameter.    USE - Apparatus is used for treating sewage.    ADVANTAGE - The apparatus efficiently reduces greenhouse gas emitted during sewage treatment. Advancing inhibition of nitrification-denitrification reaction is suppressed by maintaining aerobic region in a microorganism floc, and an anoxia region in an appropriate range by setting the measured value of NADH measurement unit as control parameter. The apparatus is compatible with respect to maintenance of water quality and reduction of dinitrogen oxide production amount.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage-treatment apparatus. (Drawing includes non-English language text)    Biological reactor (1)    Aerator (3)    Controller (4)    NADH measurement unit (5)    Treated water (101)
NOVELTY - Method for suppressing generation of surplus sludge, involves modifying activated sludge by aerating oxygen enrichment gas, and carrying out activated sludge treatment of organic wastewater using microorganisms within an aerator, where concentration of mixed liquor suspended solid (MLSS) in an aerator is 2000-30000 mg/l.    USE - The method (M1) is useful for suppressing generation of surplus sludge. The method (M2) is useful for treating wastewater. The method (M3) is useful for preparing modified activated sludge (claimed).    ADVANTAGE - The method is simple and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for treating wastewater, involves carrying out activated sludge treatment process of wastewater using microorganisms, and collecting sludge by carrying out sedimentation of processed organic wastewater; and    (2) method (M3) for preparing modified activated sludge, involves aerating oxygen enrichment gas in the activated sludge.
NOVELTY - The arrangement (140) has separator plates (150, 160) defining a region of a wet-side flow channel (154). Water vapor transfer (WVT) membranes (170) are arranged on surfaces of the separator plates so that a region of a common, planar, dry-side flow channel (164) is formed between the transfer membranes. Edge strips are positioned between the membranes so that the dry-side flow channel region is formed. A thickness of the dry-side flow channel region is defined by the strips. An individual support e.g. thread, is positioned below the dry-side flow channel region.    USE - WVT-separator plate arrangement for transferring water vapor produced by a fuel cell i.e. proton exchange membrane (PEM) fuel cell, of a fuel cell system.    ADVANTAGE - The arrangement can be made thinner, lighter and simpler, and efficiently transfers water vapor between adjacent flow fields in a WVT-device for providing moistening of a dry WVT-side.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a WVT arrangement. The thread is made of plastic, distributed adhesive or glass.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an edge section directed along dry-side flow channels of parts of a WVT-separator plate arrangement including wet-side plates.    WVT-separator plate arrangement (140)    Separator plates (150, 160)    Upper and lower diffusion medium (152)    Wet-side flow channel (154)    Common, planar, dry-side flow channel (164)    WVT membranes (170)
NOVELTY - A wood coal (1) which is a dry material, is thrown into a container (2) and stirred. Air is supplied and wood coal is made to generate heat naturally. The wood coal is dried with generated heat until humidity of exhaust gas discharged from the container reaches predetermined value. Thus, wood coal is dried.    USE - Method for drying wood coal used as fuel for boiler.    ADVANTAGE - The wood coal is dried without using exterior heat energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for drying system of wood coal, which has the container, stirring unit (4) for stirring wood coal, an air supply unit (8) for supplying air to the container, a humidity measuring unit (16) for measuring humidity of exhaust gas, and a control unit (17) for controlling stirring rate, air supply amount or temperature of air.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of drying system of wood coal. (Drawing includes non-English language text)    Wood coal (1)    Container (2)    Stirring unit (4)    Air supply unit (8)    Nitrogen supply unit (9)    Heating unit (13)    Temperature measuring units (14,15)    Humidity measuring unit (16)    Control unit (17)
NOVELTY - The method comprises crushing a carbon source comprising garden garbage comprising leaves, pruning and flower and nitrogen source material comprising kitchen garbage and water treatment sludge, urban inland river and lake sludge pipeline well and human and animal excreta into granule with grain diameter of 2-50 mm, and dehydrating the material having water content of more than 80% to less than 80%. The nitrogen source material is present at less than 30 wt%.    USE - The method is useful for fermenting town biomass waste material.    ADVANTAGE - The method is simple.
NOVELTY - The tobacco microbial organic fertilizer composition comprises (30-50 parts by weight (pbw)) of ferment bean, 0.2-1 pbw of Bacillus subtilis agent, and 49-69.8 pbw of humic acid.    USE - Used as a tobacco microbial organic fertilizer composition. No biological data given.    ADVANTAGE - The tobacco microbial organic fertilizer composition is simple and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing tobacco microbial organic fertilizer composition.
NOVELTY - The device has a spiral feeder arranged in a feeding opening of a gasification furnace. A top part or 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 through the pipeline. A top part of the secondary dust remover is provided with an output pipe. The primary dust remover and the secondary dust remover are equipped with a funnel shaped ash outlet. The side wall of the gasification furnace is provided with a viewing port.    USE - Saponin hydrolysate extraction residue gasification device.    ADVANTAGE - The device saves energy consumption, and protects the environment from being polluted.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a saponin hydrolysate extraction residue gasification device.
NOVELTY - The method involves providing an anode diffusion layer with a micro porous layer, and preparing a cathode (1) with the micro porous layer. Specific mass of carbon powder and ethanol are mixed in specific mass ratio. Function layer suspension or a solution layer is deposited and accumulated using an electric fluid power spray. An electric heating plate is heated to remove solvent when a layer is deposited on the plate and stress concentration is reduced. A cathode diffusion layer is utilized as a substrate.    USE - Method for manufacturing an integrated fuel cell membrane electrode.    ADVANTAGE - The method enables batch production of the membrane electrode in a simple and cost effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an integrated fuel cell membrane electrode.    Cathode (1)    Cathode catalyst layer (3)    Proton exchange layer (5)    Anode catalyst-proton exchange transition layer (6)
NOVELTY - Increasing oil content and/or seed yield in plants comprises increasing expression of a nucleic acid encoding an alternative oxidase 1 (AOX1) protein.    USE - The methods are useful for increasing oil content and/or seed yield in plants; for producing oil; and for producing food, feed, or industrial product, where: (a) the food or feed is oil, meal, grain, starch, flour or protein; or (b) the industrial product is biofuel, fiber, industrial chemicals, a pharmaceutical or a nutraceutical. The isolated gene or the chimeric gene is useful for increasing plant seed oil content and/or Thousand Kernel Weight (all claimed).    ADVANTAGE - The methods improve plant seed yield and seed oil content by increasing the expression of AOX1.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) plants obtained by the method above; (2) an isolated Brassica napus AOX1 gene encoding the protein of SEQ ID NO. 2; or an isolated Brassica napus AOX1 gene consisting of the nucleotide sequence of SEQ ID NO. 1; (3) an isolated Brassica napus AOX1 protein consisting of the amino acid sequence of SEQ ID NO.2; (4) chimeric gene comprising the following operably linked nucleic acid molecules: (a) a heterologous plant-expressible promoter; (b) a nucleic acid encoding an AOX1 protein containing at least 60% sequence identity to SEQ ID NO. 2; and optionally (c) a DNA region involved in transcription termination and polyadenylation; (5) a plant or plant cell comprising the chimeric gene; (6) seeds from the plants; (7) oil from the seeds; (8) a method for producing oil, comprising harvesting seeds from the plants and extracting the oil from the seeds; and (9) a method of producing food, feed, or an industrial product comprising: (a) obtaining the plant or its part; and (b) preparing the food, feed or industrial product from the plant or its part. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.
NOVELTY - The reactor has a gasifier that is provided with a tubular gastight wall (3) which is arranged within a pressure vessel. The tubular gastight wall is provided with pressure relief passages (20) which are sealed by rupture elements (38,39). The pressure relief passages are provided with a sleeve (22) that has a cooled section extending outwardly from an opening in the gasifier wall. The cooled section of the sleeve is provided with a double wall to enclose an annular coolant channel (24).    USE - Gasification reactor used for producing synthetic gas by partial combustion of carbonaceous feed such as pulverized coal, oil, biomass, and gas.    ADVANTAGE - The cooled section of the sleeve is provided with the double wall to enclose the annular coolant channel, so that the damage of the pressure relief passages and the coolant channels due to the fly ash particles and the overpressure in the gasifier can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the gasification reactor.    Tubular gastight wall (3)    Pressure relief passages (20)    Sleeve (22)    Annular coolant channel (24)    Rupture elements (38,39)
NOVELTY - Membrane-free bio-electrochemical device for co-processing of electroplating wastewater and domestic sewage comprises an anode chamber for microbial catalytically degradation of domestic sewage organic matters and release of electrons and a cathode chamber for reducing metal ion acceptor electrons. The two chambers are separated by a three-phase separator and the material exchange pathway is retained. The cathode and the anode can simultaneously produce certain amount of electric energy during co-processing of domestic sewage and electroplating wastewater.    USE - Used as a membrane-free bio-electrochemical device for co-processing of electroplating wastewater and domestic sewage.    ADVANTAGE - The device does not utilize the addition of expensive membrane separation material and is economical.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the membrane-free bio-electrochemical device for co-processing of electroplating wastewater and domestic sewage (Drawing includes non-English language text).
NOVELTY - An organic fertilizer is prepared by selecting non-water washed rabbit dung (60 wt.%), clover and edible fungus leftovers (30 wt.%) and slaughtering waste (10 wt.%) as raw materials; mixing; and post-fermenting to produce organic fertilizer.    USE - As organic fertilizer used in cultivation industry (claimed).    ADVANTAGE - The nonpolluted harmless organic fertilizer shows long fertilizer efficiency, and avoids environment pollution. The organic fertilizer prepared by the method allows excretion of livestock industry, change of waste into treasure, and usage of less dosage level. The method is simple, easy to operate, low cost, allows the use of wide source of raw materials, provides economic benefit and social benefit, and is suitable for enterprise in town enterprises. The green efficient organic fertilizer provides high yield, good mouth feel, and improves the quality of the product for producing green nonpolluted agricultural products. The organic fertilizer does not damage the structure of the soil and compaction of the soil, and does not destroy natural ecological balance of soil.
NOVELTY - A recyclable degrading granulation conditioning agent comprises wood uniform body particles having a particle size of 0.5-10 cm. The wood uniform body is ball or cube processed by dry wood crusher, forming machine and mechanical equipment. The wood uniform body is provided with particle size and same shape.    USE - As recyclable degrading granulation conditioning agent for degrading granulation amendment in sludge compost (claimed).    ADVANTAGE - The wood uniform body has light weight, good fluidity, good water absorption, biodegradable, and can be easily recycled without affecting the product quality. The conditioning agent has organic ventilation property, shows slow degradation speed of compost, stable structure, improves the air in the heap in the mass transfer efficiency, good water absorption, can reduce the water content of sludge, improves permeability of material, has high organic matter, nitrogen-phosphorus-potassium nutrient content, high fertilizer effect for a long time, and acts as excellent organic slow release fertilizer and soil modifying agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for degrading granulation amendment in sludge compost involving: 1) mixing sludge and sludge conditioning agent according to mass ratio of 1: (0.35 to 1.35) to obtain the mixed material, where the water content of the material is 65%, 2) mixing material into high temperature fermenting device of aerobic fermentation at a ventilation rate of 0.05-6 m3/(min m3), and mixing material at a temperature of at least 5 days at 55 degrees C, 3) fermenting for 9-20 days, then sieving conditioning agent at a sieving rate of more than 98% to finish the amendment in sludge compost via drum screen, where in step (1), the water content of sludge is 75-85%, and the organic matter content is 40-85%.
NOVELTY - A genetically modified host cell comprising one or more recombinant nucleic acids encoding crotonase, butyryl-coA dehydrogenase, electron transport flavoprotein B, electron transport flavoprotein A, 3-hydroxybutyryl-coA dehydrogenase, acetyl-coA acetyltransferase, or aldehyde/alcohol dehydrogenase, and one or more biomass polymer-degrading enzymes, where at least one of one or more biomass polymer-degrading enzymes is secretory enzyme, is new.    USE - The host cell chosen from bacterial, fungal, yeast, plant, animal and human cell is useful for producing butanol from biomass polymer chosen from cellulose and hemicellulose, preferably xylan (all claimed), which is used in combustible fuel composition. The host cell is also useful for producing other alcohols and branched-chain hydrocarbons e.g. pinene.    ADVANTAGE - The host cell produces butanol which is an advanced biofuel, directly from input of biomass without addition of exogenous substrates or enzymes and the produced butanol allows replacement of petroleum-derived fuels with renewable fuels and ethanol. The host cell is not adversely affected during the process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing butanol from biomass polymer, which involves culturing the above-mentioned host cell in a medium to form culture such that the one or more recombinant nucleic acids are expressed in the cell, where the medium comprises biomass polymer as carbon source for the host cell, and extracting butanol from the culture.
NOVELTY - The apparatus (100) has an aerobic annihilation tub (160) that is provided for fermenting the waste cake after waste cake is mixed with digested sludge in a mixed tide structure (155). A supernatant reservoir (125) is arranged between a dehydrator (120) and an anaerobic digester (130) for temporarily storing the supernatant made in the dehydrator. The supernatant is supplied to the anaerobic digester. A fire-extinguishing sludge reservoir (150) is arranged between the anaerobic digester and mixed tide structure for absorbing supernatant in the anaerobic digester.    USE - Apparatus for disposing organic waste.    ADVANTAGE - Since the recycling efficiency of the organic waste is increased, the generation of organic waste is reduced. The generation of discharged water in non-discharge system is prevented. The installation cost of the organic waste disposing apparatus is reduced. The generation of environmental contamination in the organic waste disposing apparatus is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for disposing organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of organic waste disposing apparatus.(Drawing includes non-English language text)    Organic waste disposing apparatus (100)    Dehydrator (120)    Supernatant reservoir (125)    Anaerobic digester (130)    Fire-extinguishing sludge reservoir (150)    Mixed tide structure (155)    Aerobic annihilation tub (160)
NOVELTY - System, comprises: a filter configured to remove matter with a particle size of larger than 25 mu from a liquid component; at least one nanofilter configured to remove acids and concentrate xylose in filtered liquid component; and an apparatus configured to adjust pH of the nanofiltered liquid component using a calcium hydroxide composition.    USE - The system is useful for treating liquid component separated from biomass (lignocellulosic material containing at least one of corn cob, corn plant husk, corn plant leaves or corn plant stalks) to yield treated liquid component containing sugars available to be fermented into a fermentation product (all claimed).    ADVANTAGE - The system: increases fermentation efficiency of lignocellulosic hydrolysate without loss in fermentable sugar, sugar degradation, possible downstream effects in distillation and lactic acid bacterial contamination; and minimizes calcium buildup.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating the liquid component comprising: removing matter from the liquid component; removing acids and concentrate xylose in the liquid component; and adjusting pH of the liquid component using calcium hydroxide composition.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of a biorefinery comprising ethanol production facility.    Biorefinery (100)    Preparation apparatus (102)    Fermentation system (106)    Distillation system (108)    Waste treatment system (110)
NOVELTY - A microorganism, which belong to Klebsiella genus or Serratia genus, having the capability to produce ethanol from a glycerol, is new.    USE - The microorganism is useful for producing ethanol (claimed).    ADVANTAGE - Novel microorganisms with excellent ethanol resistance and ethanol-producing capability are provided. The microorganisms are applicable to the system which ethanol manufactured from the glycerol contained in the waste liquid which arises, for example in the refinement/purification processes of biodiesel fuel. Ethanol can be produced efficiently using the microorganism above.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for producing ethanol by contacting the wastewater containing a glycerol with the microorganism above, and collecting the produced ethanol; and    (2) a waste-water-treatment apparatus comprising the fermenter where wastewater containing a glycerol and the microorganisms are made to contact.
NOVELTY - Granular fertilizer comprises ashes of hen droppings.    USE - As granular fertilizer for rice field.    ADVANTAGE - The granular fertilizer has good disintegrability of 60% or more with respect to water, is environmentally-friendly as ashes of hen droppings are not widely dispersed and thus does not exert undesirable influence on environment, and highly effective as the fertilizer is easily absorbed without the fertilizer component being washed away and has favorable mixing with soil and hardness and high utility value.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composite granular fertilizer comprising ashes of hen droppings and 1 or more types of manure chosen from magnesia manure, natural fertilizer of phosphoric acid and potassium, calcareous fertilizer and silicic acid fertilizer; and    (2) method for producing granular fertilizer, involves adding hydrochloric acid to ashes of hen droppings and carrying out neutralization process.
NOVELTY - Preparation of high-efficient liquid fertilizer involves: mixing amino acid powder (%) (40, preferably 30), zinc sulfate (25-35), manganese sulfate (8), boric acid (3), molybdenum acid (3), copper sulfate (1), ferrous sulfate (1), with water (1), putting into corrosion-resistant reaction kettle. The water is common tap water, softened by SG system softening water processor.    USE - For preparation of high-efficient liquid fertilizer (claimed).    ADVANTAGE - The method prepares high-efficient liquid fertilizer with function of strong stress resistance, improving soil structure and rhizosphere circulating reducing the dosage of phosphorus, relieving environmental pollution and being environment-friendly. The method produce liquid fertilizer with stress resistance and improve soil structure.
NOVELTY - A sludge compost comprises organic-inorganic composite conditioning agent comprising porous ceramic particles and sawdust. Volume ratio of porous ceramic particles and sawdust is 1:2-1:5.    USE - Sludge compost used for sludge high temperature aerobic fermentation treatment.    ADVANTAGE - The sludge compost has high porosity, effectively improves stacked mud structure and oxygen diffusion rate, and is low in cost and good in thermal stability, and can be repeatedly used for sludge high temperature aerobic fermentation treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the sludge compost, comprising mixing porous ceramic particles and sawdust for 20-30 minutes at 10 revolutions/minute. The compost is added into the sludge at amount of 15-20%.
NOVELTY - A biomass carbonizing furnace comprises a combustion chamber with fluid inlet, fire gate, and a combustible gas combustion device; and a carbonization chamber above the combustion chamber. The carbonization chamber has a coke feeding port at its upper part, a coke discharging opening at its bottom, a raw material circulating conveying device at its upper part, and a drying chamber at upper part.    USE - A biomass carbonizing furnace for pyrolyzing the biomass raw material.    ADVANTAGE - The furnace can improve biomass raw material carbonizing speed and can improve biomass raw material for carbonization quality.    DETAILED DESCRIPTION - A biomass carbonizing furnace comprises a combustion chamber with fluid inlet at its one end, and a carbonization chamber above the combustion chamber. The combustion chamber has a fire gate and a combustible gas combustion device. The carbonization chamber has a coke feeding port at its upper part, a coke discharging opening at its bottom, a raw material circulating conveying device at its upper part, and a drying chamber at upper part. The upper part of the drying chamber has a drying chamber material inlet and a water outlet. The drying chamber has a drying chamber material outlet at its bottom, and a drying chamber raw material circulating conveying device. The drying chamber discharging opening is connected with the coking feeding port.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a biomass carbonizing furnace.
NOVELTY - An external heat type biomass pyrolysis device comprises pyrolyzing furnace having 3 layers of concentric steel cylinder. Three concentric cylinder wall of the steel cylinder are divided into 3 functional areas from inside to outside in turn as pyrolysis unit, combustion chamber and ash discharge channel. The pyrolysis unit is cylindrical and comprises bottom pyrolysis chamber outer wall and open tube opening. An outer wall of the pyrolysis chamber has biomass inlet pipe.    USE - An external heat type biomass pyrolysis device.    DETAILED DESCRIPTION - External heat type biomass pyrolysis device comprises pyrolyzing furnace having 3 layers of concentric steel cylinder. Three concentric cylinder wall of the steel cylinder are divided into 3 functional areas from inside to outside in turn as pyrolysis unit, combustion chamber and ash discharge channel. The pyrolysis unit is cylindrical and comprises bottom pyrolysis chamber outer wall and open tube opening. An outer wall of the pyrolysis chamber has biomass inlet pipe. An outer wall of the pyrolysis chamber has drive motor for spiral elevator for lifting material. The motor is on an exterior of the pyrolysis furnace. The combustion chamber surrounding the outer wall of the pyrolysis chamber has sealed burning chamber provided with ignition device. A combustion chamber outer wall has combustion flue gas outlet and fuel inlet pipe.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an external heat type biomass pyrolysis device.
NOVELTY - Device comprises kettle (1), alcohol feeding part (2) and stirrer (3), where the alcohol feeding part enters the kettle through lower part of the kettle and stirrer is wing type axial flow stirring paddle.    USE - The device is useful for performing esterification reaction for producing biodiesel (claimed).    ADVANTAGE - The device enables to improve reaction speed of esterification reaction, reduces energy consumption during reaction even when reactants are allowed to react completely, recycles unreacted alcohol, avoids partial overheating caused during the reaction as kettle enables uniform stirring of reactants, and is easy to maintain the temperature of the reaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows diagrammatic representation of the device.    Kettle (1)    Alcohol feeding part (2)    Stirring part (3)    Heat exchanger (4)
NOVELTY - Methanol composite fuel comprises (in parts weight): methanol (95-98.5) and composite additive (1.5-5) comprising (in parts volume): magnesium naphthenate (15-20), zinc salt of sulfur phosphorus secondary alcohol (5-10), di-tert-butyl-p-cresol (15-30), isoamyl alcohol (30-45) and solvent oil No. 120 (30-40).    USE - The methanol composite fuel is useful as fuel for cooking stove.    ADVANTAGE - The methanol composite fuel is environmentally-friendly, has high thermal efficiency and low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing methanol composite fuel, which involves (a) allowing the composite additive to react in reaction kettle, and (b) organically mixing two different systems of methanol and composite additive using static mixer.
NOVELTY - The pool has computer processor (18) is connected with temperature sensor unit (17) by signal conditioning circuit (14). The computer processor is provided with emitting antenna (19). A current divider (11) is connected with the computer processor through conductive wire (8). The photovoltaic supporting column (7) is set on top solar battery (6). The marsh gas tank (1) is provided with marsh material inlet and outlet (20). The display (23) is connected with computer processor through internal conducting wire. A receiving antenna is arranged above computer processor.    USE - Marsh gas pool.    ADVANTAGE - The temperature of the biogas, biogas residue can be displayed on the display. The temperature change in gas pool can be adjusted so as to increase the yield of the marsh gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas pool. (Drawing includes non-English language text)    Marsh gas tank (1)    Solar battery (6)    Photovoltaic supporting column (7)    Conductive wire (8)    Current divider (11)    Signal conditioning circuit (14)    Temperature sensor unit (17)    Computer processor (18)    Emitting antenna (19)    Marsh material inlet and outlet (20)    Display (23)
NOVELTY - Preparation of fermented silage involves obtaining Pantoea agglomerans, lactic acid bacteria, Saccharomycetes and Bifidobacterium, thawing and separately inoculating to normal culture medium for activating strains, culturing the activated bacterium liquid for amplifying strains, mixing seed strain liquid in ratio 1-4:6-12:6-10:5-8, spraying the mixed working seed strain liquid on surface of greenfeed and naturally fermenting the greenfeed.    USE - The method is useful for preparing fermented silage which is used for promoting immunity in livestock.    ADVANTAGE - The fermented silage can be prepared simply and cost-effectively (1 ton= 1 Yuan). The mixed seed strain liquid effectively decomposes greenfeed and thus improves palatability of greenfeed and enhances bioavailability of plant residual waste, and kills various spoilage microorganisms at aerobic condition and prevents food putrefaction.    DETAILED DESCRIPTION - Method for preparing fermented silage, involves (a) obtaining Pantoea agglomerans, lactic acid bacteria, Saccharomycetes and Bifidobacterium, thawing the microorganisms and inoculating separately to normal culture medium for activating strains for 10-30 hours to obtain an activated bacterium liquid, (b) culturing the activated bacterium liquid in the normal culture liquid medium and amplifying strains for 2-5 times in ratio of 1:10-20 to obtain seed strain liquid, (c) mixing seed strain liquid in a ratio of 1-4:6-12:6-10:5-8 to obtain mixed seed strain liquid containing 150000-20000 million/ml of beneficial bacterium, (d) spraying the mixed seed strain liquid on surface of greenfeed (800-1500 g/ton) and uniformly mixing the above contents, and (e) naturally fermenting the greenfeed at 25-37 degrees C for 65-80 hours at humidity of 50-80% and again fermenting the mixture at 10-25 degrees C for 4-7 days to obtain fermented feed.
NOVELTY - Production of tea seed cake bio-organic fertilizer includes mixing tea seed cake, animal wastes selected from chicken manure, duck feces, pig manure, cow dung, or sheep dung, and microbial agent, which is a composite microbial agent comprising nitrogen-fixing bacteria and cellulose-decomposing bacteria, or effective microorganisms (EM) agent; conducting high-temperature fermentation with oxygenation; turning and humidifying; conducting takes aerobic fermentation; conducting anaerobic fermentation; stopping fermentation; and drying, crushing, pelletizing, and screening the materials.    USE - Production of tea seed cake bio-organic fertilizer (claimed) used for killing insects.    ADVANTAGE - The tea seed cake bio-organic fertilizer is multifunctional, efficient, and safe; and has low cost.    DETAILED DESCRIPTION - Production of tea seed cake bio-organic fertilizer comprises:    (A) providing (pts.wt.) tea seed cake, which is in powder form (2-5), animal wastes (3-7), and microbial agent (0.2-0.4), where animal wastes are selected from chicken manure, duck feces, pig manure, cow dung, or sheep dung, and microbial agent is a composite microbial agent comprising nitrogen-fixing bacteria and cellulose-decomposing bacteria, or EM agent; mixing the tea seed cake, animal wastes, and microbial agent; conducting high-temperature fermentation with oxygenation in fermentation tank; turning and humidifying for 1-3 times; controlling tea seed cake and animal wastes water content at 50-60%; conducting takes aerobic fermentation until the temperature of material is 40-50 degrees C; conducting anaerobic fermentation at 25 degrees C; and stopping fermentation when there is no more foul odor; and    (B) drying, crushing, pelletizing, and screening the materials; and obtaining tea seed cake bio-organic fertilizer.    An INDEPENDENT CLAIM is included for tea seed cake bio-organic fertilizer.
NOVELTY - Flower culture medium is made of cow manure and biogas residues and sawdust. The volume ratio of raw materials, such as cow manure and biogas residues and sawdust is 1:1.    USE - The flower culture medium is for azalea flower, which favors slightly acidic soil (claimed). It is used for promoting the growth of azalea flower.    ADVANTAGE - The flower culture medium has high nutrient content and excellent physicochemical properties; improves the biological characteristics of flower; effectively utilizes the methane fermentation residue resources; protects the natural grass carbon resource; and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of flower culture medium comprising providing raw material, which is methane fermentation residue or cow manure and biogas residues of gas generation for more than 1 year and sawdust, which is doped sawdust made of larch and poplar; taking cow manure and biogas residues and sawdust; drying in air; crushing; mixing at 1:1 volume ratio; diluting phosphoric acid reagent (analytically pure, 85% concentration) for 200-500 times by volume to obtain phosphoric acid solution; and spraying at 15-37.5 L/m3 to obtain flower culture medium having pH of 4.5-5.5, nutrient i.e. nitrogen-phosphorus-potassium content of greater than or equal to 35 g/kg, electrical conductivity of 1.1-1.5 mS/cm, and porosity of 80-85%.
NOVELTY - A biological compound fertilizer of rabbit dung humic acid, comprises (wt.%): rabbit dung (40), weathered coal (12), bone powder (25), triple superphosphate (13) and potassium humate (10).    USE - As biological compound fertilizer of rabbit dung humic acid (claimed).    ADVANTAGE - The method improves the soil activity, improves the alkali replacement of the soil and accelerating organic soil to decompose into the humic acid, improves the physical and chemical properties of the soil, promotes plants to absorb nutrients and makes the plants grow vigorously, reinforces the stress resistance and disease resistance of crops, increases the output of the crops and improves the product quality to achieve high output and excellent quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the biological compound fertilizer of rabbit dung humic acid involving: mixing rabbit dung (40 wt.%), weathered coal (12 wt.%), bone powder (25 wt.%), spraying water and blending to keep the moisture at 45-50%; accumulating the mixture in a fermenting tank to ferment for 12-18 days, overturning the pile in time when the fermentation temperature is raised to 50-60 degrees C so as to prevent overhigh temperature; after finishing the fermentation, pouring the fermented mixture from the fermentation tank to dry; and then adding triple superphosphate (13 wt.%) and potassium humate (10 wt.%), breaking by a crusher; granulating, controlling the inlet temperature of a dryer at 130-140 degrees C and the outlet temperature at 50-60 degrees C to carry out a drying process; screening to obtain the finished product.
NOVELTY - A potato residue fuel rod is produced by putting polyacrylamide in potato residue, stirring for 3-10 minutes, and extruding and dewatering the potato residue by a belt type filter press to obtain potato residue filter cake having water content of 65-80%.    USE - Method for the production of potato residue fuel rod (claimed).    ADVANTAGE - The method is able to re-use waste, reduces environment pollution caused by discharge of potato residue, and reduces production cost.    DETAILED DESCRIPTION - Production of potato residue fuel rod comprises:    (A) putting polyacrylamide in potato residue, stirring for 3-10 minutes, and extruding and dewatering the potato residue by a belt type filter press to obtain potato residue filter cake having water content of 65-80%;    (B) frying the potato residue filter cake in air, stacking potato residue filter cake for 0.2-0.8 m, turning the stack for 1-5 times/day in drying for 6-16 days, and forming first potato residue having the water content of 50-60%;    (C) mixing the first potato residue with potato residue filter cake at mass ratio 0.3-2:1, and then drying in air until having the first potato residue with water content of 50-60%, drying the first potato residue by a roller drying machine, having the temperature of hot wind at 600-800 degrees C to obtain dry potato residue with water content of 12-15%, mixing the dry potato residue with the first potato residue to obtain the mixed potato residue having water content of 17-20%; and    (D) crushing the mixed potato residue having the grain size of the mixed potato residue below 2 cm, putting the crushed mixed potato residue in a spiral extruding machine for extruding and molding at 200-350 degrees C and at pressure of 30-50 MPa, and obtaining the potato residue fuel rod, where concentration of polyacrylamide in potato residue is 0.5-20 mg/L.
NOVELTY - The organic fertilizer comprises wooden crude fiber (40-80 parts by weight (pbw)), straw fiber (60-90 pbw), rag (10-30 pbw), waste cotton wool (10-30 pbw), animal skeleton (10-40 pbw), fur (10-40 pbw), aquatic shell (10-30 pbw), rape seed cake (30-60 pbw), cottonseed cake (10-30 pbw), gendarmerie seed cake (30-60 pbw), and flavored solar synthesis agent (25-50 kg). The fertilizer is prepared by sterilizing the raw materials at high temperature and frying the skeleton to become old yellow, stewing and calcining the fur to become colorless, and baking the shell to become white.    USE - Used as an organic fertilizer. No biological data given.    ADVANTAGE - The fertilizer sterilizes the organic matters in an environmentally friendly manner.    DETAILED DESCRIPTION - The organic fertilizer comprises wooden crude fiber (40-80 parts by weight (pbw)), straw fiber (60-90 pbw), rag (10-30 pbw), waste cotton wool (10-30 pbw), animal skeleton (10-40 pbw), fur (10-40 pbw), aquatic shell (10-30 pbw), rape seed cake (30-60 pbw), cottonseed cake (10-30 pbw), gendarmerie seed cake (30-60 pbw), and flavored solar synthesis agent (25-50 kg). The fertilizer is prepared by sterilizing the raw materials at high temperature and frying the skeleton to become old yellow, stewing and calcining the fur to become colorless, baking the shell to become white, crushing the raw materials to become powder, adding flavored solar synthesis agent into the powder and mixing evenly.
NOVELTY - Acaricidal composition comprises etoxazole, abamectin, azocyclotin, propargite, clofentezine or pyridaben.    USE - The acaricidal composition is useful for preventing and treating harmful mite of farmlands and fruit trees.    ADVANTAGE - The composition has synergistic effect; increases the prevention effect; reduces the dosage of the active component; delays the harmful insect's resistance to the drug; and is environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an acaricide, where the active ingredient is composed of acaricidal composition.
NOVELTY - A fermentation cabin comprises a base, a cabin body on the base, and a ventilating device in the cabin. The cabin is of tower shape. Middle part of cabin body is provided with a ventilating tube which penetrates whole cabin body and extends out of cabin. Top part of cabin body is provided with a top cover. The ventilating tube is on lower part of top cover and provided with a baffle. The base is a three-face frame jointed by cross-rails at intervals. The three-face frame is jointed with a fence with brick structure. The base has hollow structure and provided with a collection port.    USE - Fermentation cabin used for fermenting decomposed or green broomcorn, corn, straw, wheat straw, rape, tobacco, and bean into feed or organic fertilizer.    ADVANTAGE - The fermentation cabin has simple structure and easy to operate, can save labor and provide in situ conversion of crop by-products, is environment-friendly, and increases agricultural product.
NOVELTY - Preparing fuel ethanol from fermentable sugar in fresh straw juice, comprises (i) collecting fresh corn straws, juicing the straws and performing solid-liquid separation to obtain straw juice and straw dregs; (ii) concentrating the straw juice until the total content of the fermentable sugar is 20-30%; (iii) adjusting the concentrated straw juice until reaching a suitable state for fermentation; and (iv) adding into ethanol fermentation strains, fermenting to obtain fermented mash, and separating the fermented mash for recovering ethanol.    USE - The method is useful for preparing fuel ethanol from fermentable sugar in fresh straw juice.    ADVANTAGE - The method has high production efficiency, and is suitable for large-scale industrial production.
NOVELTY - A fuel comprises (pts. wt.) coal powder (90-110), clay (60-80), straw (25-35 kg), lacquer putty powder (calcium oxide) (1-1.5), sodium nitrate (1-1.5), sodium hydroxide (0.2-0.5), magnesium oxide (2-3), smoke suppressor (1.3-1.6), starch (0.1-0.5), sodium (0.4-0.6), sodium silicate (0.4-0.6), and carbon powder (8-10).    USE - A fuel.    ADVANTAGE - The fuel is energy saving and capable of combustion duration of 1.5-2 hours without peculiar smell, produces white combustion smoke, is cheap and environment-friendly, has combustion heat value that can reach more than 4000 kcal thus making the fuel applicable to industrial and civil application, and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fuel comprising mixing the raw materials, setting aside for 5-8 days, and recycling.