NOVELTY - Manufacture of sludge-biomass mixed fuel comprising one or more liquid biomass among hydrophilic or hydrophobic liquid biomass involves mixing sewage sludge and hydrophilic or hydrophobic liquid biomass to obtain mixture, adding binder to the mixture to obtain mixed fuel, drying the mixed fuel and carbonizing when evaporation temperature of liquid biomass included in mixed fuel is 105 degrees C or more.    USE - Manufacture of sludge-biomass mixed fuel (claimed).    ADVANTAGE - The sludge-biomass mixed fuel has improved moisture readsorption property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge-biomass mixed fuel.
NOVELTY - The container (1) has a bottom unit (2) that is adjoined with the floor, and upstanding wall (3). A cover film is provided for covering the substance in the container main potion. A cover (4) is connected to an upper end portion of the upright wall.    USE - Container for containing liquid substance such as manure and gas-producing substance e.g. crap.    ADVANTAGE - The cover is simply connected to the container even when the container is already filled with the substance, as the cover film is provided for covering the substance in the container main potion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of applying cover film in container for containing substance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the container.    Container (1)    Bottom (2)    Upstanding wall (3)    Cover (4)    Bolt (5)
NOVELTY - Composting liquid organic waste comprises removing large foreign substances contained from the liquid organic waste, crushing the waste, processing the waste with calcium-containing mineral, heating the organic waste, adding dissolved oxygen having concentration of 2-4 mg/l to the organic waste, introducing the organic waste to a high temperature aerobic fermentor containing fermentation liquid, primary fermenting the mixture at a temperature of 60-80 degrees C, secondary fermenting the mixture in a culture anaerobic fermentor at a temperature of 20-40 degrees C, and aging the fermented waste.    USE - The method is useful for composting liquid organic waste such as food waste, livestock manure, waste molasses, alcohol waste, slaughterhouse waste, waste discharged from food processing plants, wastewater treatment plants, agriculture and leather manufacturing process, and waste obtained from processing of marine products (all claimed) to prepare liquid fertilizer.    ADVANTAGE - The method is capable of composting the liquid organic waste in an economical and energy-efficient manner.    DETAILED DESCRIPTION - Composting liquid organic waste comprises removing large foreign substances contained from the liquid organic waste, crushing the waste, processing the waste with calcium-containing mineral, heating the organic waste at 50-60 degrees C, adding dissolved oxygen having concentration of 2-4 mg/l to the organic waste at a pressure of 2-4 atm, introducing the organic waste to a high temperature aerobic fermentor containing fermentation liquid, primary fermenting the mixture at a temperature of 60-80 degrees C, secondary fermenting the mixture in a culture anaerobic fermentor at a temperature of 20-40 degrees C, and aging the fermented waste.
NOVELTY - Process of converting lignocellulosic carbohydrates to diesel fuel blendstock, involves transesterifying lignocellulosic carbohydrate-derived levulinate solution containing levulinate molecules with alcohol solution comprising alcohol molecules including hydroxyl group(s) in presence of a transesterification catalyst under effective conditions to combine at least some of the levulinate molecules with some of the alcohol molecules to form larger molecules that are diesel range molecules suitable for diesel fuel blendstock.    USE - Process of converting lignocellulosic carbohydrates to diesel fuel blendstock for gasoline, jet fuel and diesel fuel for vehicles.    ADVANTAGE - Diesel fuel blendstock produced from lignocellulosic carbohydrates has excellent physicochemical characteristics.
NOVELTY - Making (P1) ethanol from jackfruit seeds through enzymatis process involves: a) making glucose from jackfruit seeds using enzyme; b) hydrolysis using alpha -amylase; c) saccharification using glucoamylase; d) fermentation of glucose by yeast and nutrients sacharomyses sereviceae urea, and nitrogen-phosphorus-potassium to produce ethanol.    USE - For making ethanol from jackfruit seeds through enzymatic process (claimed), which is used as aperitif, versatile solvent required in the pharmaceutical and cosmetic industries and fuel.    ADVANTAGE - The process makes ethanol from jackfruit seeds through enzymatic process with short time; and produces 9.70-19.43% (preferably 11.60-16.37%) levels of glucose.
NOVELTY - Mass culturing Lecane rotifer, comprises maintaining culture in plates (1), in a liquid medium and fed with artificial nourishment.    USE - The method is useful for mass culturing Lecane rotifer, which is useful in activated sludge bulking control in wastewater treatment plants applied out of the activated sludge bioreactors (all claimed), and reducing the growth of filamentous bacteria causing the problem of activated sludge bulking in wastewater treatment plants.    ADVANTAGE - The method provides an intensive, quick and cheap mass culture of Lecane rotifers.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of method of mass culturing Lecane rotifer.    Plates (1)    Ribbed bottom (2)    Flat-bottom base (3)    Cover (4)    Vent. (5)
NOVELTY - Liquid manure comprises quercetin obtained from onion.    USE - The liquid manure is useful for cultivating rice plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the manure, which involves mixing onion and sugar, and fermenting mixture by inoculating microbial strains.
NOVELTY - The system collects and gathers (S10) deceased fuel. The heavy material such as stone and light material are separated (S30) from the deceased fuel. The separated small material is separated (S40) from the deceased type fuel based on difference of the weight. The dust generated in the multiple compartments during processing is collected (S70). The dust sampled in the cannonade population system is mixed (S80) with the stored solid fuel. The solid fuel mixed with dust is progressed (S90) to the boiler.    USE - System for classifying and supplying biomass to power-station boiler.    ADVANTAGE - The purity of the raw material is raised according to the weight and volume. The raw material is classified into the solid fuel of various kinds and property. Each classified solid fuel is stored in each compartment, and the appropriate solid fuel is selected when necessary and is injected in the boiler of the heat power plant.    DETAILED DESCRIPTION - The foreign substance such as iron is removed (S50) with the magnetic force. The solid fuel classified based on the specific weight and volume is stored (S60) in rectangular silo.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of classifying and supplying biomass to power-station boiler. (Drawing includes non-English language text)    Step for collecting and gathering deceased fuel (S10)    Step for separating heavy material and light material from deceased fuel (S30)    Step for separating small material from deceased type fuel (S40)    Step for removing foreign substance with magnetic force (S50)    Step for storing solid fuel classified based on the specific weight and volume in rectangular silo (S60)    Step for collecting dust generated in the multiple compartments during processing (S70)    Step for mixing dust sampled in cannonade population system with stored solid fuel (S80)    Step for progressing solid fuel mixed with dust to boiler (S90)
NOVELTY - A recombinant yeast capable of producing ethanol from xylose, is new. The recombinant yeast is obtained by introducing gene encoding xylose reductase (XR) derived from Spathaspora passalidarum, xylitol dehydrogenase (XDH), and xylulokinase (XK).    USE - The recombinant yeast is useful for producing ethanol from xylose (claimed), which is used for producing biofuel.    ADVANTAGE - The recombinant yeast ensures high productivity of ethanol from xylose.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing ethanol from xylose, which involves (a) culturing the recombinant yeast in a medium comprising xylose to obtain ethanol, and (b) recovering ethanol from the culture medium.
NOVELTY - Preparing substituted alkyl phenols, comprises (i) treating a substituted amino compound with an acid to form an amine salt, (ii) treating the amine salt with a diazotizing agent to form a diazonium salt, (iii) hydrolyzing the diazonium salt with a solvent and an acid to obtain an effluent phase and an organic phase comprising substituted alkyl phenol, and (iv) recycling the effluent phase to all or any of (i)-(iii) steps.    USE - The process is useful for preparing substituted alkyl phenols (claimed), preferably hydroxy-xylenes such as 2,4-xylenol, which are useful as intermediate products for production of agrochemical, dyes and medicines.    ADVANTAGE - The process is capable of economically and safely preparing substituted alkyl phenols with reduced consumption of chemical components and with high purity of 99.5% and yield of 87.5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reducing the chemical components used in a process for preparing substituted alkyl phenols, comprising recycling an effluent phase obtained in the process to various steps of the process for preparing substituted alkyl phenols.
NOVELTY - Obtaining fertilizer involves mixing meat flesh powder category of 2 or 3 with water and then fermentation is carried out to obtain a product. The product is agitated, decanted and centrifuged to obtain a centrifuged product. The centrifuged product is filtered and packaged into a bottle.    USE - Method for obtaining fertilizer (claimed) used for agricultural crops.    ADVANTAGE - The method enables to obtain fertilizer that is free from impurities.
NOVELTY - The apparatus has flowerpot module which is installed at upper portion of base structure (100). A drainage district portion is formed in flowerpot module whose inside is provided with bamboo charcoal and plant. A vegetation groove is pitted from upper portion to lower portion to form projection portion. A water beam (20) for controlling water level is installed at upper portion of river (10) to maintain fixed water level. An equation groove is settled in projection portion.    USE - Apparatus for purifying water such as contaminated water of forest, farmland, domestic wastewater, industry wastewater, livestock wastewater, livestock excretion, factory water and agricultural water.    ADVANTAGE - Since the green algae is not generated when the water passes the bamboo charcoal and falls down, the dissolved oxygen is increased and the clean state of the water is maintained. Since the apparatus is provided with the separated type container portion, various kinds of plant are implanted easily, and the administration of the plants is facilitated easily. Since multiple purifiers are arranged as the staircase type, the purifying efficiency of the apparatus is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the apparatus for purifying water.    River (10)    Water beam (20)    Base structure (100)    Waterway portion (300)    Transfer pipe (500)
NOVELTY - Preparation of hydrocortisone semi-succinate, involves: dissolving hydrocortisone and succinic anhydride in organic solvent, adding catalyst, stirring for 2-8 hours, distilling decompression, removing solvent, adding diluted hydrochloric acid, obtaining solid, adding active carbon, heating to 40-45 degrees C, stirring for 20-30 minutes, pouring low filtered liquid into distilled water, separating out crystal refrigerator, crystallizing, washing, drying to obtain white solid, the yield is more than 95%.    USE - For preparation of hydrocortisone semi-succinate (claimed).    ADVANTAGE - The reaction process controls temperature and time, greatly increase the yield of product; is easy to obtain, the operation is simple, the reaction time is short, the environment pollution is small, reduce the cost for a solvent recovery.    DETAILED DESCRIPTION - Preparation of hydrocortisone semi-succinate, involves: dissolving hydrocortisone and succinic anhydride in the organic solvent, adding catalyst, stirring for 2-8 hours, distilling decompression, removing solvent, adding diluted hydrochloric acid, stirring to separate out crystal, filtering, washing with neutral, drying, obtaining solid rear, where the obtained solid into solution in organic solvent, adding active carbon, heating to 40-45 degrees C, stirring for 20-30 minutes, pouring low filtered liquid into distilled water, separating out crystal refrigerator, crystallizing completely filtering, washing, oven drying to obtain white solid, and the yield is more than 95%.
NOVELTY - The method involves adding a wet portion (111) of a wet fermentation process with a dry fermentation process. A stream of a dry substrate (101) is received in a dry digester (110). The dry fermentation process is carried out in the dry digester to form a dry fermented composition frame (112) and a biogas frame (113). The dry fermented composition frame is fixed with a separator (115). A solid fraction part (116) and a liquid fraction part (117) of the dry fermented composition frame are separated by the separator. A residual flow of a wet substrate (102) is provided with a wet digester (105).    USE - Method for combining dry and wet fermentation processes for a biomass for use in agro-food industry.    ADVANTAGE - The method enables extracting energy from the biogas for a power generation with a livestock farm scale, maintaining pump ability of residual flow, remaining an important ingredient for the installation, achieving different types of solid residues from the agro-food industry and simply and effectively capturing emission of carbon dioxide gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for combining dry and wet fermentation process for a biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a device for combining dry and wet fermentation process for a biomass.    Dry substrate (101)    Wet substrate (102)    Wet digester (105)    Dry digester (110)    Wet portion (111)    Dry fermented composition frame (112)    Biogas frame (113)    Separator (115)    Solid fraction part (116)    Liquid fraction part (117)
NOVELTY - The film comprises a bridge structured-heat conversion polybenzoxazoleimide copolymer material mixed with aromatic cyclic group material, where the aromatic cyclic group material is heterocyclic group material, arylene group material or substituted/unsubstituted phenylene group material. The arylene group material is oxygen, sulfur, carbon monoxide, sulfur dioxide, dimethyl silane, carbon fluoride or trifluoromethyl material. Density of the bridge structured-heat conversion polybenzoxazoleimide copolymer material is 1.36-1.43 g/cubic cm.    USE - Flue gas e.g. carbon dioxide or methane, separation film.    ADVANTAGE - The bridge structured-heat conversion polybenzoxazoleimide copolymer material is mixed with the aromatic cyclic group material so as to improve selectivity, gas transmittance property and gas separation performance of the film.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a flue gas separation film manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating relationship between carbon dioxide permeability and carbon dioxide/methane selectivity of a flue gas separation film.
NOVELTY - Manufacture of biomass-and-plastic-containing solid fuel (10) involves drying biomass (1), controlling humidity of dried biomass (1a) such that moisture content is 10-40%, mixing humidity-controlled biomass (1b) with plastic (7), curing and compression-molding.    USE - Manufacture of biomass-and-plastic-containing solid fuel (claimed).    ADVANTAGE - The method enables manufacture of dry biomass-and-plastic-containing solid fuel having excellent storage stability, without using binder. Dispersion of unmolded biomass from the solid fuel is prevented, and stable strength and shape is maintained. Moisture content does not influence the emitted-heat amount and the solid fuel can be made into coal alternative fuel which can be stored for a long period of time. When the humidity-controlled mixture is compression-molded, dispersion of dry biomass is prevented. Hence, biomass is prevented from being dispersed in the manufacturing step or product transportation line.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of biomass-and-plastic-containing solid fuel, which comprises drying machine (2) which dries biomass, humidity control machine (4) for controlling the humidity of the dried biomass, mixing apparatus (6) for mixing humidity-controlled biomass and plastic, and molding machine (9) for compression-molding the mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of manufacturing method and apparatus of biomass-and-plastic-containing solid fuel.    Biomass (1)    Dried biomass (1a)    Humidity-controlled biomass (1b)    Drying machine (2)    Dry raw material storage tank (3)    Humidity control machine (4)    Water (5)    Mixing apparatus (6)    Plastic (7)    Molding machine (9)    Solid fuel (10)
NOVELTY - Removing gaseous organic sulfide contaminants from gaseous mixtures, comprises dissolving the organic sulfide contaminants in a solvent, and reacting the dissolved sulfides with media comprising an acid-based catalyst to permit cleavage of the sulfur atom from the organic sulfide molecule, such that the cleaved sulfur atom can be further reduced electrochemically to elemental sulfur or alkali metal polysulfides.    USE - The method is useful for: removing gaseous organic sulfide contaminants from gaseous mixtures, effluent and discharge gas flows, preferably bio-gas and natural gas for conversion to pipe-line quality natural gas or compressed natural gas (CNG), which is useful for enhancing oil recovery in oil wells and providing raw materials for oil refineries or petrochemical plants, and as sources of energy; and removing the higher value natural gas liquids (NGLs) from the lower value natural gas (mainly methane).    ADVANTAGE - The method is capable of removing gaseous organic sulfide contaminants from gaseous mixtures with less consumption of energy and raw materials in a cost effective manner.
NOVELTY - Method for producing an ortho-hydroxylated phenylpropanoid, involves (a) culturing microbe comprising 4-hydroxyphenylacetate 3-hydroxylase (HpaBC) activity in presence of phenylpropanoid substrate under conditions suitable to ortho-hydroxylate the phenylpropanoid substrate to result in ortho-hydroxylated phenylpropanoid, and (b) isolating the ortho-hydroxylated phenylpropanoid from the microbe, culture medium, or their combinations.    USE - The method is useful for producing ortho-hydroxylated phenylpropanoid useful in pharmaceutical applications.    ADVANTAGE - The method consumes minimal energy, is environmentally-friendly, and produces ortho-hydroxylated phenylpropanoid having excellent solubility, stability and biological activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for genetically engineered microbe, which comprises more HpaBC activity than the control microbe.
NOVELTY - The device has a two-section reactor (1) whose middle part is fixed with a net and connected with a catalyst regeneration module (11) through a first stop valve (12). An end of a biological oil collector (6) is connected with the two-section reactor through a filter (2) and another end is connected with a second stop valve (5). The biological oil collector is fixed with a vacuum pump (9) through a voltage-stabilizing cylinder (8). The two-section reactor is connected with a temperature control module (10). A NTP generator (17) is connected with a distribution pneuma (16).    USE - Biomass pyrolysis vapor anti-cracking catalytic online bio-oil preparing device.    ADVANTAGE - The device can separate a catalyst from biomass so as to effectively avoid direct mixing of the catalyst and biomass and separate defects. The device obtains refining biological oil by low-temperature catalytic reaction of catalyst regeneration module so as to effectively avoid conventional catalyst regeneration defects, and ensure utilization rate and efficiency of bio-oil preparation.    DETAILED DESCRIPTION - The NTP generator is a medium barrier discharge device. An INDEPENDENT CLAIM is also included for a biomass pyrolysis vapor anti-cracking catalytic online bio-oil preparing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass pyrolysis vapor anti-cracking catalytic online bio-oil preparing device. '(Drawing includes non-English language text)'    Two-section reactor (1)    Filter (2)    Second stop valve (5)    Biological oil collector (6)    Voltage-stabilizing cylinder (8)    Vacuum pump (9)    Temperature control module (10)    Catalyst regeneration module (11)    First stop valve (12)    Distribution pneuma (16)    NTP generator (17)
NOVELTY - A one upright fermenting groove structure, one a fermentation groove, one stir device, one driving device, two air blower, wherein the stir device has one vertical to hollow shape is set on the shaft pole of the groove, and a connected number on the horizontal-shaped stir pole of the shaft pole, the stir pole number set with discharge hole, the driving device is used for driving the shaft link pole, the air blower connected with the air supply pipeline of the shaft pole upper, lower two end, wherein said air supply pipeline has one heater. Inner fermentation groove into the organic waste, for example by drive device drives the stir pole, and the inner air blower by air to produce stir device and discharge hole by a, and at the same time a stir and hot air action, so as to make the organic waste fully uniform into organic matter (fertilizer).
NOVELTY - This utility new type claims a one waste incineration fly ash processing system, which is used for solving the technology in a dioxin substance waste incineration fly ash and inner pollution of heavy metal substance of. The system comprise: waste incineration fly ash collecting unit, used for collecting garbage burning produce a rear fly ash, fly ash, powder coal pressurizing conveying unit, a fly ash collecting unit is a, for the fly ash and coal powder conveying tube sent of powder coal taking mix a mixture with the powder coal conveying tube and waste, and the mixture is conveyed to the next process, fly ash, pulverized coal gasification melting unit with the fly ash, powder coal pressurizing conveying unit is a, fly ash, pulverized coal gasification melting unit include: gasification furnace, quenching device. This utility new type using a technology solution, completely eliminating waste incineration fly ash in a dioxin discharge and fly pollution of heavy metal in a dust, a and zero.
NOVELTY - This utility new type on claims the esterification reaction liquid in a one biological diesel oil production and a layered device, a mixer is set with liquid entrance esterification, esterification liquid first exit, second esterification liquid exit, and methanol exit exit, a device bottom is tapered, conical bottom part set with a heating coil, said acid alcohol exit is located at the bottom layer, a first conductivity meter is a exit, a second conical bottom of the layering device of conductivity meter and the first conductivity meter, a one end acid alcohol exit valve of the other end a connecting liquid tank and acid alcohol esterification tank, the second esterification liquid exit the esterification liquid entrance, first esterification liquid exit on the second esterification liquid exit, the exit is located at the top of methanol layer. This utility new type greatly increase the speed of esterification liquid layer, but also can make the efficiency of acidification reaction kettle increase to ensure the layering effect, but also has the second esterification of effect, and the continuous production is possible.
NOVELTY - This utility new type claims a high effect recovery using one esterification process system of methanol, belonging to the biology diesel oil preparation technology field. This utility new type comprise first middle tank, esterification reaction mechanism, methanol recovery mechanism, a sedimentation tank, a centrifugal machine and second middle tank, esterification reaction mechanism include reaction kettle, reaction kettle and the methanol recovery mechanism through pipeline composed of one circulation loop, a part of the reaction kettle is provided with a steam exit methanol from a methanol steam exit out of pipeline is divided into two branches, two branches of one in the upper branch in turn connected in series with pneuma liquid separator and vacuum pump, said vacuum pump exit through pipeline and the methanol distillation tower, the other branch in one branch of two directly connected with the methanol distillation column. This utility new type is methanol in reaction kettle entering into methanol distillation column supply 2 a path, methanol steam directly entering into a distillation tower a distillation, the recovery process energy consumption is greatly reduced, for the enterprise saves the production cost.
NOVELTY - This utility new type claims a biological diesel oil of one esterification process system, belonging to the preparation technology field of biological diesel oil. This utility new type include mix type reaction kettle, colloid mill, mixing kettle, a centrifuge and middle tank, a mix of a bottom type reaction kettle connect with one three-way valve, the three-way valve of one connected feed inlet of the nano colloid mill is connected with three-way valve of the other connected with the first conveying pump connected with the discharge hole of the nano colloid mill through one feeding pipeline and mix type reaction kettle of; the mixing kettle through delivery pump and the first mix type reaction kettle is connected at the bottom of the blending kettle through centrifuge with the middle tank, a middle tank through a third conveying pump and the subsequent device. This utility new type in the esterification reaction process material fully mix, which increases the yield of methyl ester or ethyl ester, the esterification time is greatly shortened, and the production efficiency is high.
NOVELTY - This new type utility claims one a biological diesel oil production system, belonging to the biology diesel oil preparation technology field. This utility new type oil storage mechanism include oil storage tank and a first conveying pump, preprocessing mechanism comprise first sedimentation tank, filter, dehydration mechanism and first middle circulation tank, a first sedimentation tank through second conveying pump and the filter, the filter and the circulation dehydrating mechanism, dehydrating mechanism and the first middle circulation tank, esterification mechanism comprise mix type reaction kettle, kettle, centrifugal machine and second middle tank, mix type reaction kettle through the sixth conveying pump and blending kettle is connected, the bottom of kettle through centrifuge and the second middle tank. This utility new type raw material oil of a select range is wide, esterification effect is good, the production process continuity is strong, and the biological diesel oil production efficiency high.
NOVELTY - A bis-triazole conjugated disaccharide derivative is new.    USE - As antibacterial and antiviral agent.    ADVANTAGE - The compound (I) has good stability; and has good antibacterial and antiviral activity. The preparation method of the compound (I) involves raw material which is easy to obtain; has mild reaction condition; and is economical and environment-friendly.    DETAILED DESCRIPTION - A bis-triazole conjugated disaccharide derivative of formula (I) is new.    P'=hydroxy or amino protecting group or H atom;    R=H, methyl or ethyl;    n=2-4.    An INDEPENDENT CLAIM is included for preparation of the compound (I).
NOVELTY - 4-Substituted-1-chloro-2-(4-fluorobenzyl) benzene compound (V), is new.    USE - For preparing type II diabetes drug (claimed).    ADVANTAGE - The compound (V) is prepared by using inexpensive raw materials and reagents with low cost, simple and safe operation, and good yield; is environment friendly; has good economic effect; and is suitable for industrial production.    DETAILED DESCRIPTION - 4-Substituted-1-chloro-2-(4-fluorobenzyl) benzene compound of formula (V), is new.X=bromo or iodo.    INDEPENDENT CLAIMS are included for the following:    (1) preparing the compound (V);    (2) preparing type II diabetes drug (i.e. empagliflozin) of formula (I) using the compound (V) as a key intermediate, involving (i) reacting the compound (V) with (S)-tetrahydro-furan-3-ol (VII) in acid-catalyst and 1-3C alcohol solution through addition of alkali metal reagent to give compound of formula (IV); (ii) performing reduction of the compound (IV) through the addition of reducing agent and an acidic additive to give compound of formula (III); (iii) reacting the compound (III) with VIII under the basic condition to give compound of formula (II); and (iv) deprotecting the compound (II) using metal catalyst to give the compound (I), or deprotecting the compound (II) under the action of an acid to give the compound (I).    R1=1-6C silyl protecting group (preferably trimethylsilyl, triethylsilyl, triisopropyl silicon or tert-butyl butyldimethylsilyl) or benzyl-based protecting group (preferably trityl, benzyl, 4-methoxybenzyl, 4-methylbenzyl, 4-nitrobenzyl, 2,4-dimethoxy-benzyl, benzyloxycarbonyl, 4-methoxy-benzyloxycarbonyl group, or 4-methyl-benzyloxycarbonyl group);    R2=1-3C alkyl (preferably methyl, ethyl, n-propyl, or isopropyl).
NOVELTY - An improving agent comprises plant ash:calcium-magnesium-phosphate fertilizer:quicklime:zeolite:hydroxyapatite:organic fertilizer with weight ratio of 0.3-1.1:0.1-1.2:0.4-2.1:0.1-0.6:0.008-0.06:0.4-1.2.    USE - An improving agent for composite heavy metal contaminated soil remediation (claimed).    ADVANTAGE - Improving agent is environment-friendly and low-cost and has high stability, improves contaminated soil fertility, and good remediation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composite heavy metal contaminated soil remediation which involves adding improving agent to composite heavy metal contaminated soil.
NOVELTY - Preparation of biodiesel oil from flowering plum seed involves pressing the seeds of flowering plum to get seed oil; dissolving KOH catalyst in methanol and adding the seed oil for trans esterification reaction at 50-70 degrees C and quickly stirring; separating upper methyl ester layer after completion of the reaction, washing with warm water until neutral; adding anhydrous Na2SO4, drying and filtering to get pale yellow, clear and transparent biodiesel oil.    USE - For preparation of biodiesel oil from flowering plum seed.    ADVANTAGE - The method provides large-scale production, and provides new woody biomass resources that can ease biodiesel production from raw material while optimizing its processes, making it the lowest cost. The production process is simple, low cost, and provides high product purity.
NOVELTY - Method for producing biogas, involves (a) crushing straws of 2-6 mm and drying the crushed straws, (b) adding 0.5-1% dextrose, 0.5-0.9% ammonium sulfate, 0.02-0.06% calcium carbonate and 0.5-1% potassium hydrogen phosphate to the dried straws, and adjusting pH of the obtained product to 6-8 using 0.01-0.03% alkaline solution (sodium hydroxide or potassium hydroxide), and (c) adding 30-50%activated sludge to the obtained product, fermenting at 35-55 degrees C, and collecting biogas which is generated from the fermented material.    USE - The method is useful for producing biogas (claimed).    ADVANTAGE - The method is rapid, cost-effective and environmentally-friendly, as no wastewater is discharged after fermentation.
NOVELTY - This new type utility claims one a water electrolytic water, include closeness kettle body and arranged on a kettle body inner closeness of pneuma water separating plate, a water separating plate pneuma of kettle body is divided the inner cavity of water storage cavity is gas storage chamber and the air chamber, air inlet and air outlet a closeness kettle body is provided with a gas storage chamber inside of, and water inlet and water outlet with the water inside a cavity, said outlet is located a closeness kettle body top of said upper air outlet mounting with pneuma water separator, a pneuma water separator the gas storage inner cavity, a pneuma a water separating plate is provided with a water return the inner air cavity water leakage hole of water storage cavity. This utility new type has simple structure, reasonable design, low investment cost and low processing and use operation is simple, use effect is good, not only is an electrolytic water supply device, but also for water electrolysis a produce of hydrogen and oxygen process.
NOVELTY - Bioorganic fertilizer comprises 15-30 pts. wt. human or animal excrement, 15-30 pts. wt. crop straw, 10-20 pts. wt. bran, 5-10 pts. wt. sawdust, 5-15 pts. wt. plant stem, 1-5 pts. wt. chitin, 1-5 pts. wt. enzyme, and 1-5 pts. wt. fermentation agent.    USE - As bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer is environmentally-friendly, improves soil nutrition and fertility, and activity of microorganism in soil.
NOVELTY - Bioorganic fertilizer comprises 6-26 wt.% filter mud obtained from sugar refinery, 55-75 wt.% bagasse, and 10-30 wt.% alcohol concentrate.    USE - The bioorganic fertilizer is useful for crops.    ADVANTAGE - The bioorganic fertilizer is prepared by simple, easy and cost-effective method, and uses simple device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned bioorganic fertilizer, which involves (a) mixing the above-mentioned components and stacking the mixture, (b) filtering the stacked mixture, (c) fermenting the mixture using Bifidobacterium, lactic acid bacterium, Bacillus, yeast, actinomycetes or acetic acid bacteria, (d) fermenting for 15-25 days, piling up the fermented product at 60 degrees C for 5-6 days and maintaining moisture of the product at 40-45%, (e) subsequently fermenting and maintaining moisture of the product at 30-35%, (f) adding organic materials, nitrogen, phosphorus and potassium to the fermented product, and (g) packing the product.
NOVELTY - Bioorganic fertilizer is prepared by mixing livestock and poultry manure, straw, water, and mixed strains, sealing mixture, subjecting the mixture to fermentation at 20-30 degrees C for 2-3 days, aging product at 50-60 degrees C for 3-5 days under ventilation, adding nitrogen source and phosphorus source to mixture, where the ratio of the mixture, nitrogen source and phosphorus source is 30:10-15:4-8, collecting aged product, crushing the aged product in machine, granulating mixture, drying granules until moisture content becomes 10-20%, and cooling dried granules.    USE - The bioorganic fertilizer is useful for improving soil structure.    ADVANTAGE - The fertilizer completely utilizes farmyard manure, causes no pollution, and can be easily absorbed by plants.    DETAILED DESCRIPTION - The bioorganic fertilizer is prepared by mixing 50 parts livestock and poultry manure, 30 parts straw, 14-18 parts water, and 3 parts mixed strains, sealing mixture, subjecting the mixture to fermentation at 20-30 degrees C for 2-3 days, aging product at 50-60 degrees C for 3-5 days under ventilation, adding nitrogen source and phosphorus source to mixture, where the ratio of the mixture, nitrogen source and phosphorus source is 30:10-15:4-8, collecting aged product, crushing the aged product in machine, granulating mixture, drying granules until moisture content becomes 10-20%, and cooling dried granules.
NOVELTY - Special fertilizer comprises 10-12 pts. wt. leftovers during monosodium glutamate (MSG) production, 45-49 pts. wt. ditch mud, 96-100 pts. wt. corn stover, 9-13 pts. wt. nitro humic acid, 35-40 pts. wt. urea, 15-25 pts. wt. potassium bisulfate, 4-6 pts. wt. vermiculite, 5-8 pts. wt. calcium superphosphate, 4-7 pts. wt. magnesium oxide, 2-3 pts. wt. ferrous sulfate, 3-5 pts. wt. effective microorganism, 8-10 pts. wt. soil conditioner, and suitable amount of water.    USE - The special fertilizer is used for improving growth of trees (claimed).    ADVANTAGE - The special fertilizer has slow-release effect, and is convenient to use.    DETAILED DESCRIPTION - Special fertilizer comprises 10-12 pts. wt. leftovers during monosodium glutamate (MSG) production, 45-49 pts. wt. ditch mud, 96-100 pts. wt. corn stover, 9-13 pts. wt. nitro humic acid, 35-40 pts. wt. urea, 15-25 pts. wt. potassium bisulfate, 4-6 pts. wt. vermiculite, 5-8 pts. wt. calcium superphosphate, 4-7 pts. wt. magnesium oxide, 2-3 pts. wt. ferrous sulfate, 3-5 pts. wt. effective microorganism, 8-10 pts. wt. soil conditioner, and suitable amount of water. The soil conditioner comprises 10-20 pts. wt. sepiolite, 1-2 pts. wt. nano-carbon powder, 4-5 pts. wt. sodium metasilicate, 17-19 pts. wt. methyl methacrylate, 3-4 pts. wt. selenium yeast, 2-3 pts. wt. copper sulfate, 2-3 pts. wt. zinc gluconate, 1-2 pts. wt. magnesium chloride, 2-3 pts. wt. ammonium molybdate, 1-2 pts. wt. boric acid, 4-6 pts. wt. dipentaerythritol hexaacrylate, 30-40 pts. wt. vinegar, 2-3 pts. wt. chitosan, 1-2 pts. wt. Eucalyptus oil, and 0.5-1 pts. wt. sodium nitrophenolate. The soil conditioner is prepared by mixing methyl methacrylate, dipentaerythritol hexaacrylate, sepiolite, nano-carbon powder and Eucalyptus oil, stirring the mixture uniformly, adding remaining ingredients except vinegar to the mixture, stirring the mixture uniformly, and mixing with vinegar.
NOVELTY - Bio-fertilizer comprises mustard straw, corn straw, lotus root powder, polyacrylamide, Bacillus subtilis, Streptomyces microflavus, B.laterosporus, diethyl aminoethyl hexanoate, polyaspartic acid, potassium fulvate, sodium tripolyphosphate, potassium dihydrogen phosphate, sodium nitrophenolate, naphthaleneacetic acid and humic acid.    USE - The bio-fertilizer is used in organic farming (claimed) for preventing plant diseases caused by insects and promoting growth of plants.    ADVANTAGE - The bio-fertilizer increases yield of plants.    DETAILED DESCRIPTION - Bio-fertilizer comprises 13-21 pts. wt. mustard straw, 32-38 pts. wt. corn straw, 7-10 pts. wt. lotus root powder, 10-25 pts. wt. polyacrylamide, 10-30 pts. wt. Bacillus subtilis, 10-25 pts. wt. Streptomyces microflavus, 10-20 pts. wt. B.laterosporus, 2-6 pts. wt. diethyl aminoethyl hexanoate, 25-45 pts. wt. polyaspartic acid, 6-18 pts. wt. potassium fulvate, 7-14 pts. wt. sodium tripolyphosphate, 7-9 pts. wt. potassium dihydrogen phosphate, 3-5 pts. wt. sodium nitrophenolate, 3-5 pts. wt. naphthaleneacetic acid and 4-7 pts. wt. humic acid.
NOVELTY - Organic biofertilizer comprises rare earth elements, humic acid, peat, starch, livestock and poultry excrement, sodium dihydrogen phosphate, sodium polyphosphate, chitin, polypeptides, metal pyrophosphate, potassium pyrophosphate, aluminum phosphate, calcium hydrophosphate, plant protein, plant activating enzymes, Trichoderma, Bacillus subtilis and Bacillus licheniformis.    USE - As organic biofertilizer.    ADVANTAGE - The organic biofertilizer is natural and environmentally-friendly, increases crop yield, improves quality of crop, and reduces heavy metal content and harmful substance in plant product.
NOVELTY - Special compound fertilizer comprises 4-5 pts. wt. tung oil, 4-15 pts. wt. human urine, 8-20 pts. wt. plant ash, 8-25 pts. wt. rapeseed cake, 15-60 pts. wt. pig manure, 4-20 pts. wt. sawdust, 1-15 pts. wt. rock phosphate powder, 2-30 pts. wt. urea, 2-12 pts. wt. potassium sulfate, and 1-8 pts. wt. humic acid.    USE - The special compound fertilizer is useful for tea tree (claimed).    ADVANTAGE - The special compound fertilizer is convenient to use and enables to supply organic and inorganic nutrients in a balanced manner.    DETAILED DESCRIPTION - Special compound fertilizer comprises 4-5 pts. wt. tung oil, 4-15 pts. wt. human urine, 8-20 pts. wt. plant ash, 8-25 pts. wt. rapeseed cake, 15-60 pts. wt. pig manure, 4-20 pts. wt. sawdust, 1-15 pts. wt. rock phosphate powder, 2-30 pts. wt. urea, 2-12 pts. wt. potassium sulfate, and 1-8 pts. wt. humic acid. The special compound fertilizer is prepared by (a) adding tung oil and human urine, and adding mixture to the plant ash, (b) crushing rapeseed cake, sawdust, and rock phosphate, and mixing with pig manure and humic acid, performing fermentation for 7 days or more, and (c) adding mixture obtained in the step (a) to fermented mixture obtained in the step (b) and adding remaining raw materials, and drying obtained product. An INDEPENDENT CLAIM is included for method for preparing the special compound fertilizer, which involves performing the above-mentioned process.
NOVELTY - Organic fertilizer comprises 10-15 pts. wt. corn straw, 15-20 pts. wt. bean straw, 4-7 pts. wt. indolebutyric acid, 25-30 pts. wt. potato stalk, 30-35 pts. wt. pigweed, 5-7 pts. wt. silicon fertilizer, 20-30 pts. wt. silicate, 4-8 pts. wt. potassium chloride, 3-9 pts. wt. monoammonium phosphate, 4-8 pts. wt. talc, 3-5 pts. wt. microorganism, 15-25 pts. wt. livestock and poultry excrement, 10-20 pts. wt. urea, 3-9 pts. wt. ammonium hydrogen carbonate and 5-9 pts. wt. zinc sulfate.    USE - The organic fertilizer is useful for rice plants (claimed).    ADVANTAGE - The fertilizer requires less dosage, provides balanced nutrition to rice plant, and improves quality of soil.
NOVELTY - Use of combination of efficient microbial technology and multi-stage anaerobic baffled reactor (ABR), multi-stage aerobic baffle reactor and oscillatory baffled reactor (OBR), is claimed for treating feces. The efficient microbial technology is performed using high solution bacteria.    USE - The combination of efficient microbial technology, and ABR and OBR is useful for treating feces (claimed).    ADVANTAGE - The combination of efficient microbial technology and ABR and OBR enables to treat excrement without producing harmful substance from excrement wastewater, and in an environmentally-friendly manner.
NOVELTY - Complex microbial fertilizer comprises mica, rock phosphate powder, kaolin, potassium, grass charcoal, quartz, calcium superphosphate, potassium hydroxide, Aeromonas powder, Candida powder, Rhodococcus powder, steamed mushroom powder, Escherichia coli powder, Bacillus subtilis powder, chicken manure and sodium alginate.    USE - The complex microbial fertilizer is useful for resolving soil compaction, repairing and conditioning soil, controlling plant diseases caused by pests, and enhancing stress resistance of crop.    ADVANTAGE - The complex microbial fertilizer increases fertilizer utilization rate, is environmentally-friendly, and increases crop quality and yield.    DETAILED DESCRIPTION - Complex microbial fertilizer comprises 5-15 pts. wt. mica, 5-8 pts. wt. rock phosphate powder, 10-20 pts. wt. kaolin, 7-12 pts. wt. potassium, 25-40 pts. wt. grass charcoal, 8-16 pts. wt. quartz, 12-22 pts. wt. calcium superphosphate, 3-6 pts. wt. potassium hydroxide, 2-4 pts. wt. Aeromonas powder, 1-3 pts. wt. Candida powder, 3-5 pts. wt. Rhodococcus powder, 2-4 pts. wt. steamed mushroom powder, 1-4 pts. wt. Escherichia coli powder, 4-6 pts. wt. Bacillus subtilis powder, 15-20 pts. wt. chicken manure and 8-16 pts. wt. sodium alginate.
NOVELTY - Special organic fertilizer comprises 30-40 pts. wt. urea-formaldehyde fertilizer, 20-30 pts. wt. organic composite fertilizer, 5-10 pts. wt. composite probiotic, 2-5 pts. wt. stabilizing agent and 2-5 pts. wt. adsorbent.    USE - The composite organic fertilizer is useful for promoting the growth of pomegranate.    ADVANTAGE - The organic fertilizer can be prepared simply, has slow-release effect and increased stability, and increases absorption of nutrition and minerals by the crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing urea-formaldehyde organic fertilizer, which involves preparing urea-formaldehyde fertilizer by dissolving the formaldehyde in water to obtain 37% formaldehyde solution, mixing the modified starch and formaldehyde to obtain starch solution, adding urea and sulfuric acid into starch solution, pouring the mixture into reaction kettle and mixing uniformly to obtain urea-formaldehyde fertilizer, then mixing the dairy manure, bamboo and straw, crushing, drying and then adding the obtained powder into donkey-hide gelatin powder and yeast, and fermenting the mixture to obtain the organic composite fertilizer, mixing the urea-formaldehyde fertilizer and organic composite fertilizer, adding composite probiotics, stabilizing agent and adsorbent and fermenting the mixture at 30-37 degrees C to obtain the product.
NOVELTY - Organic composition comprises 20-30 pts. wt. dry leaves, 20-30 pts. wt. pig manure, 10-15 pts. wt. calcium magnesium phosphate, 15-20 pts. wt. extract of castor leaves, 4-8 pts. wt. ammonium sulfate, 5-8 pts. wt. molasses, 10-15 pts. wt. Bacillus subtilis, 15-20 pts. wt. Rhizopus oryzae, 4-10 pts. wt. castor bean, 4-12 pts. wt. semen armeniacae amarum, 6-12 pts. wt. garlic, 8-16 pts. wt. bone powder, 3-9 pts. wt. plant ash, 5-10 pts. wt. peat and 3-6 pts. wt. chinaberry seed.    USE - The organic composition is useful as insecticide and fertilizer (claimed).    ADVANTAGE - The organic composition is cost-effective and environmentally-friendly, does not damage soil, and has increased quality of crop.
NOVELTY - A synthetic oil and biomass gas are prepared from biomass by heating biomass at 300-700 degrees C under 0.1-20 MPa pressure for 0.1-1000 seconds, thermal cracking at 350-600 degrees C under 0.1-10 MPa pressure for 0.1-600 seconds, gasifying coke at 750-1500 degrees C under 0.1-20 MPa pressure for 1-60 minutes, and heating at 600-1200 degrees C in hot carrier.    USE - Method for preparing synthetic oil and biomass gas from biomass.
NOVELTY - The method involves lowering biomass thermal cracking to obtain oil gas and coke. The oil and gas is separated from biomass. The coke gasification medium and gasification are obtained from gasification reaction product under lower gasification condition. The gasification condition is processed at 700-1500 degrees centigrade temperature and 0.l-20MPa pressure for 60 minutes. The gasification medium is mixture of water vapor and oxygen. The biomass is selected from crop straw, agricultural waste, forestry waste, organic garbage, aquatic plant and plant energy.    USE - Method for preparing biomass synthesis gas.    ADVANTAGE - The biomass synthesis gas is produced effectively in reliable manner, without production of tar. The energy consumption for preparing biomass synthesis gas is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating method for preparing biomass synthesis oil. (Drawing includes non-English language text)
NOVELTY - The method involves processing a geometric model. Geometrical size of an anaerobic bio-hydrogen reactor is determined. A deriving geometric model is constructed. Waste water, sludge and fermentation gas continuous flowing process is performed. Turbulent energy dissipation rate is measured. Mass conservation equation and quantity conservation equation are constructed. Atmospheric pressure condition is determined. Water power ascending flow rate is determined. Up-flow anaerobic fermentation bio-hydrogen reactor optimization designing process is performed.    USE - Up-flow anaerobic fermentation bio-hydrogen reactor design optimization method.    ADVANTAGE - The method enables improving designing efficiency. The method enables performing up-flow anaerobic fermentation bio-hydrogen reactor design optimization process in a stable manner. The method enables reducing designing period and designing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an up-flow anaerobic fermentation bio-hydrogen reactor design optimization method.'(Drawing includes non-English language text)'
NOVELTY - Preparation of lithium-iron-phosphate material involves weighing soluble phosphorus source compound, iron source compound and lithium source compound, dissolving phosphorus source compound, iron source compound and lithium source compound in deionized or distilled water, providing precursor solutions in a reactor, carrying out hydrothermal process and solid-liquid separation process, washing, providing the resultant product into carbonitriding vacuum furnace, adding carbonitride, urea or formamide, carrying out carbonitriding process, and drying.    USE - Preparation of lithium-iron-phosphate material (claimed).    ADVANTAGE - The method provides lithium-iron-phosphate material with high purity, and excellent electrochemical property, mechanical property, conductivity, and crystal lattice stability.    DETAILED DESCRIPTION - Preparation of lithium-iron-phosphate material involves weighing soluble phosphorus source compound, iron source compound and lithium source compound, dissolving phosphorus source compound, iron source compound and lithium source compound in deionized or distilled water to obtain precursor solutions, providing precursor solutions in a reactor, carrying out hydrothermal process to obtain precursor of lithium-iron-phosphate crystals, carrying out solid-liquid separation process, washing to obtain pure crystals of lithium-iron-phosphate precursor, providing the resultant product into carbonitriding vacuum furnace at 520-650 degrees C under -0.04 MPa to -0.08 MPa, then providing the resultant product into vacuum carbonitriding infiltration furnace under 5-20 degrees C/minute, adding carbonitride, urea or formamide, carrying out carbonitriding process for 1-5 hours, and drying the resultant product. The content of crystals of lithium-iron-phosphate precursor is 0.5-3 %mass.
NOVELTY - A household garbage deodorizing and sterilizing liquid contains 60-80 wt.% seed liquid, 3-10 wt.% sodium dodecyl benzene sulfonate, 1-5 wt.% sodium carbonate, and 0.1-1 wt.% alkaline protease in which seed is mixed liquid.    USE - A household garbage deodorizing and sterilizing liquid (claimed).    ADVANTAGE - Product resists smelly source, eliminates harmful organism, is non-toxic, has no residue, and does not produce secondary pollution.
NOVELTY - Plant extract prepared by heating an extract of Sphaerophysa salsula and then extracting under reflux conditions, is claimed.    USE - The plant extract is useful for killing diamondback moth.    ADVANTAGE - The environmentally friendly plant extract has good insecticidal activity and safety.
NOVELTY - A mineral mud mask comprises 50-75 wt.% Xihua red clay, 1.5-4 wt.% glycerol, 0.2-2 wt.% lauramidopropyl betaine, 0.5-5 wt.% amino acid humectant, 2-7 wt.% hyaluronic acid, 1-3 wt.% additive, and balance deionized water. The red clay is from Xihua rapeseed red clay. The additive is essence and/or preservative.    USE - Mineral mud mask used for removing dirt and reducing wrinkles.    ADVANTAGE - The mineral mud mask makes skin smooth and is easy to clean. The method has low production cost, high production efficiency, and no environmental pollution, toxicity and stimulation and is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of facial cleanser comprising selecting clean Xihua red clay block, crushing into fine powder, and sieving through 30-450 meshes screen; sterilizing at 98.066 kPa and at 121-126 degrees C for 15-25 minutes and drying; weighing, adding deionized water, stirring, heating to 65-90 degrees C, adding glycerol and lauramidopropyl betaine, stirring, cooling to 40-60 degrees C, adding hyaluronic acid, amino acid humectant, and additive, stirring, and homogenizing.
NOVELTY - Mixed fertilizer comprises 50-54 pts. urea, 10-16 pts. superphosphate, 10-18 pts. potassium sulfate, 0.5-1.5 pts. trace elements, 2-8 pts. humic acid, 2-8 pts. amino acids, 0.5-1.5 pts. biological bacteria and 4-10 pts. skimmed oil tea seed cake. The trace elements include vanadium, selenium, calcium, magnesium, sulfur, iron, zinc, boron, manganese, copper, chlorine, molybdenum and/or nickel; and the biological bacteria include nitrogen-fixing bacteria, phosphate-solubilizing bacteria, potassium-solubilizing bacteria, Bacillus, Actinomycetes 5406 and/or saccharomycetes.    USE - The mixed fertilizer is useful for Camellia oleifera (claimed), grain and oil crops, fruit tree and vegetable, tea and other economic crops.    ADVANTAGE - The fertilizer greatly increases the quality and yield of Camellia oleifera.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the mixed fertilizer, comprising taking the mentioned raw materials; crushing skimmed oil tea seed cake, and biological bacteria, mixing with humic acid, stirring, carrying out biological fermentation, to obtain organic active substance; mixing organic active substance and urea, superphosphate, potassium sulfate, amino acids and trace elements, crushing, and mixing; granulating the mixture, centrifuging, drying and screening.
NOVELTY - A refinery dry gas is subjected to pressure swing adsorption regeneration method, to obtain hydrogen and regenerated adsorbed gas. Obtained regenerated gas is fed to membrane separation system, to obtain hydrogen gas and dehydrogenated gas. Dehydrogenated gas is subjected to cold oil absorption method. The obtained cold oil comprising carbodiimide, and absorption liquid are supplied to desorption column to obtain desorption solution. The desorption solution is distilled to obtain ethylene and ethane-enriched gas.    USE - Recovery of high-purity ethylene from refinery dry gas (claimed).    ADVANTAGE - The method efficiently recovers high-purity ethylene from refinery dry gas, with high yield.    DETAILED DESCRIPTION - A refinery dry gas is subjected to pressure swing adsorption regeneration tower, to obtain intermediate gas containing composition comprising non-adsorbed components. The adsorbed components are then regenerated to obtain dry gas composition rich in ethylene. The product obtained during regeneration process, is fed to second-stage pressure swing adsorption regeneration tower to obtain hydrogen and regenerated adsorbed gas. The regenerated gas resultant from second-stage pressure swing adsorption regeneration tower is fed to a membrane separation system, to obtain hydrogen gas and dehydrogenated gas. The obtained dehydrogenated gas is contacted with cold oil absorber, and cold oil absorption method is carried out. The cold oil comprising carbodiimide obtained in the absorption process and absorption liquid of the resultant components are supplied to desorption column to obtain desorption solution containing two or more carbon components and oil absorbent. The desorption solution is added to distillation tower, and the oil adsorbent is further contacted with cold oil absorber. The desorption liquid is further distilled, to obtain ethylene and ethane-enriched gas.
NOVELTY - Producing sorbitol and isosorbide involves keeping cellulose in water in the presence of catalyst to perform a reaction and to obtain desired product.    USE - Method for producing sorbitol and isosorbide (claimed).    ADVANTAGE - The method enables to produce sorbitol and isosorbide in cost-effective, eco-friendly, simple and non-corrosive manner, and with high conversion rate of cellulose (100%) and high yield of sorbitol (90%) and isosorbide (60%).
NOVELTY - Aluminum trichloride catalyst is added into fluorobenzene and o-fluorobenzoyl chloride, reaction temperature is controlled at 100-150 degrees C, then o-fluorobenzoyl chloride is added in drops, temperature is maintained at 40-60 degrees C, obtained water-oil layer is subjected to decompression distillation, temperature is increased to 100-110 degrees C, temperature is maintained for 2 hours, fluorobenzene is recycled, and 2000 ml water is added to obtain crude product. The crude product is recrystallized by adding recrystallization solvent, to obtain 2,4'-difluorobenzophenone.    USE - Synthesis of 2,4'-difluorobenzophenone used as alcohol intermediate.    ADVANTAGE - 2,4'-Difluorobenzophenone is prepared by simple method.    DETAILED DESCRIPTION - Aluminum trichloride catalyst is added into fluorobenzene and o-fluorobenzoyl chloride, such that ratio of fluorobenzene, o-fluorobenzoyl chloride and aluminum trichloride is 1-2:1:2-3, reaction temperature is controlled at 100-150 degrees C, then o-fluorobenzoyl chloride is added in drops, temperature is maintained at 40-60 degrees C, obtained water-oil layer is subjected to decompression distillation, temperature is increased to 100-110 degrees C, temperature is maintained for 2 hours, fluorobenzene is recycled under vacuum degree of 0.098 MPa, and 2000 ml water is added, to obtain crude product. The crude product is recrystallized by adding recrystallization solvent, to obtain 2,4'-difluorobenzophenone.
NOVELTY - Re-crystallizing sodium pyruvate comprises (i) dissolving sodium pyruvate crude product in pure water and filtering to remove inorganic impurities, (ii) dropping aqueous solution of sodium pyruvate into medical grade anhydrous ethanol in ice bath, crystallizing sodium pyruvate and filtering to obtain wet product, and (iii) vacuum drying the wet product, crushing, sieving, checking and packaging to obtain pure white solid sodium pyruvate.    USE - The method is useful for re-crystallizing sodium pyruvate (claimed).    ADVANTAGE - The method: is simple, convenient to control, environmentally friendly and suitable for industrial production; and ensures recycling of solvent and produces high quality and high purity sodium pyruvate with yield of more than 85%.
NOVELTY - Purifying pravastatin sodium comprises: taking two different macroporous adsorption resin chromatography media in a first and second chromatographic columns, respectively, and connecting the first chromatographic column with the second chromatographic column; taking pravastatin sodium crude product, adding deionized water to the crude product and then stirring, and filtering to obtain a sample liquid; eluting the sample liquid with deionized water; and concentrating the eluted liquid and then freeze-drying to obtain the pravastatin sodium having a purity of more than 99.95%.    USE - The method is useful for purifying pravastatin sodium (claimed) that is useful in a medicine.    ADVANTAGE - The method is capable of purifying the pravastatin sodium in a simple, convenient, eco-friendly and cost-effective manner without using toxic acid and alkali solutions.    DETAILED DESCRIPTION - Purifying pravastatin sodium comprises: taking two different macroporous adsorption resin chromatography media in a first and second chromatographic columns, respectively, as fixed phase, and connecting the first chromatographic column with the second chromatographic column; taking pravastatin sodium crude product having a purity of 98-99%, adding deionized water to the crude product and then stirring, and filtering using a paper filter to obtain a sample liquid a having a pravastatin sodium concentration of 100-250 mg/ml; sampling the liquid with a sample liquid; eluting the sample liquid with deionized water using high performance liquid chromatography; and concentrating the eluted liquid and then freeze-drying to obtain the pravastatin sodium having a purity of more than 99.95%.
NOVELTY - 2,4,5-Trimethoxy-benzoic acid (I) and 2-amino-thiazole-4-methyl carboxylate (II) are heated in a solvent in presence of a condensing agent and base to obtain 2-(2,4,5-trimethoxy-benzoylamino)-thiazole-4-methyl carboxylate (III). The obtained compound (III) and (2-aminoethyl)bis(propan-2-yl)amine (IV) are subjected to amination reaction and reacted with hydrochloric acid to obtain 4-N-(2-(bis(propan-2-yl)amino)ethyl)-2-C-(2-hydroxy-4,5-dimethoxybenzene)-1,3-thiazole-2,4-dicarboxamide hydrochloride (V).    USE - Preparation of 4-N-(2-(bis(propan-2-yl)amino)ethyl)-2-C-(2-hydroxy-4,5-dimethoxybenzene)-1,3-thiazole-2,4-dicarboxamide hydrochloride (claimed).    ADVANTAGE - The method efficiently and safely provides 4-N-(2-(bis(propan-2-yl)amino)ethyl)-2-C-(2-hydroxy-4,5-dimethoxybenzene)-1,3-thiazole-2,4-dicarboxamide hydrochloride by simple method with high productivity, without affecting the environment.    DETAILED DESCRIPTION - 2,4,5-Trimethoxy-benzoic acid of formula (I) and 2-amino-thiazole-4-methyl carboxylate of formula (II) are heated in a solvent in presence of a condensing agent and base to obtain 2-(2,4,5-trimethoxy-benzoylamino)-thiazole-4-methyl carboxylate of formula (III). The obtained compound (III) and (2-aminoethyl)bis(propan-2-yl)amine of formula (IV) are subjected to amination reaction and reacted with hydrochloric acid to obtain 4-N-(2-(bis(propan-2-yl)amino)ethyl)-2-C-(2-hydroxy-4,5-dimethoxybenzene)-1,3-thiazole-2,4-dicarboxamide hydrochloride of formula (V).
NOVELTY - Producing calcium superphosphate involves crushing crude phosphate rock, grinding, grinding mesh size of 90-92 after using shock sieve screening; screening the slurry after the slurry is pumped into tank through slurry pump, and violent reaction with concentrated sulfuric acid in mixing reaction tank, the generation superphosphate; setting on reaction tank, finishing the reaction, the generated calcium phosphate directly flows into formation tank, to pool in standing 2-4 hours, formation tank of full calcium phosphate, taking inner curing library, curing in one week, and filtering.    USE - For producing calcium superphosphate (claimed).    ADVANTAGE - The method is energy saving, the whole production process does not need to use fuel, saves energy, reduces the production cost, and the reaction tank set on the generated calcium superphosphate directly flows into the formation tank, and saves the conveying loop.    DETAILED DESCRIPTION - Producing calcium superphosphate involves crushing crude phosphate rock, grinding, grinding mesh size of 90-92 after using shock sieve screening; screening the slurry after the slurry is pumped into tank through slurry pump, and violent reaction with concentrated sulfuric acid in mixing reaction tank, the generation superphosphate; setting on reaction tank, finishing the reaction, passing generated calcium phosphate into the formation tank, to pool in standing 2-4 hours, formation tank of full calcium phosphate, taking inner curing library, curing in one week, then filtering, taking out large granule of calcium phosphate.
NOVELTY - Purifying biogas using a photo-biological reactor comprises performing filtering or anaerobic treatment of biogas slurry, feeding the processed biogas slurry into a liquid storage tank, injecting biogas slurry into a liquid surface sensor, filling injected biogas slurry in a sterilizing device, adding microalgae into the biogas slurry and then placing in a lighting device with a carbon dioxide air inlet tube, culturing the microalgae to achieve the desired chemical oxygen demand, total nitrogen and total phosphorus content in the biogas slurry, and discharging the biogas slurry.    USE - The method is useful for purifying biogas (claimed).    ADVANTAGE - The method is capable of simply, economically and reliably purifying the biogas with high purification efficiency.    DETAILED DESCRIPTION - Purifying biogas using a photo-biological reactor comprises performing filter or anaerobic treatment of biogas slurry, feeding the processed biogas slurry into a liquid storage tank through a feed tube, injecting biogas slurry into a liquid surface sensor, filling injected biogas slurry in a sterilizing device, adding microalgae into the biogas slurry and then placing in a lighting device with a carbon dioxide air inlet tube, culturing the microalgae for 20-30 days, so that the density of microalgae for achieving a desired chemical oxygen demand, total nitrogen and total phosphorus content in biogas slurry, is 1.5-2.5, discharging the biogas slurry, placing discharged slurry into the liquid storage tank, and performing flocculation process. The light biological reactor comprises a liquid storage tank provided with a sterilizing device, a feed tube, a discharge tube, a lighting device, a carbon dioxide air inlet tube, a pH sensor, an illumination sensor and a liquid surface sensor.
NOVELTY - Cherry potting nutrition soil comprises 30-50 pts. wt. canal mud, 20-30 pts. wt. cattle manure, 20-30 pts. wt. plant ash, 5-10 pts. wt. sodium alginate, 3-5 pts. wt. rapeseed cake, 3-6 pts. wt. eggshell powder, 1-2 pts. wt. microbial fertilizer, 2-5 pts. wt. nutrition liquid, and 1-3 pts. wt. starch grafted acrylate.    USE - The nutrition soil is useful for potting cherry (claimed).    ADVANTAGE - The nutrition soil is easy to use, does not cause environmental pollution, and can be prepared with improved permeability, high nutritional value and rich minerals in an economical manner.
NOVELTY - Chlorocresol green synthesis involves selecting m-cresol as raw material, tetrachlorethylene as solvent, and thionyl chloride as chlorinating agent. The molar ratio of mixing m-cresol and tetrachlorethylene is 1:0.5-1:1.5. The molar ratio of mixing thionyl chloride with m-cresol is 1:0.9-1:1.1.    USE - Method for synthesizing chlorocresol green (claimed).    ADVANTAGE - The method enables to synthesize chlorocresol green in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device, which comprises three tubular reactor, receiving tank, detecting port, feeding port, and mixing tank.
NOVELTY - Preparation of amino acid chelate involves subjecting hair keratin protein to hydrolysis reaction, neutralizing, filtering obtained hydrolyzate, performing chelating reaction and preparing amino acid chelate.    USE - Preparation of amino acid chelate used for animal nutrient and plant nutrient for crop growth.    ADVANTAGE - The amino acid chelate is prepared by simple and economical method, in short period of time. Crops are grown using the amino acid chelate by environmentally-friendly method with high yield.
NOVELTY - Decolorizing and purifying iopromide comprises: (i) loading macroporous polystyrene-divinylbenzene microsphere resin as a stationary phase into a chromatographic column, setting the column flow rate with deionized water; (ii) completely dissolving crude iopromide in deionized water by stirring to obtain sample solution, then filtering; (iii) passing the sample solution via column; and (iv) eluting deionized water, measuring eluate purity by high-performance liquid chromatography, mixing the fractions having more than 99% purity, concentrating via nano-filtration membrane, then spray-drying.    USE - The method is useful for decolorizing and purifying iopromide (claimed).    ADVANTAGE - The method: yields more than 90% product having more than 99% purity; does not cause environmental pollution; and is simple and suitable for industrial production.    DETAILED DESCRIPTION - Decolorizing and purifying iopromide comprises: (i) loading macroporous polystyrene-divinylbenzene microsphere resin as a stationary phase into a chromatographic column, setting the column flow rate to 1-4 column volumes/hour using 2 column volumes of deionized water; (ii) completely dissolving 95-98% crude iopromide in deionized water by stirring to obtain a sample having concentration of 100-250 mg/ml, then filtering the sample solution through a filter paper; (iii) continuously passing the sample solution via column with a flow rate of 1-4 column volumes/hour, where the ratio of resin volume (l) to sample weight (g) is 1:10-1:80; and (iv) loading deionized water as a mobile phase, eluting one column volume with a flow rate of 1-4 column volumes/hour, measuring eluate purity by high-performance liquid chromatography by eluting 0.5 column volume every time, mixing the fractions having more than 99% purity, concentrating via nano-filtration membrane, then spray-drying to obtain iopromide having more than 99% purity.
NOVELTY - Purifying cetirizine comprises (a) dissolving cetirizine hydrochloride, and small amount of potassium iodide in water and mixed solution of ethanol, stirring uniformly, adding 40% potassium bicarbonate solution, adjusting the pH to 7.5-8.5, and allowing to stand for 15-30 minutes, (b) adding ethanol and dichloromethane mixed solution into the reaction liquid, adjusting the pH to 6-7, crystallizing for 1-1.5 hours, and (c) filtering, washing the product with dichloromethane for more than 2 times, and drying.    USE - The method is useful for purifying cetirizine (claimed).
NOVELTY - Preparation of acyclovir valerian includes adding acyclovir and carbobenzyloxy-L-valine in N,N-dimethylformamide solution, and reacting; adding carbon powder in the reaction liquid, cooling, removing dicyclohexyl urea material by filtration, concentrating the filtrate and purifying by crystallization; and drying, dissolving solution in an organic solvent, adding palladium on carbon catalyst, introducing hydrogen gas, reacting, filtering, concentrating, crystallizing and purifying to obtain the acyclovir valerian compound.    USE - Method for preparing acyclovir valerian (claimed).    ADVANTAGE - The method is simple, clean and environment-friendly, and has high yield.    DETAILED DESCRIPTION - Preparation of acyclovir valerian comprises:    (A) adding acyclovir and carbobenzyloxy (CBZ)-L-valine in N,N-dimethylformamide solution, controlling the temperature at 20-30 degrees C, and reacting for 10-15 hours to obtain the X2 and X3 reaction solutions;    (B) adding carbon powder in the reaction liquid, cooling at 0 plus minus 2 degrees C, removing X3 material by filtration, concentrating the filtrate and purifying by crystallization to obtain compound of formula (X2); and    (C) drying X2 solution, dissolving the X2 solution in an organic solvent, adding palladium on carbon catalyst, introducing hydrogen gas, reacting for 5-10 hours at 20-25 degrees C, filtering, concentrating the filtrate, crystallizing and purifying to obtain the acyclovir valerian compound of formula (X1), where X2 is 2-((2-amino-1,6-dihydro-6-oxo-9H- Purin-9-yl)methoxy)ethyl-N-section oxo group-L-valine, and X3 is dicyclohexyl urea.
NOVELTY - Preparation of belotecan involves uniformly mixing natural camptothecin with ferrous sulfate salt, adding aqueous sulfuric acid solution and methyl source, mixing uniformly, adding hydrogen peroxide, performing free-radical methylation reaction, obtaining reaction product, extracting the obtained reaction product, purifying, adding isopropylamine, acid, methylene source and polar solvent to the resultant material, carrying out Mannich reaction under heating condition, obtaining reaction product, separating the unreacted raw material, and crystallizing.    USE - Preparation of belotecan (claimed).    ADVANTAGE - The method provides belotecan with reduced energy consumption, by an economical process.
NOVELTY - Production of bispregnenolone acetate involves subjecting diosgenin to ring-opening reaction, then oxidizing, hydrolyzing, and purifying.    USE - Production of bispregnenolone acetate (claimed).    ADVANTAGE - The method enables economical production of bispregnenolone acetate with yield of 79.5% by environmentally-friendly process. Oxidant can be recycled.
NOVELTY - Soapberry peel is vacuum-concentrated, water is added, ultrasonic extraction is carried out, residue and liquid separation of resulting mixture is carried out to obtain extract and wet residue. The extract is pressed to obtain supernatant and wet residue. The supernatant is concentrated under vacuum to obtain concentrated liquid and condensate. The condensate is recycled, added to foam separation column, and purified to obtain purified material and sugar solution. The purified material is spray-dried to obtain soapberry soap powder.    USE - Processing of soapberry powder (claimed).    ADVANTAGE - The method provides soapberry powder without using organic solvent and other separation medium, and without discharging waste.    DETAILED DESCRIPTION - Soapberry peel is vacuum-concentrated, water is added, ultrasonic continuous countercurrent extraction is carried out, residue and liquid separation of resulting mixture is carried out to obtain extract and wet residue. The extract is pressed using filter press, to obtain supernatant and wet residue. The supernatant is concentrated under vacuum to obtain concentrated liquid and condensate. The condensate is recycled, added to foam separation column, purified to obtain purified material and sugar solution. The resulting sugar solution is fermented, granulated, and fermented to obtain organic fertilizer. The purified material is spray-dried to obtain soapberry soap powder.
NOVELTY - This utility new type relates to a one aritificial wetland microorganism flora adjusting device, which solves a problem that the aritificial wetland technology has a certain of limitation. This utility new type is as follows: a main pipe, pneuma source tube and a carbon source dosing agent to the formed shaped, microbial carbon source dosing the main tube is; uniform distribute a plurality of main water penetrate a hole on the main tube wall, uniform distribute several a water penetrate a hole on the tube wall of the middle section of the fill micro-organism immobilized material between the main and pneuma source a tube middle section. This utility new type of positive effects as follows: according to a condition of a sewage to be process, air, liquid nutrition, adjust microbial flora, control is simple, application range.
NOVELTY - One a new sewage processing device, include glass, support frame, an aeration head and filling layer, wherein: a glass greenhouse set with middle support frame with the glass greenhouse is divided into upper space and lower space area area, a mesh support frame of said root is provided with a large water plant support, a glass greenhouse lower space area front end set with a water inlet, a glass greenhouse lower rear space area end set with a water port, a glass greenhouse lower space area front end set with an air inlet, a glass greenhouse lower bottom area is set with one row of aeration head, said aeration head is connected with the air inlet, a lower glass greenhouse space area aeration head is set with a filler layer. This utility new type appearance, sewage processing cost is low, load of high, it is especially suitable for the construction or a large community.
NOVELTY - This utility new type claims a one by using kitchen garbage processing organic fertilizer of system, comprise the dehydration device, comprise drive device, said drive device by a drive spiral blade, feed inlet and discharge hole of charging barrel, a spiral blade along the axial direction is inserted in said charging barrel, discharging port of said material along discharging direction reducing, crushing spike device, used for for kitchen waste and a process of crushing, and a kitchen garbage in adding a organic fertilizer of auxiliary material fermentation device, for kitchen garbage crushing of a fermentation process, forming organic fertilizer, cooling device, used for for fermentation of organic fertilizer after cooling process. So set, by using kitchen garbage of this utility new type provide a processing of a organic fertilizer, the can for a process to make the kitchen waste into organic fertilizer.
NOVELTY - This utility new type provide a one normal pressure extracting straw bio-oil system of condensing device, which solves a problem that the straw in the bio-oil to extract by using carrier pneuma as fluidized medium, which not only increases the power consumption, further exist a certain safety hidden trouble. This utility new type is as follows: a condensing tube with the pyrolysis pneuma pipeline connected, wherein a condensing tube by front disk tube, the left connecting tube, a three-way pipe, a right tube and rear disk tube are connected in series, wherein each disk tube with a connecting point of a connecting tube located adjacent disk most lower tube of a tube, in a cooling tank is one a one coil, each in a cooling tank filled with circulation water, the left connecting tube, a tee joint, a right connecting tube located in the cooling tank is V shape, the lowest three-way, set on a rear fan disk tube most tube of the upper layer. This utility new type of positive effects as follows: the whole technique process pressure, eliminate the pressure generated by a safety hidden trouble, at the same time, reduces the power consumption and operation cost caused by pressure, energy-saving and environment-friendly.
NOVELTY - This utility new type provide a one normal pressure continuous thermal cracking straw extracting biological oil of a, which solves a problem that the straw in the bio-oil to extract by using carrier pneuma as fluidized medium, which not only increases the power consumption, further exist a certain safety hidden trouble. This utility new type of is as follows: drying the straw, crushing, thermal cracking, thermal cracking device is multiple by a spiral feeder are connected end to end, reciprocating, electric heating tube is coated on the surface of each a spiral feeding pipeline, one set with a pyrolysis pneuma pipeline on the upper part of each spiral feeding machine a cavity; the produce of pyrolysis pneuma condensation, the deslagging. This utility new type of positive effects as follows: the whole technique process pressure, eliminate the pressure generated by a safety hidden trouble, at the same time, reduces the power consumption and operation cost caused by pressure, energy-saving and environment-friendly.
NOVELTY - Between the refractory material and the outer wall of this utility new type provide the one with temperature regulating function of a pyrolysis and gasification furnace, a gasification furnace comprise a solution layer, burning layer, combustion layer, a gasification furnace futher comprise: first pipeline, one end said first pipeline of connected fluid source, and the other end connected inlet end of fluid channel, fluid channel, a fluid channel is only set with a combustion layer of the, temperature sensor, a temperature sensor set on the said inner layer combustion, valve, a valve set in said second pipeline a. This utility new type has simple structure, excellent property and so on, widely applied to a garbage gasification furnace, biomass gasification furnace and gasification furnace in.
NOVELTY - This utility new type relates to a removing one of a lignin, thereof comprise: reactor (1) and microwave device, a reactor (1) is provided with alkaline solution to remove lignin to a reaction section, said reaction section is contained in a microwave device (2) in a microwave field. A removing lignin of this utility new type aims to provide one of a treatment period is short, processing capacity and efficiency of high.
NOVELTY - A one sewage treatment device, include glass, support frame, an aeration head and decanter, a glass greenhouse set with middle support frame with the glass greenhouse is divided into upper space and lower space area area, a mesh support frame of said root is provided with a large water plant support, a glass greenhouse lower space area front end set with a water inlet, a glass greenhouse rear end lower space area set with water and a water outlet, and the water outlet is connected with a glass greenhouse lower space area left side set with an air inlet, a glass greenhouse lower bottom area is set with one row of aeration head, said aeration head is connected with the air inlet. This utility new type appearance, sewage processing cost is low, load of high, it is especially suitable for the construction or a large community.
NOVELTY - This utility new type relates to a one by using microorganism fuel cell for domestic sewage purification process of device. The existing micro-organic power-generating device cannot maintain microbiological fuel cell a at ambient temperature, but also can not know electric quantity detection result and with power. A one by using microorganism fuel cell for domestic sewage purification process of device, the comprise of the walking pedestal (1), a walking pedestal mounting with constant temperature and magnetic force stir. (2), proton exchange film layer (3), an anode reaction room (4), a cathode reaction room (5) and collect box (6) and the hollow barrier the external set, collect the top mounting power supply management device (7), a power supply device connecting electric device (8), anode reaction room inner suspension of (10), a cathode (11) and reference electrode cathode reaction room inner suspension of (12) a collect device. This utility new type application in the microbial fuel cell.
NOVELTY - A one biological degradable clarification integrated breaking oil extraction waste water processing device. Device main body is divided into one to four level emulsion breaking and oil and solid-liquid separator, each first-stage inner breaking emulsion and inner mounting area with a filler box bracket, stuffing box mounting bracket with a modularized combination packing box, each first-stage emulsion breaking area and inner side wall of the upper part mounting on the weir, a weir connected with water tube, water tube extending downwards passes through the emulsion breaking and oil removing side wall with the next emulsion breaking and oil outlet connected with inner. The body mounting with an aeration system, the aeration system by fan, aeration pipe, aeration head, the inner body the upper part mounting device with a scraper, a scraper by scraping oil machine, unmotivated. The device using microorganism technology for oil extraction waste water proceed demulsification and degradation. The microbial flora produce a biological enzyme, the sewage in oil droplet emulsion breaking, oil to separate water, then to water in oil as a microbial growth need of a carbon source, for the degradation, the process of oil removing effect.
NOVELTY - This utility new type claims a one high concentration organic waste water processing and using system, comprise water collecting well, a regulating tank, a marsh gas fermenting tank, a desulfurizing tower, a transition tank, biological turntable, sterilizing tank and composting device, a water collecting well, a regulating tank, a marsh gas fermenting tank, transition tank, biological rotating disc and sterilizing pool in turn connecting between the water collecting well and the marsh gas fermenting tank set with filter used for a coarse screen, a marsh gas fermentation tank and a desulfurizing tower, the marsh gas fermentation tank and the biological rotating disc set with filter used for a fine grid. This utility new type are finished at the same time in the process of sewage, but also can produce biogas and compost, a full use of resource, produce a biogas and compost can produce economic benefit of one series, reduces the operation cost of sewage treatment up to a certain extent, through water temperature and temperature water tube boiler, which can accelerate gas produce speed and accelerate sewage treatment speed, increase sewage treatment efficiency and reduces the operation cost of sewage treatment.
NOVELTY - This utility new type claims a turner of one turn polishing mechanism belongs to the field of organic fertilizer production device, in particular for components of turner for compost a polishing work using a turn. Turn throwing mechanism of the turner include mounting the power transmission shaft support frame two end and a lower shaft, a shaft is provided with two interval arrangement of chain wheel, a chain wheel mounting the link between adjacent chain plate set with support material supporting plate, a chain plate uniform fixed hanging plate of the L type, wherein the surface is coated with a chain belt, a hanging plate of the L type fixed on the belt and chain plate up. Because the belt is paved on the upper chain plate, the scraping plate are fixed on the chain plate a, a belt with the chain plate move together would not then leakage, accumulated, corrosion plate. A part due to power transmission shaft and lower shaft of not mounting chain wheel is equipped with a shaft, a rotate a support cylinder. A reducing for friction prolongs use life of belt.
NOVELTY - This utility new type provide a one normal pressure continuous hot cracking straw of thermal cracking device, which solves a problem that the straw in the bio-oil to extract by using carrier pneuma as fluidized medium, which not only increases the power consumption, further exist a certain safety hidden trouble. This utility new type is as follows: a plurality of a spiral feeder are connected end to end and arranged to the surface of each spiral feeder pipeline a uniform coated electric heating tube, and then using heat insulated material is made of binding the electric heat tube is covered on the surface of a steel tube, the upper part of each spiral feeding machine a cavity set with one end of a pyrolysis pneuma pipeline, all of pyrolysis pneuma of exit and pipeline are connected in parallel. This utility new type of positive effects as follows: the whole technique process pressure, eliminate the pressure generated by a safety hidden trouble, at the same time, reduces the power consumption and operation cost caused by pressure, energy-saving and environment-friendly.
NOVELTY - This utility new type claims a one for coal and biomass gasification of common feeder, include the adding hopper and the feeding tube, a feeding tube and a connecting with the gasification reactor through the spiral shaft in the feeding tube, one end shaft of the motor a spiral, a spiral blade set and mix up the spiral blade shaft, a blade set corresponding to mix a section body and a lower part of the spiral shaft. Feeding tube include first feeding tube and the second feeding tube, and the second tube feeding tube connecting middle storage hopper, a loose air tube set on the inner middle storage bin on the first. This utility new type is added mix up the spiral blade shaft, blade mix a can prevent the biomass and coal layer density caused by a different such that feeding of difficult. In addition a loose air inner middle storage hopper can prevent frame material " and futher mix to ensure the material of uniformity.
NOVELTY - This utility new type is a small one of the ship loaded with gas of biomass gasification reaction kettle system, a vehicle for a each engine use. It is mainly composed by the reaction kettle, a heat exchanger, a washing tower and water tank. Gasification pneuma pipe of the reaction kettle top part is connected to the reaction kettle in a heating pressurizing tube, is connected a heat exchanger air inlet pipe of one end. The reaction kettle of the lower part of the outer wall is water cold wall reaction kettle, the upper part of the super-heater. Lower heat exchanger of a separate tube one connected liquid inlet end of lower washing tower, spraying reactor connected dust steam nozzle. Washing tower top part with an air outlet connecting tube. This utility new type a the garbage is made of air as a reaction raw material use, and available pole is made of wheat straw as a raw material, it changes waste into valuable. This utility new type has simple structure and practical, production efficiency is high.
NOVELTY - This utility new type relates to a one depending on the electrolytic water produce hydrogen oxygen mix gas of a burner, the burner system comprise direct current power supply device, water electrolysis groove device, electrolyte supplying device, mix gas collecting cavity, mix gas ratio regulating chamber and a burner, wherein a hydrogen-oxygen mix gas ratio regulating cavity connecting with an air supplied device, air supplied device and connecting with the direct current power supply device, the air outlet of burner oxygen mix gas ratio regulating cavity connecting. This utility new type through direct current power supply device in the water electrolytic groove device, water electrolytic device electrolytic water groove continuously fast produce hydrogen oxygen mix gas, by hydrogen-oxygen mix gas collecting chamber collecting the hydrogen-oxygen mix ratio of 2: 1, then entering into hydrogen oxygen mix gas ratio regulating cavity, a device with the air supply of the air a mix, rear regulating hydrogen-oxygen mix ratio, the burner, produce heat.
NOVELTY - This new type utility claims one energy-saving combustion supporting a vehicle hydrogen-oxygen generating system, include the control box and a battery and a hydrogen-oxygen generator, a connecting water purification treatment device and air cleaner, inner control box control circuit plate connecting with a vehicle cigar lighter point,... and a hydrogen-oxygen generator. The vehicle hydrogen-oxygen generating system taking an electric control set, through a. detecting a tracking vehicle real-time speed, through regulating the size of a cell to a hydrogen, entering into amount of oxygen, a hydrogen making device with the vehicle real-time interaction, a circuit plate with the vehicle cigar lighter connecting point, realize the vehicle engine time, vehicle flameout time electrolytic stop parallel air pipeline inner residual hydrogen a effect inner avoids the vehicle flameout still, residual hydrogen residual oxygen pipeline pressure explosion of; the oxygen flow automatic regulating system, of a hydrogen oxygen without storage directly entering into engine cylinder, mounting operation is convenient, a save 20 %-40 % of fuel.
NOVELTY - This utility new type relates to a one lower biomass combustion furnace, belonging to burning device technology field, include gas generating furnace (1), a burner (2), bracket of self-adjusting and energy-saving cooker (3) and smoke tube (4), a burner in a gas generator and bracket of self-adjusting and energy-saving cooker, gas generating furnace is provided with grate (1.3), gas generating furnace top end opening, lower bottom of the gas generating furnace outer combustor wall of a side, the bottom of cooker bracket is provided with a through hole, the top part of burner passes through the bottom through hole of the cooker bracket, chimney connecting side surface of the cooker bracket. This utility new type using one secondary combustion and a combustion from a way, inner furnace through a secondary vent the biomass fuel combustion more fully, and using a low ignition of to make the material by upper, lower furnace around one layer of one layer would not produce;
NOVELTY - This utility new type relates to one a biomass gasification furnace, comprise a furnace body, a fan and a stove head, a stove body comprise an outer tube and inner tube, inner cylinder body connecting with the air inlet pipe, the other end a fan and connected through a mantle tube, and an outer tube wall middle part left with a gas tube, the other end tube of a gas stove head and the mantle connected, of the other end a mantle body; the outer tube right side wall close to the outer tube surface with a discharge tube, and the other end discharge tube of waste pneuma hole set with the inner tube and the outer tube set with tar tube, one end oil tube of the furnace body and a through inner tube, inner tube right side bottom wall set with ignition or the ash outlet channel, and the other end ash ignition or the channel passes through the outer tube of a furnace body and a, the top of the furnace body set with pressure cover, the pressure cover and the inner tube through a high temperature seal ring seal. This utility new type of beneficial effects as follows: simple structure, there is no tar and soot, fuel with aritificial ignition, and the effect is obvious.
NOVELTY - The utility model is a new type claims the lower one a suction type biomass gasification direct-fired, include gas generating furnace (1), air draft furnace (2), a combustion chamber (3) and a chimney (4), I (1.2) of lower part side surface (1.7) is set with the grate I (1.3) and the fixed connecting set with a gas-guide tube (1.9), a gas-guide tube is greater than depth height of the hearth I and gas-guide tube (1.9) is a whole body tube wall is set with a hollow through hole, furnace cavity II (2.2) of lower part side surface set with flue gas inlet (2.7), combustion room set with the gas generator with the wind furnace, the two end connected with a fire outlet, a flue inlet, chimney and the furnace port II (2.1) are connected. The pneuma for biomass direct-fired furnace using chimney cupping, a flue gas downwards operation inner the gas generator, and a directly observe fuel consumption condition is convenient to add material, hearth structure is simple and easy processing manufacturing and cleaning, especially suitable for rural family use.
NOVELTY - This utility new type claims a one extracting ethane from natural gas a device, comprise heat exchanger, a compressor, an expander, first-stage low temperature separator, second level low temperature separator, demethanizer, a heat exchanger in turn with the first-stage low temperature separator, an expander, a level low temperature separator, a compressor, the compressor is connected with the heat exchanger, a demethanizer, first-stage liquid phase exit of low temperature separator and liquid phase exit of second level low temperature separator is connected with a demethanizer, a level one pneuma is exit a low temperature separator is further connected with a demethanizer directly. This utility new type rear compressor through the expansion pneuma heat exchanging condensing pressure, and then cooling through the stream throttling, depth deethanizer supply cold, wherein the compressor is mature and reliable, using mix with other refrigerant refrigeration deethanizer process compared to the compressor is low, the investment is less, manufacturing period short at least one refrigeration system set, at the same time, operation maintenance is more simple, the utility model is new type of project total investment is greatly reduced.
NOVELTY - Processing of pre-hydrolysis waste liquid involves adding white liquor, green liquor, or one or more types of a weak liquid generated in a kraft pulp manufacturing process to pre-hydrolysis waste liquid, and carrying out an anaerobic treatment using granule sludge.    USE - Processing of pre-hydrolysis waste liquid generated during manufacture of dissolution kraft pulp.    ADVANTAGE - The method enables stable processing of pre-hydrolysis waste liquid with reduced chemical oxygen demand o0f wastewater. The processed pre-hydrolysis waste liquid enables efficient manufacture of methane gas which is utilized as energy source in pulp plant and biogas which is utilized as energy source in recovery boiler and kiln, and is discharged directly in ocean or river and reused as water for factories.
NOVELTY - A palm shell charcoal briquettes product comprises charcoal briquettes and palm shell raw material without the use of adhesive or binder.    USE - As palm shell charcoal briquettes product (claimed).    ADVANTAGE - The palm shell charcoal briquettes product without adhesives is produced more economically; is increased production capacity; and is produced with production capacity and greater acceleration of this type of palm shell charcoal briquettes before.
NOVELTY - Manufacturing organic fertilizer by fermentation of solid waste containing organic material or a mixture of organic materials using bacterial biofertilizer, comprises decomposing organic material using bacterial biofertilizer, drying the decomposed organic material through a dryer to a moisture content of 12-17%, mixing the dried organic material with dolomite, subsequently spraying Azotobacter sp., followed by spraying seaweed extract as a mineral fastening agent, and molding the sprayed mixture into granules or tablets using a pressing machine.    USE - The method is useful for manufacturing organic fertilizer (claimed), which is useful as a nutrient or manure for crops, and as biopesticides. No biological data given.    ADVANTAGE - The method is capable of manufacturing the organic fertilizer with high quality in a less time consuming and an eco-friendly manner. The organic fertilizer improves soil fertility and soil water holding capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the organic fertilizer obtained by the above method.
NOVELTY - Use of agricultural waste chosen from rice husks, coconut shells, corncobs and empty fruit bunches of oil palm is claimed as an activated charcoal for controlling pesticide residues in soil of dry and wet lands. The activated charcoal is used in form of powder and has properties provided in table 1 of the patent specification. The activated charcoal when applied to soil binds to or restrains residues of pesticides.    USE - The agricultural waste chosen from rice husks, coconut shells, corncobs and empty fruit bunches of oil palm is useful as an activated charcoal for controlling residues of organochlorine class of pesticide chosen from lindane, aldrin, dieldrin, heptachlor, dichlorodiphenyltrichloroethane (DDT) and endosulfan, and organophosphate class of pesticide preferably chlorpyrifos, in soil of dry and wet lands (all claimed), preferably agricultural or horticultural land.    ADVANTAGE - The agricultural waste as activated charcoal prevents washing away of the pesticide residues with flow of water, and hence river is protected from contamination of the pesticide residues. The activated charcoal increases population of beneficial microorganisms in the soil, as the activated charcoal serves as suitable habitat for the beneficial microorganisms, and hence increased population of beneficial microorganisms enable decomposition of the pesticide residues that are adsorbed on the surface of the activated charcoal. The agricultural waste as activated charcoal exhibits high pesticide residues absorption efficacy up to 750 mg/g or more.
NOVELTY - The hydrogen water generator apparatus (1) has electrolysis board (3) having anode plate (31) and cathode plate (32) arranged substantially horizontal inside of the drink container (2). An electroconductive part (4) is arranged from the anode plate and the cathode plate to the exterior of the drink container. An electric power feeding part (5) supplies electric power to the anode plate and the cathode plate through the electroconductive part, respectively.    USE - Hydrogen water generator apparatus.    ADVANTAGE - Provide an improved and user-friendly hydrogen water generator apparatus that generates hydrogen water with high hydrogen gas solubility.    DESCRIPTION OF DRAWING(S) - The drawing shows the longitudinal cross sectional view of the hydrogen water generator apparatus.    Hydrogen water generator apparatus (1)    Drink container (2)    Electrolysis board (3)    Electroconductive part (4)    Electric power feeding part (5)    Anode plate (31)    Cathode plate (32)
NOVELTY - The manufacturer has a gas reservoir equipped with a manometer (11) to determine pressure in a process vessel (1). Pressure regulator pendulum weights (8) are increased when gas increases, where the pressure regulator pendulum weights are decreased if gas is unused to prevent corrosion and gas leaks in the manufacturer. A biogas reactor (3) is equipped with a switch (12) that serve as a tool to open and close the gas, where the biogas reactor is moved from one place to another according to location of user's needs. An inlet (4) enters a fermentation medium into the vessel.    USE - Portable biogas equipment manufacturer for facilitating fermentation of biogas manure from household, restaurant and market. Uses include but are not limited to cow, horse, buffalo, pig, chicken, goat and sheep, industrial waste e.g. palm oil and tapioca, and organic waste.    ADVANTAGE - The manufacturer is easily ignited and easy to operate in shifts about incorporating wheel or hand stroller or car. The manufacturer allows flame to easily to set up, clean cookware and kitchen to be clean and tidy, thus saving installation time and cost of making the manufacturer in a quick manner. The manufacturer prevents leakage of gas from biogas or leakage from the vessel.    DETAILED DESCRIPTION - The manufacturer is equipped with a base made of wood.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a portable biogas equipment manufacturer.    Process vessel (1)    Biogas reactor (3)    Inlet (4)    Pressure regulator pendulum weights (8)    Manometer (11)    Switch (12)
NOVELTY - Carbonization method, involves thermally decomposing biomass having low moisture content within carbonization furnace, obtaining carbonized fuel and dry distillation gas having low moisture content, drying biomass having high moisture content, storing the obtained dried biomass, carrying out fixed period continuation, thermally decomposing obtained product within the carbonization furnace, drying biomass having high moisture content in cabin, acquiring dried biomass, and storing obtained dried biomass.    USE - Carbonization method.    ADVANTAGE - The method performs carbonization process rapidly without adding extensive improvement to existing carbonization device.    DETAILED DESCRIPTION - Carbonization method, involves (a) thermally decomposing biomass having low moisture content within carbonization furnace, and obtaining carbonized fuel and dry distillation gas having low moisture content, (b) drying biomass having high moisture content in dry cabin using hot gas obtained by secondary combustion of the dry distillation gas at step (a), and acquiring dried biomass, (c) storing the obtained dried biomass, and carrying out fixed period continuation, (d) thermally decomposing obtained product within the carbonization furnace, and obtaining carbonized fuel and dry distillation gas of biomass having high moisture content, (e) drying biomass having high moisture content in cabin using hot gas obtained by the secondary combustion of the dry distillation gas at step (d), and acquiring dried biomass, and (f) storing obtained dried biomass.
NOVELTY - Preparing lenalidomide or its acid salt comprises performing condensation reaction of 2-(hydroxymethyl)-3-nitro-benzoic acid compound (I) or its acid salt with 3-aminopiperidine-2,6-dione (AA) under alkaline conditions to give 3-(4-nitro-1-oxo-isoindolin-2-yl)piperidine-2,6-dione (II), and performing catalytic hydrogenation reaction.    USE - The method is useful for preparing lenalidomide (claimed).    ADVANTAGE - The method easily, simply and safely prepares lenalidomide with reduced toxicity and without using virulent reagent in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing lenalidomide or its acid salt comprises performing condensation reaction of 2-(hydroxymethyl)-3-nitro-benzoic acid compound of formula (I) or its acid salt with 3-aminopiperidine-2,6-dione of formula (AA) under alkaline conditions to give 3-(4-nitro-1-oxo-isoindolin-2-yl)piperidine-2,6-dione of formula (II), and performing catalytic hydrogenation reaction.    R1=phenyl, benzyl, 1-6C-alkyl, 3-6C-cycloalkyl, phenylsulfonyl, p-toluenesulfonyl, methanesulfonyl, acetyl or trifluoroacetyl.
NOVELTY - Compound Fertilizer composition comprises (in pts.wt.): tung oil (2-10), human urine (2-10), urea (0-30), diammonium phosphate (3-20), potassium sulfate (0-40), soybean cake (0-25), peanut cake (5-28), livestock manure (5-25), wheat straw (2-20), Coriaria sinica (0-10), plant ash (1-10) and humic acid (0.5-8). Compound Fertilizer composition is prepared by heating urea and tung oil.    USE - Compound Fertilizer composition used for cropping lily (claimed).    ADVANTAGE - The compound Fertilizer composition shows improved planting in barren land.    DETAILED DESCRIPTION - Compound Fertilizer composition comprises (in pts.wt.): tung oil (2-10), human urine (2-10), urea (0-30), diammonium phosphate (3-20), potassium sulfate (0-40), soybean cake (0-25), peanut cake (5-28), livestock manure (5-25), wheat straw (2-20), Coriaria sinica (0-10), plant ash (1-10) and humic acid (0.5-8). Compound Fertilizer composition is prepared by heating urea and tung oil at 65-100 degrees C, and then the obtained material is coated to obtain coated controlled-release urea. The bean cake, peanut cake, wheat straw, Coriaria sinica and plant ash are crushed, and then mixed them with livestock manure and humic acid in balanced amount of water. The obtained material is fermented for 7-10 days to obtain fermented organic fertilizer. The human urine, tung oil and modified oxide are mixed uniformly to obtain farm oil urea fertilizer. The obtained farm urea fertilizer is mixed with the obtained fermented organic fertilizer, diammonium phosphate, potassium sulfate and coated controlled-release urea to obtain the finished product.
NOVELTY - The fuel cell (10) comprises separators (14,18,20) to separate an electrolytic membrane (16a) and an electrode structure (16b). An electrode (56) is laminated on both sides of the electrolytic membrane. The reactive-gas flow path distributes the reactive gas along the electrode plane, where the sealing elements (46,48,50) surround the reactive-gas flow path. The separators have plane seal portions (46f,48f,50f) between the inner side seal portions for opposing the edge part of the reactive-gas flow path. A flat seal is provided in the plane part.    USE - Fuel cell for generating electric power.    ADVANTAGE - The separators have plane seal portions between the inner side seal portions for opposing the edge part of the reactive-gas flow path, thus reliably prevents the shortcut of the reactive gas and the retention of generated water, and ensures desired electric power generation performance by simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Fuel cell (10)    Separators (14,18,20)    Electrolytic membrane (16a)    Electrode structure (16b)    Sealing elements (46,48,50)    Plane seal portions (46f,48f,50f)    Electrode (56)
NOVELTY - The fuel cell system has a modification part, which generates the fuel from the raw material for modification and modification water, and a hot storage water circulation circuit (24), which circulates the hot storage water. A condenser (25) condenses the water vapor in the combustion exhaust gas. A control apparatus (19) is provided to control the fuel cell and has a supply amount increasing part, which increases the supply amount of the oxidizing agent gas for combustion in the self-supporting generating mode when the temperature of the fuel cell is higher than predetermined temperature.    USE - Fuel cell system.    ADVANTAGE - The fuel cell system has a modification part, which generates the fuel from the raw material for modification and modification water, and a hot storage water circulation circuit, which circulates the hot storage water, and hence ensures reduced cost of the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell system. (Drawing includes non-English language text).    Generator (11)    Control apparatus (19)    Storage tank (21)    Hot storage water circulation circuit (24)    Condenser (25)
NOVELTY - The system has an electric power generation/electrolysis part electrolyzing water vapor supplied from a hydrogen-producing part i.e. fuel generation part (1), during regeneration of electric power. A detection part detects steam partial pressure in a closed space, which seals the hydrogen-producing part. A restriction part restricts electric power generation of the electric power generation/electrolysis part by using hydrogen supplied from the hydrogen-producing part in oxidized state of iron oxide based on a detection result of the detection part.    USE - Secondary battery-type fuel cell system for performing electric power generation.    ADVANTAGE - The restriction part restricts the electric power generation of the electric power generation/electrolysis part by using the hydrogen supplied from the producing part in oxidized state of the iron oxide based on the detection result of the detection part so as to suppress increase of steam partial pressure during electric power generation operation, so that charging and discharging efficiency of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a secondary battery-type fuel cell system.'(Drawing includes non-English language text)'    Fuel generation part (1)    Fuel cell part (2)    Container (3)    Piping (5)    Switch part (6)
NOVELTY - Fertilizer composition comprises carrier system for delivering bacterial mixture to crops, where the carrier system is coated using 1x 106-1x 1011 colony forming units (CFU)/g bacterial mixture chosen from genus Bacillus, Pseudomonas, and Streptomyces and nitrogen, phosphorus, and potassium (NPK) rating.    USE - The composition is useful for fertilizing crops. The crops are chosen from rice, corn, soy beans, tomatoes, lettuce, barley, wheat, legumes, and grass (all claimed).    ADVANTAGE - The composition has specified NPK rating.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing the composition, involves coating carrier with the above-mentioned bacterial mixture to produce bacteria coated carrier, and drying the coated carrier; and    (2) method (M2) for fertilizing crops involves contacting the crops with the above-mentioned composition.
NOVELTY - The method involves providing a medium for propagation of ethanologen. A first cell mass of ethanologen is supplied to the medium. Xylose is supplied to the medium as a carbon source for cell mass growth of the ethanologen. The medium comprising the first cell mass of ethanologen is maintained at a pH of between about 5.0 and 6.0 and at temperature of between about 26 and about 37 degrees Celsius such that the first cell mass of ethanologen is propagated into a second cell mass of ethanologen and the second cell mass of ethanologen is larger than the first cell mass of ethanologen.    USE - Method for propagating ethanologen e.g. yeast cells, organism and Saccharomyces cerevisiae (all claimed), for production of a fermentation product from biomass in a fermentation system.    ADVANTAGE - The method enables facilitating improvement in efficiency and yield of cellulosic ethanol from biomass. The method enables adjusting pre-treatment conditions such as pH, temperature and time, so that formation of inhibitors can be reduced or managed and components of the pre-treated biomass can be treated to remove or reduce a level of inhibitors.    DETAILED DESCRIPTION - The method enables providing an agent to the medium selected from a group consisting of nutrient, yeast extract, urea, diammonium phosphate, magnesium sulfate and zinc sulfate. An INDEPENDENT CLAIM is also included for a system for propagating ethanologen for production of a fermentation product from biomass in a fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of biorefinery comprising a cellulosic ethanol production facility.
NOVELTY - Device for producing humus, preferably compost, comprises a compost container (1), which forms a casing. The compost container is closed at the top by a lid (2). The lid forms a rain water collection basin (3). At least one outlet (5), which opens into the compost interior (4), is associated to the rain water collection basin. The outlet opens into a collection container, which is associated with the casing.    USE - The device is useful for producing humus, preferably compost.    ADVANTAGE - The device produces humus, which improves decomposition atmosphere in the compost container over a longer period.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of the device.    Compost container (1)    Lid (2)    Rain water collection basin (3)    Compost interior (4)    Outlet (5)
NOVELTY - Producing glucose from an organism, which has capability to store disaccharides in its body.    USE - The method is useful for producing glucose from the organism chosen from insects, crustaceans and mushrooms (all claimed). The glucose is useful for preparing bioethanol, and used as raw material for polymeric raw material.    ADVANTAGE - The glucose production method is time-saving, simple and cost-effective.
NOVELTY - Method for operating an electrochemical cell stack, involves feeding a reactant gas to the cell stack, halting the flow of the reactant gas to at least one cell in the cell stack, increasing the voltage applied to the at least one cell, and initiating the flow of reactant gas to the at least one cell in response to the voltage increasing above a threshold for a predetermined amount of time.    USE - The method or system is useful for operating an electrochemical cell stack which is used for separating hydrogen from contaminants in a gas stream substantially composed of hydrogen.    ADVANTAGE - The method requires decreased power and enables restoration of catalyst in an electrochemical cell to allow operation of the electrochemical cell at high carbon monoxide levels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system.
NOVELTY - Method for preparing microbial biofertilizer involves processing rice straw and sludge of aquaculture pond, mixing processed raw materials and compressing to obtain the product.    USE - The method is useful for preparing microbial biofertilizer (claimed).    ADVANTAGE - The method enables to prepare microbial biofertilizer, which is environmentally-friendly and safe, as the fertilizer contains natural and organic raw materials.
NOVELTY - Biologically purified fungal strain Cerrena sp. FBV41 is new.    USE - The fungal strain is useful for producing laccase enzyme, which is useful for decolorizing dyes and pretreating straw.
NOVELTY - Recovering hydrogen from isomerizing and reforming of hydrocarbons, involves the steps of combining a hydrochloric acid (HCl)-scrubbed, isomerization-zone net gas stream that comprises hydrogen and C6-hydrocarbons with a reforming-zone net gas stream that comprises hydrogen and C6-hydrocarbons to form a combined net gas stream that comprises hydrogen and light end hydrocarbons. The light end hydrocarbons are extracted from the combined net gas stream in a re-contacting zone using a reforming-zone product stream that comprises C5+ hydrocarbons to form a hydrogen-rich net gas stream.    USE - The method is useful for recovering hydrogen from isomerizing and reforming of hydrocarbons.
NOVELTY - The method involves drying plant biomass and reacting the dried plant biomass with hydrogen in a reactor at a temperature of about 150-200degree centigrade and pressure of about 50-200at, until 10-15% by weight of the material is remained. The reacted dried plant biomass is cooled for condensing the vapor from the hydrocarbon mixture mixed with the vapor obtained from reacted dried plant biomass to obtain a finished hydrocarbon mixture.    USE - Method for producing hydrocarbon mixture from plant biomass.
NOVELTY - The machine has a dryer for drying sludge (1) by using a hydrothermal continuing manufacture-type absorption refrigerating machine. An exhaust cycle duct (21) is fixed with a belt drier package (10a). An air conditioner (80) is provided with a regenerator (91) that is fixed with the hydrothermal continuing manufacture-type absorption refrigerating machine based on absorptive freezing cycle. A dehumidifying cooling coil (81) condenses and eliminates moisture of dry air. A cooling water circulation pump (72) circulates cooling water stored in a cooling water storage unit (72).    USE - Bulk unit available belt-type sludge drying machine.    ADVANTAGE - The absorption refrigerating machine utilizes digestion gas and biogas to produce region hot-water so as to perform sludge drying process in a landfill facility by a sewage treatment equipment, thus reducing power consumption. The machine effectively collects heat of combustion gas in a hot air production-type condenser of the absorption refrigerating machine so as to produce dry air of an electrical type heat pump (EHP) at high temperature by using refrigeration cycle condenser energy source. The machine exhausts gas to a cooling tower after heats sludge by using a heat radiation unit so as to improve coefficient performance of the cooling tower. The machine ensures that an EHP application belt drier dries water in a thermal medium so as to prevent water leakage and improve stability of the landfill facility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a bulk unit available belt-type sludge drying machine.'(Drawing includes non-English language text)'    Sludge (1)    Belt drier package (10a)    Exhaust cycle duct (21)    Cooling water circulation pump (72)    Air conditioner (80)    Dehumidifying cooling coil (81)    Regenerator (91)
NOVELTY - Reducing (M1) the cloud point of a renewable oil, involves: providing a renewable oil comprising waxy impurities; cooling the renewable oil; adding a polymer to the cooled renewable oil; mixing the cooled renewable oil and the polymer to form an oil-polymer mixture, which comprises solidified impurities; and separating at least a portion of the solidified impurities from the oil-polymer mixture to form a refined renewable oil.    USE - For reducing the cloud point of a renewable oil (claimed) such as biofuel.    ADVANTAGE - The method is useful for the efficient removal of gums and waxes from a renewable oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reducing (M2) the cloud point of a renewable oil, involving: providing renewable oil comprising phosphorus-containing compounds and/or free fatty acids; cooling the renewable oil; adding a polymer to the cooled renewable oil; binding the polymer to the phosphorus-containing compounds and/or the free fatty acids; and separating at least a portion of the polymer to form a refined renewable oil.
NOVELTY - Treating a formation containing crude oil hydrocarbons, involves: either injecting an aqueous composition comprising an internal olefin sulfonate with a nominal carbon chain length of 24-44 into the formation, and displacing the crude oil hydrocarbons toward one or more production wells; or providing into the formation, the aqueous composition by surfactant mixture/carrier fluid co-injection or by injection with a carrier fluid for the purpose of foam generation during tertiary oil recovery in heterogeneous or fractured reservoirs.    USE - The method is useful for treating a formation containing crude oil hydrocarbons by injecting an internal olefin sulfonate into the formation (all claimed), where the internal olefin sulfonate is used as a surfactant in enhanced oil recovery, preferably in traditional alkaline-surfactant and alkaline-surfactant-polymer chemical floods in tertiary oil recovery.    ADVANTAGE - The aqueous composition improves the wettability of a subsurface surface in a subsurface formation containing crude oil hydrocarbons, and has improved compatibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separating crude oil hydrocarbons from crude oil hydrocarbons compositions including a mixture of hydrocarbon molecules with a median carbon number of the mixture of hydrocarbon molecules of at least 28, comprising contacting the composition with an internal olefin sulfonate with a nominal carbon chain length of 24-44, preferably 24-36, where during the contacting step at least part of the crude oil hydrocarbons are separated from the remainder of the crude oil hydrocarbons comprising composition.
NOVELTY - Catalytic process involves producing hydrocarbon comprising organic halide in a process unit, and contacting the hydrocarbon comprising organic halide with metal chloride under anhydrous conditions in a halide removal vessel to produce contacted hydrocarbon containing 50-100 wt.% total halide in the hydrocarbon removed.    USE - Catalytic process (claimed).    ADVANTAGE - The method enables catalytic process that provides hydrocarbon products having reduced organic halide contaminants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for forming hydrocarbon, which comprises a process unit that produces hydrocarbon comprising organic halide, and a halide removal vessel, in which hydrocarbon comprising organic halide is contacted with metal chloride under anhydrous conditions to produce contacted hydrocarbon.
NOVELTY - A Trichoderma fungal culture cell, is new. The fungal culture cell expresses beta -glucosidase derived from Pyrococcus furiosus. Gene of beta -glucosidase derived from P.furiosus in which codons are changed, are introduced into Trichoderma fungal culture cell to form tetramer.    USE - The Trichoderma fungal culture cell is useful for producing sugar liquid (claimed) and in saccharification reaction.    ADVANTAGE - The fungal culture cell stably expresses beta -glucosidase, and maintains saccharification efficiency and provides prolonged saccharification reaction as beta -glucosidase is not secreted immediately, and stored and maintained in cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing sugar liquid, involves contacting cell and cellulase, and hydrolyzing cellulose containing biomass; and    (2) gene encoding beta -glucosidase.
NOVELTY - Preparing a nanoparticle composition, comprises: forming a nanoparticle aerosol comprising metal functionalized nanoparticles in a gas; collecting the metal functionalized nanoparticles of the aerosol in a capture fluid in communication with the low pressure reactor, where the capture fluid comprises a compound including a functional group Y1 reactive with the functional group of the metal functionalized nanoparticles; and reacting the compound and the metal functionalized nanoparticles to prepare the nanoparticle composition comprising nanoparticles.    USE - The method is useful for preparing a nanoparticle composition (claimed).    ADVANTAGE - The nanoparticle composition has excellent physical properties such as clarity and stability and improved luminescent quantum efficiency and photoluminescent intensity.    DETAILED DESCRIPTION - Preparing a nanoparticle composition, comprises: forming a nanoparticle aerosol comprising metal functionalized nanoparticles of formula (MX) in a gas; collecting the MX-functional nanoparticles of the aerosol in a capture fluid in communication with the low pressure reactor, where the capture fluid comprises a compound including a functional group Y1 reactive with the functional group of the metal functionalized nanoparticles; and reacting the compound and the metal functionalized nanoparticles to prepare the nanoparticle composition comprising nanoparticles.    M = group IV element; and    X = functional group comprising H or halo, preferably F, Cl, Br or I.
NOVELTY - The apparatus has an ammonia dissociator (6) that receives ammonia gas from an ammonia conditioner (5) and converts ammonia gas into a mixture of hydrogen, nitrogen and ammonia gases. A separator (7) receives the mixture and returns ammonia gas to ammonia dissociator, while separating hydrogen gas from nitrogen gas and venting nitrogen gas out of separator. A hydrogen conditioner (8) receives hydrogen gas and controls temperature and pressure of hydrogen gas. A fuel cell (10) receives hydrogen gas from hydrogen conditioner and produces an electrical current.    USE - Apparatus for converting ammonia into electrical energy used in automotive, racing, shipping, and railway industries for powering car, motorcycle, container truck and ship, bus, boat, train, and used for stationary and interim energy supply purposes such as power plant, generator, and back-up or emergency generator.    ADVANTAGE - The energy contained in the hydrogen and nitrogen gases are recovered between the temperature extremes from about 500 degrees C to about 1000 degrees C and so the loss of heat energy and consequent loss of ammonia/hydrogen/electricity production (AHEP) efficiency are prevented. The system controls the temperatures of the gases leaving the dissociator and entering both the hydrogen separator and the fuel cell such that damage to the components is prevented. Voltage regulators are used in such a way that over charging the battery is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for generating electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ammonia based system to prepare and utilize hydrogen to produce electricity.    Ammonia conditioner (5)    Ammonia dissociator (6)    Separator (7)    Hydrogen conditioner (8)    Fuel cell (10)
NOVELTY - Producing alcohol comprises saccharifying cellulosic biomass with cellulase in the presence of a recombinant yeast transformed with a gene encoding a polypeptide having a function of enhancing the saccharifying activity of cellulase.    USE - The method is used for producing alcohol (claimed).    ADVANTAGE - Polypeptides having a function of enhancing the saccharification efficiency of cellulase within reaction temperature regions of general fermenting microorganisms other than heat-resistant yeast are provided. Enhancement of the saccharifying activity of cellulase can improve the rate of saccharifying cellulosic biomass and the yield of ethanol from the cellulosic biomass.    DETAILED DESCRIPTION - Producing alcohol comprises saccharifying cellulosic biomass with cellulase in the presence of a recombinant yeast transformed with a gene encoding a polypeptide according to any one of the following (i) to (iii): (i) a polypeptide comprising the amino acid sequence shown in SEQ ID NO: 2 or 4; (ii) a polypeptide having 70% or more identity with a defined sequence of 241 or 238 amino acids (SEQ ID NO. 2 or 4), given in the specification, and having a function of enhancing the saccharifying activity of cellulase; and (iii) a polypeptide having an amino acid sequence that has a substitution, a deletion, an addition, or an insertion of one or more amino acid residues with respect to the amino acid sequence of SEQ ID NO. 2 or 4, and having a function of enhancing the saccharifying activity of cellulase.
NOVELTY - Method for producing hydrocarbon and hydrogen fuels involves (a) fermenting a biomass material containing fermentation medium with an inoculum comprising mixed culture of microorganisms derived from rumen contents of rumen-containing animal and incubating to produce volatile fatty acids in the medium, and (b) subjecting the volatile fatty acids or their salts to electrolysis under conditions effective to convert the volatile fatty acids or their salts to hydrocarbons and hydrogen.    USE - The method is useful for producing hydrocarbon and hydrogen fuels (claimed).    ADVANTAGE - The method is simple, rapid and cost-effective, and enables to produce hydrocarbon and hydrogen fuels simultaneously from biomass materials.    DETAILED DESCRIPTION - Method for producing hydrocarbon and hydrogen fuels involves (a) fermenting a biomass material containing fermentation medium with an inoculum comprising mixed culture of microorganisms derived from rumen contents of rumen-containing animal and incubating under anaerobic conditions for a sufficient time to produce volatile fatty acids in the medium, and (b) subjecting the volatile fatty acids or their salts to electrolysis under conditions effective to convert the volatile fatty acids or their salts to hydrocarbons and hydrogen, where the volatile fatty acids or their salts are concentrated in the medium prior to the electrolysis.
NOVELTY - Method for pre-treating cellulose-containing biomass involves carrying out hydrothermal treatment of the cellulose-containing biomass and fluidizing treated cellulose-containing biomass.    USE - The method is useful for pre-treating cellulose-containing biomass for preparing sugar (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing biomass composition for saccharification involves performing the steps as above-mentioned in the pretreatment method (M1); and    (2) method (M3) of preparing sugar involves hydrolyzing the above-mentioned biomass composition for saccharification.
NOVELTY - The system has an LNG generator (98) which includes heat exchanger (22) responsive for producing liquid natural gas. A first control valve applies preset amount of LNG in selected first portion of produced LNG to LNG storage unit as product. Second control valve applies second portion of produced LNG to nitrogen liquefaction section (55) to assist in liquefaction of nitrogen as determined by selected first portion amount. Third control valve applies liquid nitrogen from nitrogen liquefaction section to liquid nitrogen storage unit to store liquefied nitrogen as product.    USE - System for producing LNG and merchant gas products.    ADVANTAGE - The output pipeline pressure is reduced if letdown station is used, so that necessity to compress the gas returned to the relatively high pipeline pressure is eliminated. Thus power consumption of the system is significantly reduced. The output is increased with added components, so that economy of the increased capacity makes up the difference in the increased system cost.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the LNG producing system.    Heat exchanger (22)    Separator (34)    Control valve (35)    Nitrogen liquefaction section (55)    LNG generator (98)
NOVELTY - Method for treating solid organic material, involves providing phagotrophic algae, providing solid organic material, combining the algae and the solid organic material, allowing the algae to grow by engulfing or uptaking the solid organic material, forming an algal product, and collecting the algal product.    USE - The method or system is useful for treating solid organic material for producing algal product (all claimed) e.g. biomass, lipid, protein and carbohydrates which is used in nutritional, pharmaceutical, cosmetic, and industrial products, where the algal biomass and lipid are converted into biofuel.    ADVANTAGE - The method destroys harmful pathogens, and treats cost-effectively and rapidly in less time, preferably 5 days.    DETAILED DESCRIPTION - Method for treating solid organic material, involves (a) providing phagotrophic algae, providing solid organic material, combining the algae and the solid organic material, allowing the algae to grow by engulfing or uptaking the solid organic material, forming an algal product, and collecting the algal product, or (b) providing waste activated sludge at a pH more than 7, pretreating the waste activated sludge, adjusting the pH of the waste activated sludge to a pH of below 7, providing phagotrophic algae, combining the algae with the waste activated sludge, forming an algal product, and collecting the algal product. An INDEPENDENT CLAIM is included for system.
NOVELTY - Producing hybrid fuel, comprises mixing hydrophobic bio-liquid or oil with coal formed with multiple pores on the surface, and drying the mixture.    USE - The method is useful for producing hybrid fuel (claimed) for a power plant.    ADVANTAGE - The method is capable of producing the hybrid fuel with high calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hybrid fuel produced by the method.
NOVELTY - High-performance fuel, useful for engines comprises a mixture of a bioalcohol and a biogas.    USE - The fuel is useful for high performance engines.    ADVANTAGE - The fuel has high performance properties, burns completely and is cost effective and free of pollution.
NOVELTY - System for treating wastewater, comprises fluid tanks (1,2) and a draining tank with a passage for fluid and bagasse bundle (7) impregnated with bacteria. The bacteria are Pseudomonas sp., Nitrosomonas, Nitrobacter, Nitrosococcus, Azotobacter, Azomonas and Rhizobium. Pipes (4,5) are provided that pass through fluid tank. The fluid tank is provided with display type filters (8,9).    USE - System for treating wastewater.    ADVANTAGE - The system enables to treat wastewater by manually or automatically controlling and supplying the quantity of bacteria required for treating certain volume of wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating wastewater, which involves taking samples of wastewater from an outlet of a treatment plant, collecting samples of wastewater contained in the tanks of the treatment plant, taking the samples to a laboratory analysis and quantify bacteria tanks by volume of wastewater and then comparing with the amount of bacteria needed to meet the quality standard of residual water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a wastewater treatment system.    Fluid tanks (1,2)    Pipes (4,5)    Wall (6)    Bagasse bundle (7)    Display type filters (8,9)
NOVELTY - The device comprises a heat insulator (110) for maintaining temperature in an inside tank (100) suitable for cultivation. A pressure reduction valve (150) is provided for supplying the microorganism undiluted solution and nutrient. A flow meter (250) is provided for measuring flow rate in a discharge pipe (170). A culture tank (130) is formed with the inside tank and an extrinsic tank (120) is provided with the heat insulator. A container support portion (350) is formed to prop a vessel in a lower surface of a culture fluid exhausting portion.    USE - Device for distribution and cultivation of useful microorganism.    ADVANTAGE - The container support portion is formed to prop a vessel in a lower surface of a culture fluid exhausting portion which ensures that the smell from cultivated useful microorganism is removed effectively. The food waste is easily dispersed and the environment is made neat and clean.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a device for distribution and cultivation of useful microorganism.    Inside tank (100)    Heat insulator (110)    Extrinsic tank (120)    Culture tank (130)    Pressure reduction valve (150)    Discharge pipe (170)    Flow meter (250)    Container support portion (350)
NOVELTY - Preparation of entecavir (I) involves performing Tamao-Fleming oxidation reaction of 5-amino-3-((3R)-3-(hydroxymethyl)-2-methylidenecyclopentyl)-3H-imidazo(4,5-b)pyridin-7-one-derivative (II) in solvent.    USE - Preparation of entecavir (claimed).    ADVANTAGE - The method is economical and environmentally-friendly, and enables manufacture of entecavir, with high yield under mild reaction conditions.    DETAILED DESCRIPTION - Preparation of entecavir of formula (I) involves performing Tamao-Fleming oxidation reaction of 5-amino-3-((3R)-3-(hydroxymethyl)-2-methylidenecyclopentyl)-3H-imidazo(4,5-b)pyridin-7-one-derivative of formula (II) in solvent.    R1=group of formula (1);and    Y'=3-9C or heteroatom optionally connected to form optionally substituted 4-10 membered silicon-carbon heterocyclyl with silicon, or 3-9C optionally connected to substituent to form optionally substituted 4-10 membered silicon-carbon ring with silicon, in which the heteroatom is chosen from O, S or N, number of heteroatom is 1-3, substituent in the substitution is 1-3C alkyl, and silicon-carbon ring or silicon-carbon heterocyclyl ring is one ring or two combined ring.    An INDEPENDENT CLAIM is included for 5-amino-3-((3R)-3-(hydroxymethyl)-2-methylidenecyclopentyl)-3H-imidazo(4,5-b)pyridin-7-one-derivative (II) and 5-amino-3-((3R)-3-(hydroxymethyl)-2-methylidenecyclopentyl)-3H-imidazo(4,5-b)pyridin-7-one-derivative of formula (III).    R2=group of formula (14);    R'4,R'5=H,1-6C linear or branched alkyl or nitro;    R21=pyridyl (optionally substituted by one or more substituents chosen from 1-3C alkyl, halo and 1-3C alkoxy) or 6-10C aryl (optionally substituted by one or more substituents chosen from alkyl, halo and alkoxy);and    P2=group of formula (15) or (16), 1-6C substituted by 1-6C alkoxy or trimethylsilylethoxymethyl.
NOVELTY - A method for manufacturing an upgraded fuel gas and simultaneously producing succinic acid, involves: providing a bioreactor; providing anaerobic succinic acid-producing microorganisms; providing a carbon based substrate for the anaerobic succinic acid- producing microorganisms; adding a carbon dioxide (CO2)-containing fuel gas to the bioreactor; collecting the upgraded fuel gas thus produced, where the upgraded fuel gas has a lower carbon dioxide content than the carbon dioxide-containing fuel gas added; and optionally collecting the effluent containing succinic acid.    USE - For manufacturing an upgraded fuel gas and succinic acid (claimed).    ADVANTAGE - The process produces upgraded fuel gas having lower carbon dioxide content than the carbon dioxide-containing fuel gas added; and produces upgraded biogas having CH4 content of at least 90% (preferably at least 96%, especially at least 99.9%).
NOVELTY - Host cell expressing recombinant enzyme having beta-xylosidase activity comprising an amino acid sequence that is at least 70% identical to SEQ ID NO: 3, is new. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The host cell, the recombinant enzyme having beta-xylosidase activity, or the composition is useful for degradation of biomass for producing by-product, e.g. biofuel, where biofuel is ethanol; and for producing fermentable sugars (all claimed).    ADVANTAGE - The host cell expresses a mixture of cellulolytic enzymes to improve performance of the hydrolytic process or saccharification of biomass, thus increasing the amount of released fermentable sugars, and thus improving the performance of by-products preferably biofuels, derived from the fermentation process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a recombinant enzyme having beta-xylosidase activity expressed by the host cell;    (2) a composition comprising the host cell and/or recombinant enzyme having beta-xylosidase activity;    (3) a method for producing fermentable sugars comprising: (a) incubating the biomass with recombinant enzyme having beta-xylosidase activity or the composition; and (b) recovering fermentable sugars obtained after incubation of step (a); and    (4) a process for producing by-product from biomass comprising: (a) incubating the biomass with recombinant enzyme having beta-xylosidase activity or the composition; (b) fermenting the fermentable sugars obtained after incubation in step (a) with at least one fermenter microorganism; and (c) recovering the by-product obtained after fermentation of step (b).
NOVELTY - Method for producing aromatic hydrocarbons, involves processing a raw feedstock to form an intermediate feedstock, converting the intermediate feedstock to a feedstock stream comprising an alcohol, a carboxylic acid, or their combinations, conditioning the feedstock stream to provide an oxygenate mixture having a H:Ceff ratio of 0.8-1.8, and exposing the oxygenate mixture to a condensation catalyst.    USE - The method is useful for producing aromatic hydrocarbons, preferably biomass-derived aromatic hydrocarbons, hydrogen and COx molecules (all claimed).    ADVANTAGE - The method provides high yield.
NOVELTY - The system has a multifunctional controller parallely connected with a computer. An electrical resistor is connected with a model resistor, where the electrical resistor and the model resistor are equipped with an electrolyzer unit. The electrolyzer unit is equipped with a normalizing converter. An output end of the multi-functional controller is connected with an imitator through a measuring channel. The imitator is connected with the electrolyzer unit.    USE - Electrolyzer power line signal processing system.
NOVELTY - Manufacture of growing medium comprises removing contaminant objects from initial material which is by-product of composting process and comprises oversize biodegradable material and contaminants, removing mineral contaminants from the initial material, and subsequently defibrating the remaining material.    USE - Method for manufacturing growing medium (claimed) used for agriculture, horticulture and floriculture.    ADVANTAGE - The process utilizes waste material and eases the strain placed on landfill sites, and utilizes recycled material to produce growing medium which may be used as substitute for peat. The growing medium overcomes the environmental and horticultural disadvantages of extracting and using peat; has good water retention properties, which protect roots against excess water; and provides good soil structure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an apparatus for manufacturing growing medium from initial material, comprising contaminant object removing mechanism, mineral contaminant removing mechanism, and defibration unit;    (2) a defibrating unit comprising a feed screw which is rotatable to urge biodegradable material against a surface having a recess with edges; and    (3) a growing medium comprising defibrated material having bulk density of 100-300 kg/m3.
NOVELTY - Method for treating conversion stripper condensate involves conveying conversion stripper condensate from ammonia synthesis system to a stripping tower to carry out ammonia distillation treatment, condensing gas from outlet of the stripper to separate acid liquid, conveying the acid liquid to a thin liquid barrel through direct piping, discharging the acid liquid in the thin liquid barrel into a thin liquid distillation tower of alkali production apparatus to carry out ammonia distillation, and recycling distilled ammonia gas to system using mother liquor to produce alkali.    USE - Method for treating ammonia synthesis system conversion stripper condensate and producing alkali.    ADVANTAGE - The ammonia synthesis system conversion stripper condensate is economically treated by environmentally-friendly process.    DETAILED DESCRIPTION - Method for treating conversion stripper condensate involves conveying conversion stripper condensate from ammonia synthesis system to a stripping tower to carry out ammonia distillation treatment, condensing gas from outlet of the stripper to separate acid liquid, conveying the acid liquid to a thin liquid barrel through direct piping, discharging the acid liquid in the thin liquid barrel into a thin liquid distillation tower of alkali production apparatus to carry out ammonia distillation, recycling distilled ammonia gas to system using mother liquor to produce alkali, introducing residue liquid discharged from the bottom of the thin liquid distillation tower to the system, and recycling or discharging to sewage.
NOVELTY - Method for preparing glucose involves decomposing cellulose using mixture of cellulolytic enzyme, and saliva or an organic saliva-derived active auxiliary.    USE - The method is useful for preparing glucose (all claimed), which is useful for producing bioethanol, and as raw material for producing polymeric material.    ADVANTAGE - The method excellently improves glucose yield, and is cost-effective, as saccharification of cellulose raw material is performed by relatively mild enzymatic degradation.
NOVELTY - The apparatus has rotating element (60) installed at lower side of elevating element (50) to rotate support rod (10) arranged vertically in both sides of inner space of anaerobic digestion tub (T). The anaerobic digestion tub is installed in upper portion of hydraulic motor (40). The support rod is connected to platform (30) that is raised through pulley (51) and wire (52). A supporting plate (20) is provided for supporting lower portion of support rod. A propeller (41) for mixing is fixed to one side of platform which is movably assembled in top and bottom portions of support rod.    USE - Hydraulic drive type apparatus for mixing organic sludge such as livestock excretion and food waste for generating biogas.    ADVANTAGE - The sludge is stirred uniformly and effectively using hydraulic motor for enhancing the generation of the biogas through the anaerobic digestion mixing optimization. The malfunction occurring due to the overload is prevented effectively. The sludge mixing apparatus is provided with improved assembling efficiency. The explosion proof function of sludge mixing apparatus is enhanced, so that safety of the operator is secured.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the installation state of the sludge mixing apparatus.    Support rod (10)    Supporting plate (20)    Platform (30)    Hydraulic motor (40)    Propeller for mixing (41)    Elevating element (50)    Pulley (51)    Wire (52)    Rotating element (60)    Anaerobic digestion tub (T)
NOVELTY - Preconditioning pretreated cellulosic material, comprises incubating the pretreated cellulosic material with phenol oxidizing enzyme and glucoamylase.    USE - The method is useful for preconditioning a pretreated cellulosic material including washed, undetoxified or unwashed pretreated corn fiber, pretreated corn stover, corn cob, wheat straw, rice straw and/or switch grass, and oil seeds including Sorghum, rapeseed, soybean, palm, sunflower, cottonseed, peanut, flax seed, linseed, safflower, palm kernel, coconut and olive to recover oil and produce fermentation product (such as alcohol (e.g. ethanol and butanol), organic acid, ketone, amino acid and gas), and sugar, which is useful for producing syrups (e.g. high fructose corn syrups) and lignocellulose-derived plastics (e.g. polyethylene, polystyrene, and polypropylene), and polylactic acid (e.g. for producing polyethylene terephthalate) (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) recovering oil and producing a sugar from pretreated cellulosic material, comprising (i) preconditioning the cellulosic material with a phenol oxidizing enzyme, (ii) saccharifying the preconditioned material with a cellulolytic enzyme preparation, and (iii) recovering oil from saccharified material in step (ii);    (2) producing a fermentation product from cellulosic material, comprising performing (a) the steps (i) and (ii) as above per se, (b) fermenting the saccharified material with a fermenting organism, and (c) optionally recovering oil from saccharified material and/or the fermented material; and    (3) a composition comprising a phenol oxidizing enzyme and a glucoamylase.
NOVELTY - Carrier material for biomass for filtration of oil-contaminated waste waters is proposed. The carrier comprises a filtering material with immobilised cells of oil-oxidising microorganism Rhodotorula sp. VKM Y-2993D with the titer of cells - 106 CFU/cm3. The filtering material is used as basalt fibre STBFconst preliminary modified with cationic starch - oxyamil OPV-1.    USE - Biotechnology.    ADVANTAGE - Proposed carrier material has a high retention capacity of suspended particles and oil products and is used for filling the filters for cleaning oil-contaminated waste waters.1 tbl, 1 ex
NOVELTY - The apparatus has jacketed processing vessel (12) having heating element (14) to generate vapors of bio-pesticidal extracts present in slurry, and valve (30) to discharge slurry. A sediment and water separator-cum-storage chamber (18) of predefine volume is provided with filter element (20) adapted to receive and separate residual bio-wastes and hot water and a drain (32) for draining hot water for recycling back to mixer-cum-grinder (10). A bio-pesticide collecting tank (34) is connected to condensing unit for condensing vapors to obtain a condensate of bio-pesticide.    USE - Apparatus for extracting bio-pesticide (claimed) such as linamarin, lotaustralin and hydrogen cyanide (all claimed) from cassava plant bio-waste.    ADVANTAGE - The mass scale extraction of bio-pesticide contents from cassava bio-waste is obtained for making viable commercial exploitation of bio-wastes using easily fabricated mechanical device for small scale industries, while providing cost efficient process in terms of utilizing the bio-waste remained after cassava harvesting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for extracting bio-pesticide from cassava bio-wastes.
NOVELTY - A lignin hydrolyzing method involves pretreating a biomass comprising lignocellulose, straw or wood before microbial process in which sugar is fermented to ethanol, and directly pumping lignin pumped into a critical water reactor. The lignin in the reactor is hydrolyzed to obtain a hydrolyzate and restoring the hydrolyzate in a biogas plant.    USE - Method for hydrolyzing lignin.    ADVANTAGE - The method enables hydrolyzing lignin with high efficiency.
NOVELTY - The anaerobic digestion tank (100) has multiple impellers (122a-122c) which are located in lower portion of the shaft (124) rotated by motor (126). A pump (134) is connected to the circulating pipe (132). A control unit is configured to control the motor, the pump and gas compressor (144). A mechanical mixing unit (120) is configured to mix the biogas with effluent. The biogas is compressed by the gas compressor connected to the circulating pipe. The compressed biogas is ejected through the gas exhausting tube into the circulating pipe.    USE - Anaerobic digestion tank.    ADVANTAGE - The operational efficiency of the anaerobic digestion tank is improved, while maximizing the mixing performance of mixing unit. The maintenance cost of the anaerobic digestion tank is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the anaerobic digestion tank.    Anaerobic digestion tank (100)    Mechanical mixing unit (120)    Impellers (122a-122c)    Shaft (124)    Motor (126)    Circulating pipe (132)    Pump (134)    Gas compressor (144)
NOVELTY - This utility new type claims a new-type one continuous flow microbial fuel battery, CSTR comprise the anode room and CSTR cathode room, CSTR room and anode CSTR cathode room set with a water inlet and a water outlet, inner CSTR anode room mounting an anode electrode, CSTR cathode inner mounting between the electric device room, CSTR room and CSTR cathode anode room, a cathode electrode, an anode electrode and a cathode electrode through connecting the external wire through a pipeline connected between the pipeline set with a proton of the sewage, CSTR anode room and CSTR cathode room CSTR anode room and the top CSTR cathode inner room is further set with a pH probe interface, a temperature probe interface, ORP detection probe interface, further set with gas collecting tube interface CSTR in the cathode room. This utility new type of can aiming at waste water is not a quantitative volume continuous power generation, a continuous sewage, it is convenient and practical.
NOVELTY - Indole derivative (I) is new.    USE - Indole derivative used for preparing drug for treating cancer, particularly lung cancer, prostate cancer, pancreatic cancer or liver cancer (all claimed).    ADVANTAGE - The indole derivative is prepared in simple and eco-friendly manner with high yield.    DETAILED DESCRIPTION - Indole derivative of formula (I) is new.    R1,R2,R3 and R4=H, halogen atom, alkyl, alkylene, alkynyl or aryl group.
NOVELTY - Preparing high molecule water-absorbing resin fertilizer comprises preparing 31.5% of aqueous sodium hydroxide solution, adding the aqueous solution into acrylic acid, then carrying out neutralization reaction with acrylamide and urea at 50-60 degrees C for 20 minutes, adding the neutralized solution with crop straw powder, then stirring, carrying out graft copolymerization reaction to the stirred solution at 110-115 degrees C for 15 minutes by adding methylenebisacrylamide and ammonium sulfate, polymerization of the reacted mixture to obtain a solid product, and crushing the solid product.    USE - The method is useful for preparing high molecule water-absorbing resin fertilizer (claimed).    ADVANTAGE - The method is capable of economically and eco-friendly preparing high molecule water-absorbing resin fertilizer with high quality and simple operation and without waste product.    DETAILED DESCRIPTION - Preparing high molecule water-absorbing resin fertilizer comprises preparing 31.5% of aqueous sodium hydroxide solution by taking 19000 g of sodium hydroxide, adding the aqueous solution into the 23000 g of acrylic acid having more than 99.5% of purity, then carrying out neutralization reaction with 1800 g of acrylamide and 21000 g of urea at 50-60 degrees C for 20 minutes, adding the neutralized solution with 4100 g of crop straw powder having mesh size of 100-200, then stirring at 50-40 degrees C under a stirring speed of 100-120 revolutions per minute, carrying out graft copolymerization reaction to the stirred solution at 110-115 degrees C for 15 minutes by adding 8 g of methylenebisacrylamide as a crosslinking agent and 10 g of ammonium sulfate as an initiator, polymerization of the reacted mixture for 10-20 minutes to obtain a solid product, heating the reacted mixture for naturally drying during the polymerization process, and crushing the solid product.
NOVELTY - Aqueous solution of sodium hydroxide is prepared, dripped continuously to 25000 g acrylic acid, neutralized, reacted, and acrylamide is added. To the resultant solution, bean platinum powder is added, cooled, and methylene bisacrylamide as crosslinker and ammonium persulfate as initiator are added. Resultant mixture is subjected to graft copolymerization, and reaction temperature is controlled. Reaction mixture is added to polymerization reactor, aged, polymerized and dried. Obtained solid product is pulverized to obtain super absorbent polymer fertilizer.    USE - Preparation of super absorbent polymer fertilizer (claimed).    ADVANTAGE - The method safely and economically provides super absorbent polymer fertilizer having high quality in short period of time, without producing waste gas and waste water.    DETAILED DESCRIPTION - 30% Sodium hydroxide solution (20000 g) is prepared. The prepared aqueous solution of sodium hydroxide is dripped continuously to 25000 g acrylic acid having purity of more than 99.5%. The resultant mixture is neutralized, reacted for 20 minutes, and 1000 g acrylamide is added. To the resultant solution, 10100 g bean platinum powder (100-200 meshes) is added, stirred to cool to 50-40 degrees C at the speed of 100-120 rpm, and 8 g methylene bisacrylamide as crosslinker and 10 g ammonium persulfate as initiator are added. The resultant mixture is subjected to graft copolymerization reaction by heating to 65-70 degrees C, and the reaction temperature is controlled at 110-115 degrees C for 15 minutes. The reaction mixture is added to polymerization reactor, aged, polymerized and dried. The obtained solid product is pulverized to obtain super absorbent polymer fertilizer.
NOVELTY - Preparation of rosuvastatin calcium comprises using 3,5-dicarbonyl-6-benzyloxyethylhexanoate as starting material and 2-benzyloxy-N-methoxy-N-methyl-acetamide (V), which is prepared by reacting benzyl alcohol (II) and 2-bromoacetic acid (III) to prepare benzyloxyacetic acid (I), reacting (I) and N,O-dimethylhydroxylamine hydrochloride (IV) to prepare (V).    USE - Preparation of rosuvastatin calcium (claimed).    ADVANTAGE - The method has increased efficiency, convenient quality control and reduced cost, is convenient for industrialization and environment-friendly, reduces the raw materials and energy investment and avoids toxic substances.    DETAILED DESCRIPTION - Preparation of rosuvastatin calcium comprises using 3,5-dicarbonyl-6-benzyloxyethylhexanoate as starting material and 2-benzyloxy-N-methoxy-N-methyl-acetamide of formula (V), which is prepared by reacting benzyl alcohol of formula (II) and 2-bromoacetic acid of formula (III) to prepare 2-(benzyloxy)-acetic acid of formula (I), reacting (I) and N,O-dimethylhydroxylamine hydrochloride of formula (IV) to prepare (V).
NOVELTY - Special liquid medicinal fertilizer comprises active microorganism, fertilizer and pesticide, and further comprises release agent. The medicinal fertilizer comprises 16-24 wt.% active microorganism, 28-31.9 wt.% fertilizer, 1.5-2.5 wt.% pesticide, 5.1-5.5 wt.% release agent, and water (remainder).    USE - The special liquid medicinal fertilizer is useful for increasing medlar yield and degrading insecticidal or pesticidal residue (claimed).    ADVANTAGE - The medicinal fertilizer enables transportation and storage easily and cost-effectively, and exhibits effect for a long period of time even required in less dosage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing special liquid medicinal fertilizer, which involves (a) mixing N-acyl sarcosine, N-acyl glutamate, N-acyl glutamic acid ester and N-alkyl- beta -alkyl aspartic acid ester to obtain water-soluble organic release agent, (b) weighing each of the components, (c) adding active microorganism and organic release agent in reaction kettle, stirring and mixing the components, and maintaining temperature at 25 degrees C for 30 minutes, and (d) then adding the fertilizer and pesticide to the reaction kettle, stirring the components, uniformly mixing the components, and filling the obtained product in bottle.
NOVELTY - Preparation of diethylbutyryl malonate comprises condensing diethyl malonate and butyl chloride in the presence of catalyst and solvent at 65-90 degrees C for 5-9 hours. Temperature is reduced to 30-35 degrees C, reaction solution is washed with 3-5% aqueous alkali, aqueous phase is separated, organic phase is washed with 30-50 ml 45-50 degrees C hot water, solvent is evaporated under normal pressure, and vacuum distillation is carried out at 129-131 degrees C and 1.7 kPa. The mass ratio of diethyl malonate, butyl chloride, catalyst, solvent and alkali is 1:0.8-1.67:0.031-0.125:1.56-3.12:0.13-0.25.    USE - Used as an intermediate (claimed).    ADVANTAGE - The diethylbutyryl malonate is economically prepared with high purity, yield of more than 95% and reduced energy consumption by simple and environmentally-friendly process.
NOVELTY - Oxygen free enclosure device comprises streaming flexible armor, which is flexible and thermally shield, where organic matter is anaerobically fermented under different mesophilic and thermophilic environmental condition. The organic waste is absorbed, and stored in metal or plastic cover to avoid solar radiation. Feeding channel is provided for allowing the organic material and removing gases generated by the decomposion of organic matter.    USE - Oxygen free enclosure device used for anaerobic degradation of organic matter such as organic waste, agricultural waste and industrial waste rich in alternative fuels that is methane, carbon dioxide gas and hydrogen gas.    ADVANTAGE - The oxygen free enclosure device is simple in structure and eco-friendly in nature.
NOVELTY - This utility new type relates to a one micro-bubble excess hydrogen preparing device, belonging to electrolytic device technology field. The device comprise a set with water inlet and water outlet of water container, said inner container set with at least one water for the cathode electrode and the anode electrode, the cathode electrode and the anode electrode in pairs without clearance a hydrophobic porous film, a hydrophobic porous film and a cathode electrode or anode electrode relative area of side surface is less than a negative electrode or a positive electrode area with hydrophobic porous membrane relative side surface, a hydrophobic porous film of thickness less than 5 mm. The device generate a large amount of super-micro air bubble of the hydrogen oxygen produce quantity;
NOVELTY - Method for fermenting biogas involves fermenting human stool, livestock manure, straw, grass, organic substance, and starch, sugar and alcohol industry effluents in closed condition, with suitable amount of water at 8 degrees C and 6.8-7 pH and stirring twice a week to obtain the product, where the fermentation is performed using Enterobacter cloacae and cesspit sludge, as inoculum.    USE - The method is useful for fermenting biogas, which is useful as fertilizer for field crop, vegetable, peanut, fruit and mushroom, and as feed additive for fish and pig (all claimed).    ADVANTAGE - The method improves biogas generation rate and enables to produce with good quality, and has high utilization rate.
NOVELTY - A straw briquette-forming production line device comprises feed conveyor (1), chaff cutter (2), scrap conveyer (3), scraping feeder (4), feed transmission device (5), straw briquetting machine (6), and discharge conveyer (7) in which feed conveyer is fixedly mounted on inlet of chaff cutter using support pole, and scrap conveyer is fixedly mounted on outlet of chaff cutter using support rod.    USE - A straw briquette-forming production line device (claimed).    ADVANTAGE - Straw briquette-forming production line device improves production efficiency and reduces labor cost, and straw briquette is easy to transport and store and has improved energy density and high combustion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram for straw briquette-forming production line device.    Feed conveyor (1)    Chaff cutter (2)    Scrap conveyer (3)    Scraping feeder (4)    Feed transmission device (5)    Straw briquetting machine (6)    Discharge conveyer (7)
NOVELTY - Improving enzymatic saccharification effect of lignocellulosic feedstock, comprises (i) crushing lignocellulosic raw material to a length of not greater than 50 mm, removing the impurities, and adding into a preprocessing section; (ii) transferring pretreatment material to a reactor by a pump, controlling the temperature at 130-160 degrees C, reacting the solution for 1-30 minutes, performing hot washing process, and performing pressure filtration under pressure, to obtain liquid feed to a biogas fermentation section; and (iii) adding 10-200 U/g cellulose to perform enzymatic saccharification, and fermentation.    USE - The lignocellulosic is useful for converting wheat or corn stalks and other agricultural and forestry wastes into bio-based chemicals (methane, xylitol, ethanol, butanol or butanediol).    ADVANTAGE - The method produces product with good detoxification effect (claimed); increases the glass conversion temperature of lignin after being subjected to hot washing process to a higher rate, and the enzymatic liquefaction and saccharification efficiency of the raw material; reduces the utilization rate of raw material, and cellulose; and removes inhibitors produced during enzymolysis and fermentation processes while preprocessing.
NOVELTY - An oil-producing yeast strain i.e. smooth Candida 2A00015 (Candida parapsilosis 2A00015) microorganism strain preserved under preservation number CCTCC M2013354, is new.    USE - As oil producing yeast strain or as mutant strain for producing oil (claimed) such as biodiesel oil.    ADVANTAGE - The strain can be prepared in high yield by using protoplast ultraviolet mutagenesis technology. The strain allows industrial scale production of oil. The oil production rate is increased by more than 20% compared to the original strain. The strain solves the problems of shortage of resources, does not cause environmental deterioration, does not adversely affect human health, can be prepared by simple and cost-effective method, and allows industrial scale production of oil. Using the strain, oil production rate is increased by up to 44.18%.
NOVELTY - Electrolysis involves plating pure platinum metal on titanium electrode, forming electrolytic electrode, placing electrode in tap water, electrifying, decomposing the water into hydrogen ion and oxygen ion under the action of current, producing predetermined amount of hydrogen and oxygen, and discharging.    USE - Electrolysis for producing hydrogen.    ADVANTAGE - Hydrogen is produced by electrolysis method with high current efficiency. The electrode has excellent corrosion resistance, durability and current density.
NOVELTY - Device for producing culture medium comprises housing (1), pedestal (2), feed inlet (3), stirrer (4), driving belt (6), discharge port (7), transmission belt (8) and driving motor (9). One end of housing is provided with the feed inlet. The housing is provided with stirrer. The discharge port is provided at one end of pedestal which is provided with driving motor.    USE - The device is useful for producing culture medium (claimed).    ADVANTAGE - The device is cost-effective, and environmentally-friendly, and enables to produce culture medium with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of culture medium production device.    Housing (1)    Pedestal (2)    Feed inlet (3)    Stirrer (4)    Driving belt (6)    Discharge port (7)    Transmission belt (8)    Driving motor (9)    Gas collection tube (13)    Temperature controller (14)
NOVELTY - Production of microbial fertilizer using enzymolyzed food waste and microbial inoculum/agent, by collecting food waste, crushing collected food waste, sorting out inorganic substances, adding heat-resistant amylase to mixture, incubating mixture, decanting oil, adding glucoamylase to enzymolyzed product, incubating mixture, adding protease and cellulase to hydrolyzed product, incubating product, subjecting hydrolyzed product to solid-liquid separation, adding liquid to sterilized fermenter, adding microbial seed solution to fermenter, and performing fermentation.    USE - The method is useful for production of microbial fertilizer (claimed).    ADVANTAGE - The method enables effective utilization of the food wastes and hence food wastes are effectively reduced and secondary pollution caused by disposal of the food waste is also reduced. The method is cost-effective as the food wastes are used as raw material, and enables conversion of biowaste into microbial fertilizer and high value and wider application prospects.    DETAILED DESCRIPTION - Method for production of microbial fertilizer using enzymolyzed food waste and microbial inoculum or agents, involves collecting food waste, crushing collected food waste, sorting out inorganic substances, adding heat-resistant amylase to obtained mixture, incubating the mixture at 90-100 degrees C for 1-2 hours, decanting oil, adding glucoamylase to cooled enzymolyzed product, incubating mixture at 40-65 degrees C for 1-3 hours, adding protease and cellulase to obtained hydrolyzed product, incubating the product at 30-40 degrees C for 3-7 hours, subjecting obtained hydrolyzed product to solid-liquid separation, subjecting fermenter to high temperature sterilization, adding the liquid to sterilized fermenter, adding microbial seed solution to the fermenter, and allowing fermentation to occur at 25-37 degrees C for 24-48 hours under sealed condition.
NOVELTY - Special fertilizer comprises 2-10 wt.% tung oil, 5-13 wt.% tung oil cake, 2-10 wt.% human excreta, 2-13 wt.% pig manure, 2-12 wt.% cow dung, 5-15 wt.% chicken manure, 7-18 wt.% corn stalk, 3-26 wt.% urea, 12-32 wt.% diammonium phosphate, 10-23 wt.% potassium chloride, and 0.5-5 wt.% humic acid.    USE - The special fertilizer is useful for Camellia (claimed).    ADVANTAGE - The special fertilizer is rich in active organic substances, nitrogen, phosphorus and trace elements, and prepared using easily available raw materials. The method is less labor intensive, and reduces production cost of fertilizer by more than 30%.    DETAILED DESCRIPTION - Special fertilizer comprises 2-10 wt.% tung oil, 5-13 wt.% tung oil cake, 2-10 wt.% human excreta, 2-13 wt.% pig manure, 2-12 wt.% cow dung, 5-15 wt.% chicken manure, 7-18 wt.% corn stalk, 3-26 wt.% urea, 12-32 wt.% diammonium phosphate, 10-23 wt.% potassium chloride, and 0.5-5 wt.% humic acid. The fertilizer is obtained by (a) crushing the above-mentioned tung oil cake to obtain product having mesh size of 10-100, preferably 50-80, mixing the obtained product with tung oil, maintaining the mixture for 2-3 days, adding human excreta to the mixture, and maintaining the obtained product for 4-8 hours, (b) crushing the above-mentioned corn stalk to obtain product having mesh size of 10-100, preferably 20, mixing the crushed product with pig manure, cow dung, chicken manure and humic acid, and fermenting the obtained product, (c) mixing the above-mentioned urea, diammonium phosphate and potassium chloride, and (d) uniformly mixing the products obtained in steps (a)-(c), and regulating water content of the mixture to 14% or less, 1-14% or 5-10%. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves performing the above-mentioned steps (a)-(d).
NOVELTY - Organic fertilizer comprises 20-40 pts. wt. rice bran, 10-15 pts. wt. lees, 15-25 pts. wt. peat, 15-25 pts. wt. soybean meal, 15-20 pts. wt. plant ash, 15-20 pts. wt. corn stalk, 10-20 pts. wt. chicken manure, 10-15 pts. wt. wheat bran, 5-7 pts. wt. ferrous sulfate, 3-6 pts. wt. ammonium sulfate, 6-8 pts. wt. magnesium sulfate, 3-9 pts. wt. borax, 4-7 pts. wt. fulvic acid, 2-6 pts. wt. potassium, 1-4 pts. wt. Bacillus megaterium, 2-5 pts. wt. Myceliophthora thermophila, 3-6 pts. wt. yeast, 4-7 pts. wt. cellulose, and 5-8 pts. wt. Lactobacillus powder.    USE - As organic fertilizer for pomegranate tree (claimed).    ADVANTAGE - The organic fertilizer increases yield and sugar content of pomegranate, and is environmentally-friendly.
NOVELTY - Organic liquid fertilizer comprises 50-60 wt.% eel bone slurry, 10-15 wt.% soybean meal, 5-8 wt.% bone meal, 15-20 wt.% sugar and 3-6 wt.% mother liquor.    USE - The organic liquid fertilizer is useful for promoting the growth of plants.    ADVANTAGE - The fertilizer improves soil fertility and enhances absorption of nutrients by plants, and develops disease resistance in plants.
NOVELTY - Preparing a soil modifying agent comprises (a) inoculating a composite strain comprising Rhodopseudomonas palustris, Lactobacillus lactis, Streptococcus and beer yeast in a culture medium for carrying out anaerobic fermentation to obtain fermented composite strains, and (b) inoculating the fermented composite strains in a fermentation medium to carry out anaerobic fermentation to obtain soil modifying agent.    USE - The method is useful for preparing a soil modifying agent, which is useful for repairing soil (all claimed).    ADVANTAGE - The method is capable of simply and economically preparing the soil modifying agent with reduced water resource consumption in an industrial and eco-friendly manner.    DETAILED DESCRIPTION - Preparing a soil modifying agent comprises (a) inoculating a composite strain comprising Rhodopseudomonas palustris, Lactobacillus lactis, Streptococcus and beer yeast in a culture medium for carrying out anaerobic fermentation to obtain fermented composite strains, and (b) inoculating the fermented composite strains in a fermentation medium to carry out anaerobic fermentation to obtain soil modifying agent. The weight ratio of the composite strain to the culture medium is 0.5-10:90-99.5. The total weight of the composite strains and the fermentation medium is 10-20 wt.%. The fermentation medium comprises 20-50 wt.% of a substrate carrier, 10-15 wt.% of Bacillus fermentation waste liquid, 10-20 wt.% of industrial culture medium, 2-5 wt.% of soil extract, 0.5-1 wt.% of growth factor solution and balance amount of water. An INDEPENDENT CLAIM is included for a soil culture medium prepared by the method.
NOVELTY - The reactor has a reference electrode (3) that is fixed in a side opening of a reaction tank (5). A lower portion of biological cathode (6) is immersed in the liquid of reaction tank. An anode room (7) is located in the reaction tank. An anode (8) is located in the anode room in reaction tank. A bottom portion of a reaction tank is provided with a water inlet, and top portion is provided with an exhaust port (9) and a water outlet.    USE - Bio-electrochemical in-situ marsh gas purifying reactor used in anaerobic biogas purifying system.    ADVANTAGE - The organic load and cathode potential are adjusted continuously so as to achieve optimum anaerobic biogas purification performance. The biological method and in situ method are incorporated for biogas purifying process, so as to reduce emission of methane and carbon, while simplifying the biogas purifying system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for in-situ marsh gas purifying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-electrochemical in-situ marsh gas purifying reactor.    Reference electrode (3)    Reaction tank (5)    Biological cathode (6)    Anode room (7)    Anode (8)    Exhaust port (9)
NOVELTY - Bio-organic fertilizer comprises 25-50 pts. wt. edible waste, 20-40 pts. wt. livestock manure, 0.5-8 pts. wt. organic material fermenting agent, and 5-12 pts. wt. of biologically active substances, where the fertilizer is prepared by mixing edible waste with livestock manure, adding organic material fermenting agent, mixing, carrying out thermophilic aerobic fermentation for 10-30 days, mixing the fermented materials and biologically active substances, grinding and then drying.    USE - The bio-organic fertilizer is useful for saline-alkali farmland.    ADVANTAGE - The fertilizer is rich in nutrients, and improves quality of saline-alkali soil and crops.
NOVELTY - A multi-stage alternately one a process sewage of a microorganism, by at least three level generating system, a machine base, a platform part is composed of five III level biological generating system (3) is connected with a machine base, a machine base and two level biological system are set with the liquid inlet pump (22), a fan (18), a lower platform, a machine base part is the aeration tank, wherein a single microorganism include a constant temperature room, the kettle, a heater and a line, the kettle (10) with inner constant temperature room (11), a constant-temperature room (11) through liquid inlet overflow joint (12) is connected with the liquid inlet (13), an overflow tube (14) connecting the lower part air inlet through the liquid outlet joint (15) is connected with the air inlet (16) and liquid outlet (17) connecting the liquid inlet (13) is connected with the liquid inlet pump (22) connecting the air inlet (16) and the fan (18) connect, the kettle (10) is provided with a heater (19), a part with a discharge tube (20) and liquid tube (21). This utility new type processing effect is good, and is greatly reduced in sewage treatment sludge amount.
NOVELTY - This utility new type claims a one microwave cracking furnace, comprise a furnace body, a seal plate and heat preservation layer, said seal plate set in said furnace body, said insulating layer is covered on the said furnace body, a furnace body and a heat insulating layer between the set with one used for containing microwave absorbent of absorbing cavity, a seal plate of said absorbing cavity part is opened with a material entrance, a heat insulating layer of the lower part is provided with a material exit. This utility new type supply through a microwave cracking furnace on one hand increase the cracking efficiency, and solves the problem that the existing microwave absorbent is not easy to a residue of technology, is efficient clean utilization of biomass energy is made.
NOVELTY - One kind of low concentration ammonia nitrogen waste water of biological strengthening treatment device, wherein provided with regulation pool, water pump for, anoxic area, sediment one zone, an aeration biologic fluidization bed zone, air blower, mixed liquid relux pump, second sediment, rest sludge discharge pump, regulating pool by water pump for water inlet, water valve for, for water flow meter, water pump and anoxic area for connection, anoxic zone through water hole and sediment by one cell connected with the sediment area through one through hole and water aeration biologic fluidization bed connected with the aeration biologic fluidization bed zone through water hole and to sediment the second area connected, via relux pump in water inlet, inner relux valve, inside relux flow meter, in relux pump, relux pump in the water outlet anaerobic zone and connected with. The supply of one of high efficient, economic, stable, remaining sludge at least in the low concentration ammonia nitrogen waste water of biological strengthening treatment device.
NOVELTY - Waste raw material containing biomass and plastics is dried, crushed, heated and pressure of 10 MPa or more is applied, to obtain waste material molded component.    USE - Manufacture of waste material molded component (claimed) used as fusion heat source in waste material melting furnace.    ADVANTAGE - The method enables manufacture of waste material molded component having high strength, without thermally decomposing and disintegrating during process. The volatilization of volatile component and scattering to outside of the waste material melting furnace is suppressed.
NOVELTY - Producing solid fuels from peat, comprises reducing size of peat, drying peat, heating the dried peat in the absence of oxygen, cooling, and converting the cooled peat into briquettes. The heating step is carried out at a temperature of 200-350 degrees C for 10-60 minutes in the presence of superheated steam, nitrogen or other inert gases, under atmospheric pressure.    USE - The method is useful for producing solid fuels from peat (claimed).    ADVANTAGE - The method is capable of economically and rapidly producing the solid fuels with reduced moisture content, oxygen content and volatile substances, increased carbon content, and high calorific value.
NOVELTY - A liquid biofuel for stoves/ovens using the principle of gasifying fuel before combustion, comprises either 0-20% methanol, 3-20% water, 1-2% additives, and ethanol sufficient to make 100%; or 25-50% ethanol, 3-10% water, 1-2% additives, and methanol sufficient to make 100%.    USE - As liquid biofuel which is useful for stoves/ovens using the principle of gasifying fuel before combustion (claimed).
NOVELTY - The method involves solidifying liquefied slag into solidified slag within a gasifier (10). An actuator (66) is operated in a manner causing a slag breaker of the gasifier to move from a neutral position into contact with the solidified slag for breaking the solidified slag into chunks, where the slag breaker comprises an opening through which the solidified slag extends prior to being broken into chunks by the movement of the slag breaker, and the actuator causes the slag breaker to move in one direction from the neutral position and in an opposite direction from the neutral position.    USE - Method for operating a gasifier during gasification process of fuels such as wood and grass, biofuels and petroleum based fuels.    ADVANTAGE - The slag breaker allows slag accumulation within the gasifier to reach an equilibrium and eliminates the need to periodically shutdown the gasifier to remove solidified slag accumulations. The broken slag stalactite chunks are small, and can be removed from the gasifier much more easily than a solidified blob of slag or slag that is solidified while in contact with a surface of a component of the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a gasifier.    Gasifier (10)    Thermocouples (44)    Water injection system (46)    Water lines (50)    Actuator (66)
NOVELTY - Composition comprises 20-80 wt.% aerosol concentrate and 20-80 wt.% aerosol propellant. The aerosol concentrate contains 1-30 wt.% alkanolamide as zwitterionic surfactant and 0.1-0.5 wt.% thickener.    USE - The composition is useful for skin cooling and cleansing (claimed).    ADVANTAGE - The composition soothes skin during summer, shrinks skin pores, instantly lowers skin temperature, removes makeup, and contains alkanolamide and propellant having low boiling point.
NOVELTY - An electrode comprises photocatalyst particle (10) containing oxynitride, nitride, oxysulfide, and/or sulfide as photocatalyst and semiconductor or good conductor (30) positioned between photocatalyst particles and between photocatalyst particle and support body (20). Electrode is deposited on support body. Semiconductor or good conductor is material which does not catalyze paired reaction of reverse reaction of water-splitting reaction and water-splitting reaction of photocatalyst.    USE - An electrode for light water-splitting reaction (claimed) used for hydrogen manufacturing apparatus.    ADVANTAGE - Internal resistance of electrode can be reduced, and photoelectric conversion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an expanded sectional view of the electrode.    Photocatalyst particle (10)    Support body (20)    Semiconductor or good conductor (30)
NOVELTY - The plant (1) has heat input devices (5a, 5b) for heating biomass in an interior region of transport devices (2a, 2b). The transport devices are arranged at an inner side of the heat input devices, and separate the airtight biomass from the heat input devices that are designed as heat exchangers. The transport devices comprise a specific gasification performance heat exchange surface area. A suction device sucks raw gas. Two cross conveyers are provided as the transport devices. The first cross conveyor preheats the biomass. The second cross conveyor gasifies the biomass.    USE - Biomass gasification plant for producing gas for a gas engine and a drive of a vehicle.    ADVANTAGE - The transport devices comprise the specific gasification performance heat exchange surface area, so that current is produced by using a compound system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass gasification plant.    Biomass gasification plant (1)    Transport devices (2a, 2b)    Reduction container (3)    Heat input devices (5a, 5b)    Pipeline (10)
NOVELTY - The monitoring device (10A) has a probe (22) for laser light reception, which receives the Raman scattered light (23). A fuel cell electric-power is generated by fuel gas (12) supplied to a fuel cell (11). An oxidizing agent (13) is supplied, such that the fuel gas is opposed to an exterior of the fuel cell. A laser light transmission unit (26) is provided for transmitting laser beam (21) through an optical fiber (25).    USE - Monitoring device for use inside a fuel cell cartridge.    ADVANTAGE - The monitoring device has a probe for laser light reception, which receives the Raman scattered light, and hence ensures accurate and improved monitoring device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a monitoring device. (Drawing includes non-English language text).    Monitoring device (10A)    Fuel cell (11)    Fuel gas (12)    Oxidizing agent (13)    Laser beam (21)    Probe (22)    Raman scattered light (23)    Optical fiber (25)    Laser light transmission unit (26)    Fuel cell cartridge (100)
NOVELTY - The equipment has a flat-plate type solar collector (1) that is provided with a set of copper pipes that are covered with a transparent glass to heat the water in copper pipes. A flow rate control valve (2) is connected to top surface of the solar collector arranged below the biogas reactor. The copper pipes are connected to flow rate control valve. The coil pipes (3) are arranged in a circular manner from top to bottom of biogas reactor. The flow rate control valve maintains the temperature of reactor below 51 degrees C.    USE - Solar power equipment for increasing production speed of biogas from livestock waste, for use with biogas reactor.    ADVANTAGE - The biogas can be produced quickly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of solar power equipment.    Solar collector (1)    Flow rate control valve (2)    Coil pipes (3)    Livestock waste (4)    Burner (7)    Water (8)
NOVELTY - The modular fuel cell system has power module which is arranged in row on a base (20). A fuel processing module (16) and power conditioning module (18) are arranged on one end of the row on the base. The power module has cabinet (10,12) that is set with fuel cell stack located in hot box. The power module is electrically and fluidly connected to the fuel processing and the power conditioning modules through the base.    USE - Modular fuel cell system installed in loading dock, narrow alley or space between buildings.    ADVANTAGE - The fuel cell system is set to provide reliable generation of power, flexibility of fuel processing and flexibility of power output voltages and frequencies with single design.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the modular fuel cell system.    Cabinets (10,12)    Fuel processing module (16)    Power conditioning module (18)    Base (20)    Door (30)
NOVELTY - Kitchen garbage recycling method, involves (a) sorting kitchen garbage, (b) adding water containing salt to the kitchen garbage, heating and stirring the mixture, and (c) diluting the garbage water, performing aerobic solid fermentation, drying the obtained product, separating liquid oil and water to generate biogas, liquid state fertilizer, and marsh gas as fuel.    USE - Kitchen garbage recycling method for generating biogas, liquid state fertilizer, and marsh gas as fuel (claimed).    ADVANTAGE - The method is harmless and simple, and requires less investment.
NOVELTY - Preparation of 4-chloro-4'-hydroxybenzophenone involves adding chlorobenzene and anisole as raw materials into a reactor, stirring uniformly at room temperature, adding aluminum chloride and p-chlorobenzoyl chloride, mixing uniformly at 35-45 degrees C, increasing temperature of the resultant solution to 45-55 degrees C, carrying out Friedel-Crafts reaction for 2 hours, obtaining reaction solution, removing methyl group by performing direct heating methyl group at 130-140 degrees C for 2 hours, and cooling.    USE - Preparation of 4-chloro-4'-hydroxybenzophenone (claimed).    ADVANTAGE - The method provides 4-chloro-4'-hydroxybenzophenone with high yield and purity, by simple, economical and environmentally-friendly process.
NOVELTY - Decomposing banana leaves, bagasse and other agricultural wastes into cellulose and lignin, comprises introducing microorganism into banana leaves, bagasse and other agricultural wastes to produce cellulase, lignin and other metabolic products, then adding an accelerating agent, and decomposing at 65-75 degrees C for 12-18 days and at 55 degrees C for 8-10 days, is claimed.    USE - The method is useful for decomposing banana leaves, bagasse and other agricultural wastes into cellulose and lignin (claimed).    ADVANTAGE - The method rapidly and efficiently decomposes the banana leaves, the bagasse and the other agricultural wastes.
NOVELTY - Preparing 4-(chloromethyl)-N-(4-methyl-3-((4-(3-pyridyl)pyrimidin-2-yl)amino)phenyl)benzamide (III), comprises suspending 4-methyl-N3-(4-(3-pyridyl)pyrimidin-2-yl)benzene-1,3-diamine (I) in an aqueous solution of an inorganic base and an organic solvent and dropping 4-(chloromethyl)benzoyl chloride (II) at a temperature of -20 degrees C to 40 degrees C, and then heating the mixture at a temperature of 0-60 degrees C for 1-24 hours, filtering the reaction solution, and washing with water.    USE - The process is useful for preparing (III), which is useful as an intermediate for preparing imatinib (claimed).    ADVANTAGE - The process ensures simple, rapid and convenient preparation of (III) with high yield of 88-94.6% in a cost effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing 4-(chloromethyl)-N-(4-methyl-3-((4-(3-pyridyl)pyrimidin-2-yl)amino)phenyl)benzamide of formula (III), comprises suspending 4-methyl-N3-(4-(3-pyridyl)pyrimidin-2-yl)benzene-1,3-diamine of formula (I) in an aqueous solution of an inorganic base and an organic solvent and dropping 4-(chloromethyl)benzoyl chloride of formula (II) at a temperature of -20 degrees C to 40 degrees C, and then heating the mixture at a temperature of 0-60 degrees C for 1-24 hours, filtering the reaction solution, and washing with water.
NOVELTY - A lornoxicam is prepared by using 5-chloro-3-chlorosulfonyl-2-thiophenecarboxylate as raw material, condensing with presence of acid-binding agent and sarcosine methyl ester hydrochloride to obtain 1st intermediate, performing cyclization reaction of 1st intermediate in sodium alkoxide solution to generate 2nd intermediate, and performing amidation of 2nd intermediate in xylene with 2-aminopyridine in which acid binding agent is triethylamine, pyridine, methylamine, dimethylamine, methanol, sodium methoxide, sodium ethoxide, sodium hydroxide, sodium carbonate, or sodium bicarbonate.    USE - Preparation of lornoxicam (claimed).    ADVANTAGE - Preparation process has short synthesis route, low toxicity and pollution, simple operation, and high product purity and yield and is environment-friendly, safe, and low-cost.    DETAILED DESCRIPTION - A lornoxicam of formula (III) is prepared by using 5-chloro-3-chlorosulfonyl-2-thiophenecarboxylate of formula (I-1) as raw material, condensing with presence of acid-binding agent and sarcosine methyl ester hydrochloride to obtain 1st intermediate of formula (I), performing cyclization reaction of 1st intermediate of formula (I) in sodium alkoxide solution to generate 2nd intermediate of formula (II), and performing amidation of 2nd intermediate of formula (II) in xylene with 2-aminopyridine of formula (I-2) in which acid binding agent is triethylamine, pyridine, methylamine, dimethylamine, methanol, sodium methoxide, sodium ethoxide, sodium hydroxide, sodium carbonate, sodium bicarbonate, potassium hydroxide, potassium carbonate, or potassium bicarbonate..
NOVELTY - Wherein technology area of plastic bottle recycling this utility new model relates to in industry and environmental protection, especially a kind of automatic receiving one bottle machine, comprising upper machine body, wherein the machine body side wall provided with the bottle, electronic screen and can print the print receipt, internal body passage is provided with the bottle mouth and connect, channel side can check detector provided with the bottle, inner passage lengthways set with steel needle and can lengthways move back, and upper side channel position and set with steel needle corresponding to the each steel needle hole, channel two side is set with can inwards extrusion and extrusion board, the lower channel provided with storage tank, and between storage tank and passage set with can opening and closing the channel baffle plate. Wherein the same when provided with multi-group feeding bottle can make multi-number user for use at the same time, reducing waste of time, increasing efficiency. The utility model can automatically updated to complete recovery and print receipt of bottle providing reward, and structure is simple, can to complete extrusion and bottle, for storage quantity is big bottle.
NOVELTY - This utility new type relating to energy utilization field, specifically, referring to a biological gas a power one interaction device. Include the fermentation tank, the fermentation tank is a cylinder, fermenting tank set with heating layer, used for holding inner fermentation tank a temperature constant; one side of the fermentation tank set with a feeding port, one side upper part of a fermentation tank set with an air outlet, inner fermentation tank set with long shaft stirrer, stir for fermentation raw material of inner fermentation tank. This utility new type biological gas heat electric interaction device, through a preprocessing in the raw material pre-rear, and then fermentation tank of heating layer set with inner tank of the fermentation temperature constant holding at 40 degrees C degrees centigrade, after a uniform stir, low in the absence of oxygen of fermentation tank dark environment, the organic matter of decomposition. Such a way would firstly the raw material of harmful substance in the treatment process, the raw material would likely exist in harmful substance so as to influence to fermenting effect.
NOVELTY - This new utility model provide a kind of can at the same time finish one material liquid stirring and cracking, promoting automatic cracking stirring marsh gas pool sealing material and liquid fermentation. When it comprises pool main body, and is set with main pool body at one side of water pressure in main pool body and upper end of skylight, main pool body gas, liquid level upper part is gas storage chamber, the lower part is fermentation chamber, lower end is set with skylight feedstock tube, wall feedstock pipe support in main pool body is set with the bottom of the cloth wall present hollow column is set with fermentation chamber in middle, upper cloth wall side wall is opened with multiple hole way, inside set with hydraulic circulation pump, a gas storage room inside has set with circle pump and liquid outlet mouth connected and breaking nozzel. Feedstock via pipe set up in the sky window, not only can solve the sealing problem of sky window, to make the original the same cover sealing the main pool body biogas is improved automatically sealing, not only solves the skylight is not easy to seal the problem, but also can realize the automatic pressure regulation to prevent to pressure and negative pressure to marsh gas pool and cause damage, and for feeding and skylight combination.
NOVELTY - The system has garbage stacking chamber from which garbage is conveyed to cutting system through transmission belt. The cutting system is provided for cutting and crushing the conveyed garbage. A mixing stirrer is provided for mixing crushed garbage. The crushed garbage material is mixed by compressor to obtain mixed fuel cake in lower portion of compressor. The mixed fuel cake is conveyed to drying room for water drying process. The dried mixed fuel cake is again dried using decomposing machine for forming granular fuel structure that is stored in finished product bin.    USE - Waste water-garbage treatment system installed in hydraulic power station.    ADVANTAGE - The waste water-garbage treatment system is provided with improved treating efficiency, reduced pollution to environment, reduced treating time and improved economic efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste water treatment system. (Drawing includes non-English language text)
NOVELTY - Treating wastes generated from animals and plants, comprises (i) laying the materials in sheet form, and uniformly digging a predetermined area of the ground to a predetermined depth to lay a concave portion of a first waterproof sheet on the ground; (ii) adding a soil into a predetermined depth to form a foundation soil; (iii) stacking animal and plant wastes to a predetermined thickness of on the foundation soil to form a waste layer; (iv) covering the soil from the ground with a second waterproof sheet, and the stacked waste matter layers; and (v) curing for a predetermined number of days.    USE - The method is useful for treating wastes generated from animals and plants (claimed).    ADVANTAGE - The method is environmental friendly (claimed), simple, and suitable for large-scale processing procedure; does not require to perform specialized processing conditions; and inhibits the generation of bad odor.
NOVELTY - Method for fertilizing Asparagus seedlings, involves (a) selecting fertile soil, (b) fertilizing soil using 1-2 tons sheep manure, 2-3 tons pig manure, 2-3 tons chicken manure, 4-5 tons mushrooms, and 4-5 tons waste litter and planting Asparagus, and (c) applying organic fertilizer to the seedlings and harvesting seedlings.    USE - The method is useful for fertilizing Asparagus seedlings (claimed).    ADVANTAGE - The method improves soil texture and quality, and increases yield of Asparagus seedlings and fertility of the soil.
NOVELTY - Preparing a plant source pesticide comprises crushing dried Polygonum cuspidatum flower and then sieving, adding methanol to the flower powder and then extracting for 3 times, combining the extracting liquids and then concentrating and drying to obtain total extract, ultrasonically extracting the total extract using petroleum ether and diethyl ether, dissolving the diethyl ether extract into 1-3 times of acetone and then purifying by silica gel column chromatography, eluting the mixture using petroleum ether and acetone and concentrating the eluate under reduced pressure and drying.    USE - The method is useful for preparing a plant source pesticide (claimed).    ADVANTAGE - The plant source pesticide has good human and animal safety, does not pollute the environment, and is not easy to cause drug resistance, and easy to degrade in the natural environment.    DETAILED DESCRIPTION - Preparing a plant source pesticide comprises crushing dried Polygonum cuspidatum flower using a crusher and then sieving through 40 meshes sieve, adding 3-6 times of methanol to the flower powder and then extracting for 3 times at an interval of 6 hours, combining the extracting liquids and then concentrating and drying to obtain total extract, ultrasonically extracting the total extract using 5-8 times of petroleum ether for 3 times at an interval of 0.5 hours to remove impurities, ultrasonically extracting the total extract using 5-8 times of diethyl ether for 3 times at an interval of 0.5 hours to remove impurities, dissolving the diethyl ether extract into 1-3 times of acetone and then purifying by silica gel column chromatography (200-300 meshes of silicon gel), eluting the mixture using petroleum ether and acetone as eluent and concentrating the eluate under reduced pressure and drying to obtain pesticide. The volume ratio of the petroleum ether to acetone is 50:1-to 2:1.
NOVELTY - The system has a rubbish stacking chamber, a sterilizing room, a cutting system, a mix stirrer, a compressor, a drying room, and a finished product bin. The rubbish stacking chamber is connected with the sterilizing room, and the rear portion of the sterilized rubbish is sent to the cutting system through a conveying belt. The crushed rubbish is passed through the mix stirrer and combustion improver comprising adhesive material bonding agent. The mix fuel cake is sent to the water drying room for removing water, and the dried fuel cake is stored in the finished product bin.    USE - Sterile water surface rubbish processing system used in hydropower station.    ADVANTAGE - The sterile water surface rubbish is converted into a new fuel. The rubbish processing system forms fine fuel of uniform specification, avoids secondary pollution and protects the environment. The rubbish processing system is feature with wide social value and high economic value.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of sterile water surface rubbish processing system. (Drawing includes non-English language text)
NOVELTY - Topiramate tablet core composition comprises 50 pts. wt. topiramate, 50-200 pts. wt. microcrystalline cellulose, 50-100 pts. wt. starch, 10-40 pts. wt. sodium carboxymethyl starch, 1-5 pts. wt. magnesium stearate, 5 pts. wt. povidone K30, and 100-500 ml of 50% ethanol solution.    USE - Topiramate tablet core composition (claimed).    ADVANTAGE - The topiramate tablet core composition has good curative effect, and can be prepared with simple, low cost and industrial production manner, and without environmental pollution.    DETAILED DESCRIPTION - Preparing topiramate tablet comprising mixing povidone K30 and 5-50% of ethanol solution to obtain a binder, uniformly mixing topiramate, starch, microcrystalline cellulose and sodium carboxymethyl starch to obtain mixed powder, adding the binder into 5/7-8/13 parts of mixed powder to obtain a soft material, heating the soft material, sieving, granulating and drying the material to obtain a primary particle, adding the rest of mixed powder and the binder in a granulation fluidized bed, granulating and drying to obtain secondary granules, mixing the primary particle, the secondary granules, magnesium stearate, microcrystalline cellulose and remaining amount of sodium carboxymethyl starch to obtain a mixture, pressing and tableting the mixture after determining topiramate content, and then packaging in a clothing bag.
NOVELTY - The method involves entering domestic rubbish material into a heat treatment furnace. A rubbish degradation pneumatic unit is connected with a first pipeline (8). Rubbish seepage filtered liquid is entered into a landfill leachate collecting tank through a second pipeline (10). Marsh gas is filled in a chemical pneumatic biogas fermenting tank (7) through a marsh gas output pipeline (12). An air blower component (3) is fixed with a pyrolysis and gasification furnace (4) that is connected with a combustion system (5).    USE - Method for removing nitrogen oxide in cement kiln flue gas of a domestic waste self-ammonia source.    ADVANTAGE - The method enables avoiding external ammonia source and processing system, reducing processing cost, providing green and environment-friendly and ensuring usage safety and reliability and nitrogen oxide discharging rate less than 100mg/Nm3.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic block diagram illustrating a method for removing nitrogen oxide in cement kiln flue gas of a domestic waste self-ammonia source.    Air blower component (3)    Pyrolysis and gasification furnace (4)    Combustion system (5)    Chemical pneumatic biogas fermenting tank (7)    Pipelines (8, 10)    Marsh gas output pipeline (12)
NOVELTY - Ammonia desulfurization process during the production of monosodium glutamate comprises carrying out evaporation and concentration process of fermentation liquid containing high ammonia-nitrogen wastewater to produce condensed water, collecting the condensed water into a storage tank through a pipeline, then passing the condensed water into an ammonia desulfurization device, carrying out ammonia desulfurization process, and emitting the smoke gas through a power plant chimney.    USE - The ammonia desulfurization process is useful in electric power plant.    ADVANTAGE - The ammonia desulfurization process is water-saving, energy-saving and eco-friendly process, and has improved resource utilization, good popularization and application value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for performing ammonia desulfurization process comprising a fermentation liquid evaporation exit and a condensed water storage tank entrance connected to a fermentation liquid evaporation concentrate device through a condensed water collecting pipeline. The condensed water collecting pipeline is connected with the condensed water storage tank through the ammonia desulfurization device and power plant chimney.
NOVELTY - The film has a high polymer main body provided with a protein inducing positive silicon acid ethyl ester mineralizing filler. Thickness of a polyoxyethylene type high molecule-inorganic hybridized film body is 85-105 microns. Mass ratio of the polyoxyethylene type high molecule is 1: 0-0.3. A polyether polyamide block copolymer is provided with the polyoxyethylene type high molecule that is provided with a polyoxyethylene chain segment, where mass fraction of the polyoxyethylene chain segment is 55-80 percentage.    USE - Polyoxyethylene-type high molecule inorganic hybrid film for carbon dioxide/methane gas separation field.    ADVANTAGE - The film has more controllable preparation process with better mild condition, and achieves better gas separation effect with 19.5-66 selectivity and 84-281 barrer permeability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a polyoxyethylene-type high molecule inorganic hybrid film preparation method    (2) an application of a polyoxyethylene-type high molecule inorganic hybrid film.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating a preparation method of polyoxyethylene-type high molecule inorganic hybrid film.
NOVELTY - Preparation of peanut straw absorbing material, involves: (1) selecting of mature peanut straw, cleaning, washing with distilled water, crushing, and drying; (2) grinding the dry peanut straw into powder, and sieving, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting; (4) adding sodium hydroxide solution, reacting, neutralizing; (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea, re-soaking in deionized water, and reacting; (6) filtering solution and washing with deionized water, drying.    USE - The method is useful for preparing peanut straw absorbing material (claimed).    ADVANTAGE - The method prepares peanut straw absorbing material in a simple, time-efficient, cost-effective and environment-friendly manner, and where the material has enhanced heavy metal absorbing ability in waste water.    DETAILED DESCRIPTION - Preparation of peanut straw absorbing material, involves: (1) selecting of mature peanut straw, cleaning, crushing, and drying at 80 degrees C; (2) grinding the dry peanut straw into powder, and sieving through 60 mesh, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting at 35-50 degrees C for 1-2 hours; (4) adding 0.05-0.1 mol/L potassium hydroxide (KOH) solution, reacting for 30-60 minutes, then the solution is neutralized by diluting with sulfuric acid (H2SO4); (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea at 1:1, re-soaking in deionized water, and reacting at 50 degrees C for 5-10 hours; (6) filtering solution and washing with deionized water or 95% alcohol 3-4 times to remove residual ionic liquid, drying at 50 degrees C to obtain a peanut straw adsorbent material.
NOVELTY - Preparation of tomato straw absorbing material, involves: (1) selecting of ripe tomatoes high long straw, cleaning, washing with distilled water, crushing, and drying; (2) grinding the dry tomato straw into powder, and sieving, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting; (4) adding sodium hydroxide solution, reacting, neutralizing; (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea, re-soaking in deionized water; (6) filtering solution and washing with deionized water, drying.    USE - The method is useful for preparing tomato straw absorbing material (claimed).    ADVANTAGE - The method prepares tomato straw absorbing material in a simple, time-efficient, cost-effective and environment-friendly manner, and where the material has enhanced heavy metal absorbing ability in waste water.    DETAILED DESCRIPTION - Preparation of tomato straw absorbing material, involves: (1) selecting of mature tomato straw, soaking in water and cleaning to remove dirt and dust, and drying at 80 degrees C; (2) grinding the dry tomatoes straw into powder, and sieving through 60 mesh, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting at 35-50 degrees C for 1-2 hours; (4) adding 0.05-0.1 mol/L potassium hydroxide (KOH) solution, reacting for 30-60 minutes, then the solution is neutralized by diluting with sulfuric acid (H2SO4); (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea at 1:1, re-soaking in deionized water, and reacting at 50 degrees C for 5-10 hours; (6) filtering solution and washing with deionized water or 95% alcohol 3-4 times to remove residual ionic liquid, drying at 50 degrees C to obtain a tomato straw adsorbent material.
NOVELTY - A sulfonated polyether-ether-ketone amidogen modified titanium nano-tube hybrid film comprises sulfonated polyether-ether-ketone and amidogen modified titanium oxide nano tube in a mass ratio of 0.92-0.99:0.08-0.01, where the film has a thickness of 55-80 microns.    USE - Sulfonated polyether-ether-ketone amidogen modified titanium nano-tube hybrid film for separating carbon dioxide and methane gas.    ADVANTAGE - The hybrid film is prepared in an easy manner with high selectivity and permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a sulfonated polyether-ether-ketone amidogen modified titanium nano-tube hybrid film, which involves performing hydrothermal reaction on rutile titanium dioxide and 3-(methacryloyloxy) propyl trimethoxy silane to obtain the double bond modified titanium oxide nano tube and modifying the titanium oxide nano tube with 1-vinyl imidazole under the action of cross-linking agent and initiator to prepare the amidogen modified titanium oxide nano tube, mixing the amidogen modified titanium oxide nano tube with sulfonated polyether-ether-ketone solution through a flow casting technique to obtain the hybrid film.
NOVELTY - Preparation of sesame straw absorbing material, involves: (1) selecting of mature high long sesame straw, cleaning, washing with distilled water, crushing, and drying; (2) grinding the dry sesame straw into powder, and sieving, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting; (4) adding sodium hydroxide solution, reacting, neutralizing; (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea, re-soaking in deionized water; (6) filtering solution and washing with deionized water, drying.    USE - The method is useful for preparing sesame straw absorbing material (claimed).    ADVANTAGE - The method prepares sesame straw absorbing material in a simple, time-efficient, cost-effective and environment-friendly manner, and where the material has enhanced heavy metal absorbing ability in waste water.    DETAILED DESCRIPTION - Preparation of sesame straw absorbing material, involves: (1) selecting of mature high long sesame straw, soaking in water and cleaning to remove dirt and dust, and drying at 80 degrees C; (2) grinding the dry sesame straw into powder, and sieving through 60 mesh, collecting powder; (3) leaching the collected powder in deionized water, adding and activating amylase, reacting at 35-50 degrees C for 1-2 hours; (4) adding 0.05-0.1 mol/L potassium hydroxide (KOH) solution, reacting for 30-60 minutes, then the solution is neutralized by diluting with sulfuric acid (H2SO4); (5) filtering the obtained liquid in (4) and drying, mixing the dried powder with urea at 1:1, re-soaking in deionized water, and reacting at 50 degrees C for 5-10 hours; (6) filtering solution and washing with deionized water or 95% alcohol 3-4 times to remove residual ionic liquid, drying at 50 degrees C to obtain a sesame straw adsorbent material.
NOVELTY - Manufacture of solid acid catalyst involves pretreating grains or beans, grinding, drying at 40-120 degrees C for 0.5-4 hours, carbonizing the dried product in a muffle furnace at 200-600 degrees C for 30 minutes to 4 hours to form activated carbon carrier, immersing activated carbon carrier in concentrated sulfuric acid, sulfonating at 60-120 degrees C for 1-4 hours, stirring at rate of 50-800 rpm, washing sulfonated product with water such that pH is 7, mixing the product with metal particles, zeolite and binder, wet granulating to obtain spherical granulated solid particles, calcining, and cooling.    USE - Manufacture of solid acid catalyst used for promoting biodiesel oil (claimed).    ADVANTAGE - The method enables efficient and economical manufacture of solid acid catalyst with excellent activity by simple method.    DETAILED DESCRIPTION - Manufacture of solid acid catalyst involves pretreating grains or beans, grinding, drying at 40-120 degrees C for 0.5-4 hours, carbonizing the dried product in a muffle furnace at 200-600 degrees C for 30 minutes to 4 hours to form activated carbon carrier, immersing activated carbon carrier in concentrated sulfuric acid, sulfonating at 60-120 degrees C for 1-4 hours, stirring at rate of 50-800 rpm, washing sulfonated product with water such that the pH is 7, mixing the product with metal particles, zeolite and binder in ratio of 1:0.05-0.1:0.1-0.3:0.05-0.1, wet granulating to obtain spherical granulated solid particles, calcining at 100-500 degrees C for 30 minutes to 4 hours in a muffle furnace, and cooling. The ratio of activated carbon and concentrated sulfuric acid is 1 g:5-15 ml.
NOVELTY - The system has a selecting plant, a pneuma plant, a refuse derived fuel (RDF) plant and a filling plant. RDF plant has a fuel dumps, a RDF incinerator, a high-temperature flue gas discharge device, a heat water circulation passage, and a steam pipes. Heat exchange rear produces low temperature for furnace cooling, and forms high temperature for waste heat circulation. Steam pipe and the other end turbogenerator is connected at one end communicating with RDF incinerator. RDF incinerator steam pipe produces high-temperature steam through the input turbine generator as a power generation sources.    USE - Resource recycling system for domestic garbage and municipal sludge in garbage processing field.    ADVANTAGE - Reduces household garbage and municipal sludge, sustainable operation at low cost, achieves considerable economic and environmental benefits, and has long-term or even permanent use with industrial applicability by the resource recycling system.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow chart of the resource recycling system. (Drawing includes non-English language text).
NOVELTY - This utility new type lower claims a garbage mixer of one heating mechanism, comprise: heat conducting oil heater (1), (2), stir tank (3), the oil tube (4) and the oil tube (5), a heat conducting oil heater (1) is inner set with electric heating tube (6), heater (1) upper end is opened with oil hole, a heater (1) end is provided with oil hole, a stir tank (3) comprise shell and set in the shell of inner shell, outer shell and the inner shell form heating interlayer, said oil outlet tube (4) one end connecting the oil hole, and the other end a lower end in said shell, said oil inlet tube (5) one end connecting the oil hole, and the other end connecting the shell upper end, said oil inlet tube (5) connecting with a heat-transfer oil pump (2). Through said method, this utility new type can continuously stir tank for heating, temperature control is accurate, uniform heating, which is good for molding a garbage inner stir fermentation tank, and the energy consumption is low.
NOVELTY - Preparing hydrogen using microwave plasma in alcohol, comprises (a) preparing aqueous alcohol solution, and injecting into a reactor; (b) collecting front gas, discharging gas in the reactor, controlling pressure inside the reactor; and (c) starting a microwave generator, injecting the microwave into the reactor, discharging liquid phase electrode, adding in the aqueous alcohol solution to produce plasma, allowing the plasma energetic particles to colloid with alcohol molecules, decomposing to obtain hydrogen-containing mixed gas, discharging the residual gas, collecting, and storing.    USE - The method is useful for preparing hydrogen using microwave plasma in alcohol (claimed).    ADVANTAGE - The method: has quick preparing speed; is simple and convenient for preparing hydrogen.    DETAILED DESCRIPTION - Preparing hydrogen using microwave plasma in alcohol, comprises (a) preparing 4-50 vol.% aqueous alcohol solution, and then injecting into a reactor; (b) collecting front gas, discharging gas in the reactor, controlling pressure inside the reactor to 1000-8000 Pa; and (c) starting a microwave generator, injecting the microwave produced through the waveguide coaxial cable into the reactor, discharging liquid phase electrode, then adding in the aqueous alcohol solution to produce plasma, allowing the plasma energetic particles to colloid with the alcohol molecules, decomposing to obtain hydrogen-containing mixed gas, connecting the reactor with a pipeline, discharging the residual gas, collecting the mixed gas, and storing.
NOVELTY - Recycling of phosphorus-containing wastewater synthetic slow-release fertilizer comprises measuring phosphorus-containing wastewater, adding calcium chloride aluminate hydrate, stirring at room temperature for 8-96 hours, adding into column chromatography at room temperature for 4-24 hours, separating precipitate, and drying to 80-500 degrees C for 4-12 hours.    USE - Method for recycling of phosphorus-containing wastewater synthetic slow-release fertilizer (claimed).    ADVANTAGE - The method is environment-friendly and achieves removal rate of more than 99%.
NOVELTY - Method of extracting lithium salt lake mother liquid comprises sun drying salt lake brine having high magnesium-lithium ratio to produce concentrated brine; freezing concentrated brine to produce mother liquor with nitrate crystals; mixing mother liquor with sulfur to produce potassium-magnesium fertilizer concentration, or precipitating using potassium salt to produce potassium chloride; and saturating concentrate to obtain bischofite and brine, which is lithium carbonate raw brine.    USE - Method of extracting lithium salt lake mother liquid.    ADVANTAGE - The method has simple process, provides high utilization rate of lithium salt mother liquor, has low production cost, is environment friendly, and has good comprehensive benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for extracting lithium salt lake mother liquid (Drawing includes non-English language text).
NOVELTY - Reducing algal turbidity, involves: eutrophication of water in a variety of complex microbial agents; improving transparency, planting submerged plants; according to submersed plants growth, putting a certain amount of herbivorous fish regularly eat carp fishing artificially, through the fish with the water portion of nutrients; and in each of these steps are measured before and after the water quality indicators.    USE - The method is useful for reducing algal turbidity (claimed).    ADVANTAGE - The method introduces microbes, submerged plants, and herbivorous fish producing a complete food chain of aquatic ecosystem with good compatibility.
NOVELTY - Preparation of insect microbial agent comprises mixing livestock manure and conditioning agent, adding inoculated microbial agent, stacking into dunghill, covering surface with straw or tarpaulins, fermenting, and composting; spreading out to dry, and cultivating saprophytic insect eggs; collecting insects when matured, and feeding into farmed animals, or drying and crushing to be used as feed protein sources; and drying remaining manure mixture, and crushing to be used as bioorganic fertilizer.    USE - Method for preparation of insect microbial agent (claimed).    ADVANTAGE - The method utilizes livestock manure which avoids environment pollution, and it has efficient conversion of developing new feed with protein source and biological organic fertilizer with no bad odor.    DETAILED DESCRIPTION - Preparation of insect microbial agent comprises:    (A) mixing livestock manure and conditioning agent at mass ratio of 10-15:1, adding inoculated microbial agent, stacking into 1 m high dunghill, covering surface with straw or tarpaulins, fermenting for 5-7 days, and composting;    (B) spreading out to dry until dunghill temperature is dropped to 30 degrees C or less, and cultivating saprophytic insect eggs; and    (C) collecting saprophytic insects when matured, and feeding into farmed animals, or drying and crushing to be used as feed protein sources; and drying remaining manure mixture, and crushing to be used as bioorganic fertilizer.    The microbial agent is Bacillus subtilis, Lactobacillus, yeast and Rhodopseudomonas palustris.
NOVELTY - A crops organic fertilizer additive comprises 40-50 pts. wt. silkworm excrement, 5-10 pts. wt. rice bran, 10-20 pts. wt. corn flour, and 0.05-0.1 pts. wt. microbial agent.    USE - Crops organic fertilizer additive.    ADVANTAGE - The fertilizer additive provides comprehensive nutrition for crops, increases fertilizer effect and soil organic matter content, and promotes microbial growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer additive comprising mixing raw materials, composting, regulating water content to 50%, turning once every 24 hours when temperature reaches 70 degrees C, and continuously fermenting for 15-20 days.
NOVELTY - Granulation of fertilizer comprises mixing macroelement, medium element, and microelement fertilizers, organic materials, and synergistic substances, spraying with 10-50 wt.% molasses alcoholic fermentation liquid, and mixing, where moisture content of molasses alcoholic fermentation liquid is 30-95%; granulating, bonding short fiber with organic material, enlarging particle diameter, rolling, and extrusion granulating to form granules; and drying, sieving, weighing, packaging, checking according to national standards, and storing.    USE - Method for granulating fertilizer (claimed).    ADVANTAGE - The method greatly increases fertilizer grain, increases production efficiency, reduces production cost, and is environment-friendly.
NOVELTY - Fertilizer composition comprises (in pts.wt.): gypsum (100), humic acid (150), digester supernatant (50), Lactobacillus bacteria (20), pulverized urea (1) and potassium chloride (8).    USE - Fertilizer composition used for cultivating red jujube (claimed).    ADVANTAGE - The fertilizer composition shows improved yield of red jujube.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) mixing raw material except potassium chloride and urea uniformly, and then keeping the obtained material for 10 days;    (B) adding potassium chloride and urea to the obtained material, and then crushing the obtained material;    (C) mixing the obtained material, and then extruding and granulating them; and    (D) packing the obtained material to obtain the finished product.
NOVELTY - Combined extractive distillation and hydrogenation isobutane preparation system comprises extractive distillation column (2), alkali washing tower (8), stripper (9), olefin washing tower (12), light constituent tower (13), hydrogenation reactor (16), heat exchanger (17), feed heater (18), separation device (20) and stabilizer column (25).    USE - Combined extractive distillation and hydrogenation isobutane preparation system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the combined extractive distillation process comprising gasifying unsaturated hydrocarbon, removing solvent, distilling, mixing olefin, stripping, performing hydrogenation, separating and stabilizing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of combined extractive distillation and hydrogenation isobutane preparation system.    Extractive distillation column (2)    Alkali washing tower (8)    Stripper (9)    Olefin washing tower (12)    Light constituent tower (13)    Hydrogenation reactor (16)    Heat exchanger (17)    Feed heater (18)    Separation device (20)    Stabilizer column (25)
NOVELTY - Dichloro acetamidine is synthesized by adding dichloroacetonitrile and liquid alcohol to flask, adding alkali metal carbonate catalyst, and reacting for 2-5 hours.    USE - Synthesis of dichloro acetamidine for pharmaceutical intermediate.    ADVANTAGE - Synthesis of dichloro acetamidine is simple and has small amount of side reactions, improved yield, and reduced catalyst dosage.
NOVELTY - Horizontal three-phase biological fluidized bed comprises treatment tank, sedimentation tank and sludge processing device provided on one side of treatment tank inlet, where the other side has a water outlet. The sedimentation tank is arranged side by side in the treatment tank provided with a side outlet. The inner tank comprises partition wall separating multi-form from the water inlet end of horizontal arrangement.    USE - The horizontal three-phase biological fluidized bed is useful for sewage treatment (claimed).    ADVANTAGE - The horizontal three-phase biological fluidized bed saves space, avoids the use of decentralized sewage treatment filler for pumps, valves and other equipment, and avoids the loss of carrier accumulation and compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for using the horizontal three-phase biological fluidized bed for sewage treatment, which involves: (a) uniformly placing influent wastewater into sewage processing device; (b) anaerobic treatment; (c) high load anaerobic biological processing; and (d) filtration and clarification.
NOVELTY - Efficient integrated ecological filter bed system comprises ecological filter bed having upper part set with ecological floating bed with plant stress resistance; and aquatic perennial water purification plants.    USE - The efficient integrated ecological filter bed system is useful in polluted river or lake, sludge water, domestic sewage, and industrial sewage.    ADVANTAGE - The efficient integrated ecological filter bed system has visual landscape effects, and wide range of applications. It belongs to water in-situ remediation technologies, and it has no secondary pollution on the surrounding environment. The construction cost is not high, and the operation and maintenance costs are low.
NOVELTY - A farm wastewater processing system comprises sedimentation tank (1), waste pre-processing tank (2), biogas tank (3), biogas processing device (4), filter tank (5), anaerobic reactor (6), acid-base regulating tank (7), and bioreactor (8) in which sedimentation tank, waste pre-processing tank, biogas tank, and biogas processing device are connected, sedimentation tank, filter tank, anaerobic reactor, acid-base regulating tank, and bioreactor are connected, anaerobic reactor has greater than or equal to 1 anaerobic reaction tank, and anaerobic tank water inlet and filter tank are connected.    USE - A farm wastewater processing system (claimed).    ADVANTAGE - Farm wastewater processing system is simple, efficient, and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of farm wastewater processing system.    Sedimentation tank (1)    Waste pre-processing tank (2)    Biogas tank (3)    Biogas processing device (4)    Filter tank (5)    Anaerobic reactor (6)    Acid-base regulating tank (7)    Bioreactor (8)
NOVELTY - Preparation of organic fertilizer comprises sieving livestock and poultry manure, drying, adding water, pre-fermenting to obtain solid-liquid mixture, and pumping into fermentation tank; controlling moisture content, fermenting, releasing toxic gases as biogas to fully ferment mixture, taking out, and removing residues; and mixing residues and humus coke fertilizer, stirring, composting, and controlling moisture content; and filtering, grinding, drying, and filling.    USE - Method for preparation of organic fertilizer (claimed).    ADVANTAGE - The method utilizes economic and efficient resources, saves energy, produces environment-friendly product, and it has low operation cost.    DETAILED DESCRIPTION - Preparation of organic fertilizer comprises:    (A) sieving livestock and poultry manure, drying, adding water, and mixing through pre-fermentation tank;    (B) adjusting temperature to 15-25 degrees C, pre-fermenting for 10-20 days to obtain solid-liquid mixture, and pumping into fermentation tank;    (C) controlling moisture content to 45-55%, fermenting to 55-65 degrees C for 45-60 days, releasing toxic gases as biogas to fully ferment mixture, taking out, and removing residues; and mixing residues and humus coke fertilizer at volume ratio of 4:1, stirring to obtain first mixture, composting for 15 days, and controlling moisture content to 30% to obtain second mixture; and    (D) filtering, grinding, drying until moisture content is less than 15%, and filling through filling machine.
NOVELTY - An organic fertilizer additive comprises 2-4 pts. wt. wild chrysanthemum, 2-4 pts. wt. rhizoma atractylodis, 2-5 pts. wt. silkworm dropping, 2-4 pts. wt. corn, 0.5-1 pt. wt. chitosan, 1-1.5 pts. wt. dry yeast, and 80-85 pts. wt. water.    USE - Organic fertilizer additive.    ADVANTAGE - The additive provides comprehensive nutrition for crops, increases fertilizer effect and update soil and organic matter, and promotes microbe breeding.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer additive comprising adding wild chrysanthemum, rhizoma atractylodis, silkworm dropping, corn and water into pot, heating, adding water, continuously heating for 10 with high heat, rear water continuously heating for 10 minutes, and standing for 5 hours; taking out, storing in shady place, standing for 20-30 minutes, adding dry yeast and chitosan, fermenting for 25 days, and filtering.
NOVELTY - Device comprises tank body structure, which is provided with clapboard (4). The tank body structure is divided into upper part tank (3) and lower part tank (7). The lower part tank is provided with valve (9) and the upper part tank is provided with feeding port (8).    USE - Device used for producing marsh gas and fertilizer.    ADVANTAGE - The device is safe and stable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a marsh gas and fertilizer producing device.    Upper part tank (3)    Clapboard (4)    Lower part tank (7)    Feeding port (8)    Valve (9)
NOVELTY - Small solid waste biological converter comprises support frame module (1), fermentation tank module (2), control module (3), cooling discharge module (4), and power module (5).    USE - Small solid waste biological converter.    ADVANTAGE - The converter is simple to operate and energy-saving, has compact design, beautiful appearance and strong practicability, reduces emission, and saves manpower and material resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of small solid waste biological converter.    Support frame module (1)    Fermentation tank module (2)    Control module (3)    Cooling discharge module (4)    Power module (5)
NOVELTY - An environment-friendly biological organic fertilizer comprises organic matter, alcohol waste liquid, beneficial biological bacteria, and trace element.    USE - Environment-friendly biological organic fertilizer used for preventing and treating lotus root decay disease (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application method of biological organic fertilizer comprising carrying out spray granulation.
NOVELTY - Manufacture of rice composite matrix comprises adding 20-25 pts. wt. human and animal excreta, 30-50 pts. wt. straw and 10-20 pts. wt. canal mud into marsh gas tank, adding 0.8-0.1 wt.% ferment additive, and fermenting; mixing 100-150 pts. wt. residue and 3-6 pts. wt. inorganic fertilizer and stirring; drying and crushing.    USE - Method for manufacturing rice composite matrix (claimed) used for planting rice.    ADVANTAGE - The method is convenient and has less pollution and low cost. The rice composite matrix has high fertility and can use resources repeatedly.
NOVELTY - Multivariate alcoholic fermentation of molasses fertilizer comprises mixing fertilizer, macroelement, medium element and microelement, crushing, adding to 5-50 wt.% liquid molasses in alcohol ferment kettle, heating at 100-140 degrees C, and continuously stirring, where water content of fertilizer raw material is 3-10%; and spray granulating, cooling, sieving, packaging, checking, storing qualified product, and recycling unqualified product.    USE - Method for multivariate alcoholic fermenting molasses fertilizer (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - An organic solid fertilizer comprises 30-60 pts. wt. earthworm manure, 10-20 pts. wt. livestock manure, 10-20 pts. wt. wheat straw, 8-10 pts. wt. urea, 0.5-1 pt. wt. ammonium dihydrogen phosphate, 0.3-0.6 pt. wt. potassium sulfate, 0.2-0.3 pt. wt. sodium selenite, 0.2-0.4 pt. wt. potassium silicate, 0.1-0.3 pt. wt. ammonium molybdate, 0.5-0.7 pt. wt. aluminum potassium sulfate, 0.1-0.3 pt. wt. calcium carbonate, 0.3-0.5 pt. wt. calcium oxide, 0.2-0.5 pt. wt. copper sulfate, 0.1-0.2 pt. wt. polyacrylamide, and 0.3-0.5 pt. wt. HM fermentation medium.    USE - Organic solid fertilizer used for improving soil and promoting growth of crop.    ADVANTAGE - The fertilizer is rich in microelements and efficiently absorbed by plant and makes soil more loose and not compact.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of organic solid fertilizer comprising weighing raw materials, mixing earthworm manure, livestock manure, wheat straw, urea and HM fermentation medium, compost fermenting for 2-3 months, and turning once for every 15 days; mixing with remaining components and compost fermenting for 20-35 days; and drying and packing.
NOVELTY - Preparation of organic substrate comprises weighing dairy manure, mushroom residue, cotton seed hull, corn straw, melon seedlings, tobacco stalk, sawdust, perlite, and ceramic compound, adding organic fertilizer fermenting bacteria, sealing with plastic cover, adding water, static composting, fermenting, turning, adjusting pH value, and controlling EC matrix value; drying until water content is 5-8%; screening, cleaning, air separating, and granulating to a particle size of less than 1 mm; and adding Bacillus subtilis and Bacillus licheniformis and packing.    USE - Method for preparing organic substrate used for black cabbage vegetable (claimed).    DETAILED DESCRIPTION - Preparation of organic substrate comprises (A) weighing 10-20 pts. wt. dairy manure, 20-25 pts. wt. mushroom residue, 30-35 pts. wt. cotton seed hull, 30-50 pts. wt. corn straw, 20-25 pts. wt. melon seedlings, 12-18 pts. wt. tobacco stalk, 10-12 pts. wt. sawdust, 6-8 pts. wt. perlite, and 3-5 pts. wt. ceramic compound, adding 2-4 wt.% organic fertilizer fermenting bacteria, sealing with plastic cover, adding water to adjust moisture content to 60-70% and carbon nitrogen ratio to 35-38, static composting, fermenting, turning after 4 days, turning once after 6 days, where fermenting temperature is 60-70 degrees C, adjusting pH value to 6.5-7.5, and controlling EC matrix value to 0.9-1.1 mS/cm; (B) drying until water content is 5-8%, where organic matter content is less than 12; (C) screening, cleaning, air separating, and granulating to a particle size of less than 1 mm; and (D) adding 2-4% Bacillus subtilis and Bacillus licheniformis and packing.
NOVELTY - Organic fertilizer preparation involves mixing collected samples and humus in acid soils with water, where the solid-liquid ratio is 1:4-8, and then filtered to obtain humus extracts. Diluted acid is added to the obtained extract to adjust the pH value to 3.5-4.8 to obtain acidified extract. Blueberries isolated bacteria is added to the extract to obtain acidic soil bacteria isolated complex. The obtained complex is filtered, and then nutrients are mixed with the obtained material, and then the obtained material is fermented at 50-55 degrees C for 15-30 days.    USE - Method for preparing organic fertilizer for blueberry (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that has improved acidity and fertility of soil.    DETAILED DESCRIPTION - Organic fertilizer preparation involves mixing collected samples and humus in acid soils with water, where the solid-liquid ratio is 1:4-8, and then filtered to obtain humus extracts. Diluted acid is added to the obtained extract to adjust the pH value to 3.5-4.8 to obtain acidified extract. Blueberries isolated bacteria is added to the extract to obtain acidic soil bacteria isolated complex. The obtained complex is filtered, and then nutrients are mixed with the obtained material, and then the obtained material is fermented at 50-55 degrees C for 15-30 days. The obtained material is detected for maturity using indicators. The obtained material is heated at 30-50 degrees C, where the water content of material is 30%. The obtained material is packed in containers to obtain the desired product.
NOVELTY - Preparation of levocarnitine compound comprises taking 4-chloro-ethyl acetoacetate as raw material, performing hydrogenation reduction with asymmetric ruthenium phosphine ligand complex catalyst in solvent, vacuum-concentrating, high vacuum-distilling to obtain (R)-4-chloro-3-hydroxy-ethylbutyrate, slowly dropping inorganic alkali and trimethylamine aqueous solution, controlling dropping speed, reacting at room temperature, adjusting pH to 6 by concentrated hydrochloric acid and resin column purifying.    USE - Method for preparing levocarnitine compound (claimed) used for medicine chemical synthesis technology field.    ADVANTAGE - The simple-operation, environment-protecting and short-step method has one-pot reaction which only uses water as solvent and reaction is performed at room temperature. It has yield of 80%. The levocarnitine compound has good quality and high purity.
NOVELTY - L- alpha -aminobutanamide hydrochloride is prepared by heating and reacting L- alpha -aminobutyric acid and 2,2-dimethoxypropane under action of acid catalyst, post-processing to obtain (S)-4-ethyl-2,2-dimethoxyoxazolidin-5-one, performing ammonolysis reaction under action of ammonolysis agent to obtain L- alpha -aminobutanamide, and performing salt-forming reaction with hydrochloric acid (HCl).    USE - Preparation of L- alpha -aminobutanamide hydrochloride (claimed).    ADVANTAGE - Preparation of L- alpha -aminobutanamide hydrochloride is simple, low-cost, and environment-friendly and has high yield and product purity and mild reaction condition.
NOVELTY - A 1-carboxymethyl-2-substituted benzimidazole is new.    USE - 1-carboxymethyl-2-substituted benzimidazole for vital biochemical reactions.    ADVANTAGE - Preparation is environment-friendly, simple, low cost, easy to operate, uses cheap and easy to obtain raw materials, and has anti-cancer and anti-tumor properties.    DETAILED DESCRIPTION - A 1-carboxymethyl-2-substituted benzimidazole of formula (I) is new.    R=H, 1-7C alkyl, haloalkyl, SH, aminoalkyl, phenoxymethylene, alpha -naphthalene oxymethylene, beta -naphthyl oxymethylene, substituted phenoxymethylene, or optionally substituted phenyl.    An INDEPENDENT CLAIM is included for preparation of 1-carboxymethyl-2-substituted benzimidazole.
NOVELTY - A valsartan is purified by dissolving valsartan crude product in alcohol solvent, adjusting pH to 3-4, filtering to obtain filtrate, adding mixed solvent of water and 2-amino-3-methylbenzoic acid, stirring, standing for 10-15 minutes, cooling at less than or equal to 0 degrees C, crystallizing, and filtering to obtain fine product.    USE - Purification of valsartan (claimed).    ADVANTAGE - Purification process has short reaction time high product yield and is simple to operate and environment-friendly. Product has high purity.
NOVELTY - Preparing biomass oil involves using biomass as raw material and then adding ethyl acetate, methanol or acetone solution to the biomass as an additive for fast pyrolysis and to obtain desired product.    USE - Method for preparing biomass oil (claimed).    ADVANTAGE - The method enables to prepare biomass oil in cost-effective and simple manner.
NOVELTY - N-(2-methyl-6-(1,3,4-oxadiazol-2-yl)phenyl)formamide compound (I), is new.    USE - (I) is useful in an agricultural and horticultural insecticide (claimed) for controlling and preventing insects in crops.    ADVANTAGE - (I) has low toxicity and is eco-friendly.    DETAILED DESCRIPTION - N-(2-methyl-6-(1,3,4-oxadiazol-2-yl)phenyl)formamide compound of formula (I), is new.    X = Cl or Br;    R1 = 3-bromine-1-(3-chloro-2-pyridyl)-1H-pyrrole-5-yl (optionally substituted with phenyl, halo, CN, N, OH, mercapto, amino, 1-3C-alkoxy, 1-3C-alkylthio, 1-3C-haloalkoxy or 1-3C-haloalkyl) or H; and    R2 = thienyl, phenyl, pyrazinyl (all optionally substituted with halo, CN, N, OH, mercapto, amino, 1-3C-(halo)alkoxy or 1-3C-(halo)alkylthio), pyridyl (optionally substituted with oxo, halo, CN, N, OH, sulfhydryl, mercapto, amino, 1-3C-(halo)alkoxy or 1-3C-(halo)alkylthio), H or halo such as F, Cl, Br or I.    An INDEPENDENT CLAIM is included for preparing (I).
NOVELTY - Thiamine hydrochloride preparation involves treating thiamine with hydrogen peroxide in an adequate amount in a cation exchange column to obtain resultant product. The obtained product is washed with purified water and then mixed with 5% of barium chloride solution uniformly until white precipitates are formed. The formed precipitates are separated with eluent and dried to obtain desired product.    USE - Method for preparing thiamine hydrochloride (claimed).    ADVANTAGE - The method enable to prepare thiamine hydrochloride in an eco-friendly manner.
NOVELTY - Substituted guaiacol compounds (Q) are new. (I) is Menverins H, (II) is Menverins I, (III) is Menverins J, (IV) is Menverins K, and (V) is Menverins L.    USE - (Q) are useful for preparing ocean anti-fouling coating (all claimed).    ADVANTAGE - (Q) are capable of easily preparing environmentally friendly ocean anti-fouling agent with high efficiency and good lipophilic properties.    DETAILED DESCRIPTION - Substituted guaiacol compounds (Q) of formulae (I)-(V) are new. (I) is Menverins H, (II) is Menverins I, (III) is Menverins J, (IV) is Menverins K, and (V) is Menverins L. An INDEPENDENT CLAIM is included for the preparation of (Q).
NOVELTY - An organic Rankine cycle system comprises a refrigerant mixture including 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea), propane (R290), 1,1,1,2,3,3-hexafluoropropane (HFC-236ea), 1,1,2,2,3-pentafluoropropane (HFC-245ca), normal pentane (R601) and isopentane (R601a). The mass ratio of R227ea and R245ca is 5-95:5-95, the mass ratio of R227ea, R236ea and R245ca is 5-95:2-80:3-93, and the mass ratio of R227ea, R245ca and R601 is 5-90:5-90:5-80.    USE - Organic Rankine cycle system (claimed).    ADVANTAGE - The organic Rankine cycle system is safe to use, and has excellent cycle characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic Rankine cycle system, which involves mixing 1,1,1,2,3,3,3-heptafluoropropane, propane, 1,1,1,2,3,3-hexafluoropropane, 1,1,2,2,3-pentafluoropropane, normal pentane and isopentane at normal temperature.
NOVELTY - Molybdate light emitting material.    USE - In the optical fiber communications, three-dimensional display, fluorescent labeled biological marker, and infrared radiation detection (claimed).    ADVANTAGE - The molybdate light emitting material has high purity, stable performance, high upconversion luminescence brightness, color purity, and good stability; and is prepared by simple and environment friendly; and is prepare without harmful gas emissions.    DETAILED DESCRIPTION - Molybdate light emitting material of formula ZnR4-4(x+y)Mo3O16:4xEr3+,4yYb3+.    z=doped mole percentage of Er3+;    y=doped mole percentage of Yb3+;    x=0.0001-0.5;    y=0.1-1;    x+y=0.1-1;    R=rare earth europium ion, iron ion, iron ion, cerium ion, thulium ion, praseodymium ion, neodymium ion, samarium ion, gadolinium ion, terbium ion.    An INDEPENDENT CLAIM is included for preparation of molybdate light emitting material of formula ZnR4-4(x+y)Mo3O16:4xEr3+,4yYb3+ involving grinding and mixing compound containing ytterbium ion, compound containing erbium ion, compound containing rare earth ion, compound containing zinc ion, and compound containing molybdenum ions to obtain mixture; sintering the mixture in the air atmosphere at 200-400 degrees C for 1-15 hours to obtain product; naturally cooling the product, grinding and mixing uniform, calcining at 400-900 degrees C in the air atmosphere for 15 hours to obtain product; naturally cooling the product, grinding and mixing, calcining at 900-1300 in the air atmosphere for 2-10 hours, naturally cooling to room temperature to obtain the molybdate light emitting material.
NOVELTY - The rotary type dry distillation furnace has a smoke gas outlet (3) and a smoke gas inlet (7) which are connected in a heating plate (1). A distributing plate (4) is arranged in the heating plate. The smoke gas entrance (A) and a smoke gas exit (B) are connected with the smoke gas clapboard (10). The movable seal rings (12,13) are provided in the smoke gas entrance and the smoke gas exit respectively. The smoke gas entrance and smoke gas exit are connected with a smoke gas entering pipeline (8) and a smoke gas discharging pipeline (14).    USE - Rotary type dry distillation furnace for rubbish treatment.    ADVANTAGE - The pyrolysis material is heated uniformly in the dry distillation furnace, and investment cost of the furnace is reduced. The heat efficiency is improved, and the furnace is operated in simple, safety and reliable manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the rotary type dry distillation furnace.    Heating plate (1)    Smoke gas outlet (3)    Distributing plate (4)    Smoke gas inlet (7)    Smoke gas entering pipeline (8)    Smoke gas clapboard (10)    Movable seal rings (12,13)    Smoke gas discharging pipeline (14)    Smoke gas entrance (A)    Smoke gas exit (B)
NOVELTY - Combustible waste is added to a pyrolysis furnace, nitrogen gas is introduced into the furnace, pressure in the pyrolysis furnace is maintained at 0.05-0.1 MPa, and heated. Obtained combustible waste is processed in pyrolysis furnace at 280-300 degrees C, to obtain combustible waste pyrolytic carbon. Obtained combustible waste is processed in pyrolysis furnace at 580-600 degrees C, and cooled, to obtain combustible waste pyrolysis tar. Obtained combustible waste is processed in pyrolysis furnace at 700 degrees C or more until pyrolysis gas is completely collected, to obtain combustible waste pyrolysis fuel gas.    USE - Pyrolysis of combustible waste (claimed).    ADVANTAGE - The method enables pyrolysis of combustible waste with dioxin emission of 0.1 ng/Nm3 or less and reduced combustion of carbon, volatile heavy metals and chlorine.    DETAILED DESCRIPTION - Combustible waste is added to a pyrolysis furnace, nitrogen gas is introduced into the furnace, pressure in the pyrolysis furnace is maintained at 0.05-0.1 MPa, and heated. Obtained combustible waste is processed in pyrolysis furnace at 280-300 degrees C, to obtain combustible waste pyrolytic carbon. Obtained combustible waste is processed in pyrolysis furnace at 580-600 degrees C, and cooled, to obtain combustible waste pyrolysis tar. Obtained combustible waste is processed in pyrolysis furnace at 700 degrees C or more until pyrolysis gas is completely collected, to obtain combustible waste pyrolysis fuel gas. The combustible waste is municipal solid waste, medical waste, trite garbage, tires, waste plastics, industrial waste, sludge, food waste, garden waste leaves and branches, and/or manure. Municipal solid waste and food waste are cleaned to remove inorganic debris, crushed, anaerobic fermentation is carried out for 8-10 days, dehydrated to remove water content of 30% or less, and dried.
NOVELTY - The device has sludge storage hopper (4) connected with circulation fluidized bed main portion (5) by spiral material feeding unit (3). An upper portion of circulation fluidized bed main portion is connected with cyclone separator (6) whose lower tube is connected to catalytic reactor (9) by returning device (7), and air outlet tube is extended into inner portion of catalytic reactor and connected to air distribution tube (11). The catalytic reactor is set with gas exit tube (12), and is connected to side surface lower portion of catalytic reactor by returning spiral unit (13).    USE - Circulating-type fluidized bed pyrolysis device for pyrolyzing carbon catalytic sludge, used in solid waste resource treatment field.    ADVANTAGE - The continuous operation of catalytic reaction is performed for effectively at reduced cost for improving the sludge pyrolysis oil quality. The sludge pyrolysis reactor using circulation fluidized bed is provided with increased heat transfer effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Circulating-type fluidized bed pyrolysis device for pyrolyzing carbon catalytic sludge.    Spiral material feeding unit (3)    Sludge storage hopper (4)    Circulation fluidized bed main portion (5)    Cyclone separator (6)    Returning device (7)    Catalytic reactor (9)    Air distribution tube (11)    Gas exit tube (12)    Returning spiral unit (13)
NOVELTY - Method for preparing biological oil by pyrolysis of biomass, crushing biomass into granules, screening the granules, drying, placing into silo in pyrolysis reactor, purging nitrogen to remove air, preheating the reactor, passing carrier gas through the reactor, forming alkaline gas environment, performing pyrolysis, performing gas-solid separation to obtain biological carbon and ash, cooling to obtain oil, separating upper layer and lower layer, cooling the lower layer to obtain product, and non-condensable gas, and collecting the non-condensable gas.    USE - The method is useful for preparing biological oil and biological carbon which is used as fuel or soil modifying agent and non-condensable gas which is used as a carrier gas for gas recycling as byproducts (claimed).    DETAILED DESCRIPTION - Method for preparing biological oil by pyrolysis of biomass, crushing biomass into granules, screening the granules, drying, placing into silo in pyrolysis reactor, purging nitrogen to remove air, preheating the reactor, passing carrier gas through the reactor, forming alkaline gas environment, increasing the biomass granules inside the silo in the reactor, performing pyrolysis using steam, performing gas-solid separation to obtain biological carbon and ash, where the biological carbon is used as fuel or soil modifying agent, cooling by spraying medium in quenching tower to obtain oil, maintaining the oil under static condition to separate upper phase and lower phase, separating the upper layer which is a aqueous phase portion using funnel, then separating the lower layer which is oil phase portion, cooling the oil using water-cooled condenser and then ice-cold condenser to obtain product and non-condensable gas, and collecting the non-condensable gas which is used as a carrier gas for gas recycling.
NOVELTY - The method involves dehydrating sludge. The dehydrated sludge granulation is provided into integrated closeness pyrolysis and gasification device for drying, carbonization, gasification and combustion processes. The drying section (4) is set at temperature of at 90 to 150 degrees C and gasification section (8) is set at temperature of 1000-1200 degrees C. The organic substance and inorganic substance are collected through collecting pipeline and harmless slag in high temperature combustion residue is discharged through slag discharging port (13).    USE - Method for generating fuel gas using gasification of sludge such as municipal sludge, pharmaceutical factory sludge, leather sludge, paper sludge, printing sludge and dyeing sludge.    ADVANTAGE - The dioxin condition is avoided and the operation cost and the labor intensity are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of single-direction sealing door.    Single-direction sealing door (1)    Down seal door (3)    Drying section (4)    Gasification section (8)    Slag discharging port (13)
NOVELTY - Preparing natural gas using converter exhaust gas comprises taking converter exhaust gas and coke oven gas as raw material gas, storing the converter exhaust gas in a converter exhaust gas storage container, adjusting the ratio of converter exhaust gas and coke oven gas, passing the converter exhaust gas and the coke oven gas into a methanation device, carrying out methanation reaction of hydrogen with carbon monoxide and carbon dioxide in raw material gas, so as to convert carbon monoxide and carbon dioxide to methane, and separating nitrogen gas to obtain natural gas composed of methane.    USE - The method is useful for preparing natural gas using converter exhaust gas (claimed).    ADVANTAGE - The method is economical, realizes utilization of converter exhaust gas, avoids the resource waste and environmental pollution and increases the economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for natural gas producing device, comprising methanation unit and nitrogen separation device, where the methanation device is connected to converter exhaust gas pipe and coke oven gas supply pipe, and the converter exhaust gas pipe is connected to converter exhaust gas storage container; the converter exhaust gas and coke oven gas is passed into methanation device via converter exhaust gas pipe and coke oven gas supply pipe; and the nitrogen separation device is provided with a nitrogen gas exports and export.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the natural gas producing device.
NOVELTY - Natural gas synthesis involves processing calcium carbide in a furnace to obtain coal gas, which is processed into methanation chamber for purification, where hydrogen gas, carbon monoxide gas, and carbon dioxide gas are supplied to the methanation chamber. On the completion of methanation process the obtained methane gas is separated out and collected in a different chamber.    USE - Method for synthesizing natural gas (claimed).    ADVANTAGE - The method enables to synthesize natural gas in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a natural gas production device, which comprises methanation chamber, gas circulation pipeline, and coke furnace, circulation pump.
NOVELTY - Wet-type microaerobic biogas ammonia desulfurization device comprises a microaerobic peristaltic pump, an integrated data collecting system, an anaerobic digestion tank, a stirring motor, an electromagnetic valve, an online gas analyzer and a wet-type ammonia desulfurization reactor. The inner part of the anaerobic digestion tank is set with a stirring device. The stirring motor is connected with the stirring device. The microaerobic peristaltic pump is connected with the anaerobic digestion tank through the electromagnetic valve.    USE - Used as wet-type microaerobic biogas ammonia desulfurization device.    ADVANTAGE - The device produces ammonium sulfate rich sludge which can be used in fertilizer, does not produce wastewater, waste liquid and waste residue, does not cause secondary pollution, and is economical.    DETAILED DESCRIPTION - Wet-type microaerobic biogas ammonia desulfurization device comprises a microaerobic peristaltic pump, an integrated data collecting system, an anaerobic digestion tank, a stirring motor, an electromagnetic valve, an online gas analyzer and a wet-type ammonia desulfurization reactor. The inner part of the anaerobic digestion tank is set with a stirring device. The stirring motor is connected with the stirring device. The microaerobic peristaltic pump is connected with the anaerobic digestion tank through the electromagnetic valve. The anaerobic digestion tank is connected with the online gas analyzer and the wet-type ammonia desulfurization reactor through an exhaust gas outlet. The microaerobic peristaltic pump, the electromagnetic valve, the stirring motor and the online gas analyzer are connected with the integrated data collecting system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wet-type microaerobic biogas ammonia desulfurization device.
NOVELTY - Manufacturing high combustion value non-polluting coal using domestic waste comprises transporting domestic waste from each dispersed point into the waste storing area, transporting the waste automatically/manually into the reaction kettle, sealing the reaction kettle, introducing steam into the reaction kettle, controlling the temperature and pressure change, forming carbide mixture, reducing temperature and pressure, discharging the reaction formed liquefied water and gas, adding the carbide mixture into a screening device, screening carbide mixture as non-combustible material.    USE - The method is useful for manufacturing high combustion value non-polluting coal using domestic waste (claimed).    ADVANTAGE - The method does not cause pollution, has low processing cost, and produces coal having high combustion value, and low emission.    DETAILED DESCRIPTION - Manufacturing high combustion value non-polluting coal using domestic waste comprises (i) transporting domestic waste from each dispersed point into the waste storing area, (ii) transporting the waste automatically or manually from the waste storage area into the reaction kettle, and completely sealing the reaction kettle, (iii) introducing steam into the reaction kettle, dynamically controlling the waste temperature and pressure change over time, forming carbide mixture in the reaction kettle, (iv) reducing temperature and pressure in the reaction kettle, discharging the reaction formed liquefied water and gas, and (v) adding the carbide mixture into a screening device, screening carbide mixture as non-combustible material, and finally obtaining carbide.
NOVELTY - The reactor has micro-algae culturing unit (1) whose bottom portion is set with diving pump (2) connected with water distribute tube (9) by suction tube main portion (3). A tower-shaped angle-iron-bracket (4) is uniformly distributed with several liquid storage tanks (5). The liquid storage tank is set with transparent plastic thin film, stainless steel wire mesh that is fixed on angle-steel bracket connected with tower-shaped angle-iron-bracket, and transparent corrugated plastic drainage plate that is fixed on stainless steel wire mesh.    USE - Bionic laminated micro-algae photosynthesis reactor used in medical application and sewage purification application.    ADVANTAGE - The bionic laminated micro-algae photosynthesis reactor is provided with improved photosynthetic efficiency, high energy saving efficiency, convenient maintenance efficiency, improved carbon fixation efficiency, low cost and high safety coefficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bionic laminated micro-algae photosynthesis reactor.    Micro-algae culturing unit (1)    Diving pump (2)    Suction tube main portion (3)    Tower-shaped angle-iron-bracket (4)    Liquid storage tank (5)    Water distribute tube (9)
NOVELTY - A Candida tropicalis strain Y2 (CCTCC 2013726), is new.    USE - The C.tropicalis strain Y2 is used for preparing functional feed additive for aquaculture animal and treating waste resources and wastewater resources in marine aquaculture (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of C.tropicalis strain Y2, which is for preparing functional feed additive for aquaculture animal and treating waste resources and wastewater resources in marine aquaculture.
NOVELTY - Multifunctional Bacillus subtilis MZS1 (CCTCC NO: M2014042) is new.    USE - The strain is used for degrading lignin and cellulose, broad spectrum dye decoloring and degrading chlorpyrifos (claimed).    ADVANTAGE - The strain exhibits good chlorpyrifos degradation ability in soil and water, and can form stable relationship with indigenous bacterial community.
NOVELTY - Microbial inoculum comprises Pseudomonas aeruginosa, Pseudomonas putida, Acinetobacter lwoffii, Pseudomonas, Achromobacter, methyl methanesulfonate (MMS) Pseudomonas, Candida tropicalis and white Nocardioform.    USE - The microbial inoculum is useful in soil repairing agent for restoring petroleum polluted soil, and degrading total petroleum hydrocarbon (TPH) pollutant in soil, normal alkane, hopane and aromatic hydrocarbon (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) soil repairing agent, comprising microbial inoculum and biological surfactant; (2) use of microbial inoculum in restoring petroleum polluted soil, where the application method comprises (a) reactivating Pseudomonas aeruginosa, Pseudomonas putida, Acinetobacter lwoffii, Pseudomonas, Achromobacter, MMS Pseudomonas, Candida tropicalis and white nocardioform strains, enlarging culture, and mixing to obtain mixture, (b) crushing large sludge and uniformly mixing with the mixture, adding 8-10 wt.% of urea, 1-3 wt.% of ammonium dihydrogen phosphate, uniformly mixing to obtain oil sludge, adding 4-6 wt.% of microbial inoculum into oil sludge, uniformly stirring, maintaining oil in water to 30-35%, turning the mixture for every 2 days, placing the sludge in ventilation for oxygen supply, simultaneously maintaining the water content in the sludge, allowing to stand for half month to degrade total petroleum hydrocarbon (TPH), crude oil and bacteria and microzyme, observing oil color until the color is closed to normal soil; and (3) use of soil repairing agent for repairing petroleum pollution in soil, where the application method comprises mixing rhamnolipid and the mixture obtained in step (a), freeze drying to obtain purity of more than 85%, adding 0.75-1 vol.% rhamnolipid mixture into the sludge, and performing step (b) as above per se.
NOVELTY - Obtaining polyhydroxyalkanoate (PHA) comprises mixing the sludge with xylose-utilizing Zymomonas, screening strains which are able to produce PHA, culturing the positive clones in a culture medium for protein expression, and extracting PHA.    USE - The method is used for obtaining PHA (claimed).    ADVANTAGE - The method is used for rapidly obtaining PHA with high yield. The method is simple.
NOVELTY - A low temperature straw biogas fermentation promoter, comprises: 10 pts.wt. of iron(ii) chloride tetrahydrate, 2-4 pts.wt. of nickel chloride hexahydrate, 1-2 pts.wt. of cobalt(II) chloride hexahydrate, 20-40 pts.wt. of cellulose, and 44-67 pts.wt. of wheat bran.    USE - As low temperature straw biogas fermentation promoter use for production of methane gas.    ADVANTAGE - The composition is simple and economical; can be prepared using easy preparation method which is flexible, and easy-to-control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the low temperature straw biogas fermentation promoter, involving: dissolving 10 pts.wt. of iron(ii) chloride tetrahydrate (FeCl2.4H2O), 2-4 pts.wt. of nickel chloride hexahydrate (NiCl2.6H2O), and 1-2 pts.wt. of cobalt(II) chloride hexahydrate (CoCl2.6H2O), in 1-2 pts.wt. of water to obtain saturated solution; adding 44-67 pts.wt. of wheat bran, fully and uniformly mixing; then adding 20-40 pts.wt. of cellulose, to obtain the low temperature straw biogas fermentation promoter.
NOVELTY - Preparation of biogas involves crushing bagasse, obtaining crushed product, stirring, processing portion of crushed bagasse with water and calcium hydroxide, obtaining calcium hydroxide-pretreated bagasse (A), processing portion of crushed bagasse with water, obtaining hydrothermally-pretreated bagasse (B), processing remaining portion of bagasse, obtaining calcium hydroxide-hydrothermally-pretreated bagasse (C), mixing products (A), (B) and (C), obtaining pretreated bagasse, mixing with activated sludge, adding water, adding to anaerobic reactor and performing fermentation reaction.    USE - Preparation of biogas (claimed).    ADVANTAGE - The method enables preparation of biogas with high yield.    DETAILED DESCRIPTION - Preparation of biogas involves crushing bagasse, obtaining crushed product having particle size of 10 mesh or less, stirring, mixing portion of crushed bagasse with water and calcium hydroxide, leaving still for 4 days, adjusting pH to 7-8, obtaining calcium hydroxide-pretreated bagasse (A), mixing a portion of crushed bagasse with water in reactor, processing at 120-200 degrees C and 0-75 kPa for 10-30 minutes and cooling to 60 degrees C or less, obtaining hydrothermally-pretreated bagasse (B), mixing remaining portion of bagasse with water and calcium hydroxide, adding to reactor, processing at 120-200 degrees C and 0-75 kPa for 10-30 minutes, cooling to 60 degrees C or less, obtaining calcium hydroxide-hydrothermally-pretreated bagasse (C), mixing products (A), (B) and (C), obtaining pretreated bagasse, mixing activated sludge and pretreated bagasse, adding water, diluting, obtaining mixture containing pretreated bagasse volatile solid and activated sludge in the weight ratio of 0.65-0.85:1 and water and pretreated bagasse volatile solids in the weight ratio of 16.8-24.6:1, adding to anaerobic reactor and performing fermentation reaction at 35 plus minus 1 degrees C.
NOVELTY - The device has a gasification furnace provided with a heat boiler. The gasification furnace produces gas from a biomass raw material. A gas pressure device is connected with an injector. A steam ejector and a combustion nozzle are connected with the heat boiler. The heat boiler is provided with a lifting jet and externally supplied hot water. An upper side of the gasification furnace is provided with a bottom ash and a grate oxide layer. The lifting jet is connected with an inlet end, which is placed in a receiving room. A pipeline is connected with multiple tube section.    USE - Heat accumulating type biomass gasification combustion device.    ADVANTAGE - The device avoids producing dust in a heat storage body so as to fully and smoothly ensure stable combustion operation. The device reduces nitrogen oxide and oxygen amount, size of combustion process gage, and pneuma smoke discharging amount, and is environmental friendly, and has better energy-saving property, high efficiency, low corrosiveness effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a heat accumulating type biomass gasification combustion method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a heat accumulating type biomass gasification combustion device.
NOVELTY - Methanation catalyst comprising 5-60 wt.% of nickel(II) oxide as active component and aluminum oxide as carrier, is new.    USE - Methanation catalyst.    ADVANTAGE - The methanation catalyst can be simply prepared with high yield in eco-friendly, cost-effective and less energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the catalyst.
NOVELTY - This utility new type provide the one a compost planting machine, include compost bucket, upper part and front part of said compost bucket set with a one with a planting basin set with fertilizer bucket connected with the charging of the one side compost bucket of, a. taking door on the other side compost fertilizer bucket of the one side add material box of the a door set with a vent hole. This utility new type perfectly the kitchen waste compost and courtyard planting combine are integrated, solving the problem that the kitchen waste compost fermentation of the problem that moving rear. Design of feeding in accordance with human engineering principle, easy. Compost planting space of basin skilfully uses the rest space, and the planting pot, avoiding direct sunlight, but does not affect the heating, which is good for decomposed. Rear kitchen decomposed lower the air environment, and directly taken out from the taking door in fertilizer can be put in a planting pot. Time-saving labour force, the family kitchen garbage from harmless and resources to provide the solution of whole body.
NOVELTY - The method involves removing oil in pneumatic liquid using coal gas primary cooler (2) and pneumatic liquid separator (1). Pressurized stripping process of free ammonia is performed by sending residual ammonia water to pressure stripping tower (4). Pressure-distilling process of mixed steam condensation is performed by sending steam condensing liquid to atmospheric distillation tower (7) and ammonia water condenser (8). Anhydrous ammonia rectifying process is performed by sending ammonia water to anhydrous ammonia rectifying tower (12) to obtain anhydrous ammonia product.    USE - Method for producing anhydrous ammonia gas in coking industry.    ADVANTAGE - The process of producing anhydrous ammonia gas is implemented effectively with reduced corrosion of phosphate, simple and convenient operational efficiency, small waste water discharge and improved environmental protection efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process of producing anhydrous ammonia gas.    Pneumatic liquid separator (1)    Coal gas primary cooler (2)    Pressure stripping tower (4)    Atmospheric distillation tower (7)    Ammonia water condenser (8)    Anhydrous ammonia rectifying tower (12)
NOVELTY - Biogas liquid processing method involves collecting biogas, sending collected biogas into settling tank, adding coagulant, stirring, standing for 2 hours, performing solid-liquid separation, performing pre-dehydration treatment, performing centrifugal dewatering, and purifying.    USE - Method for liquid processing of biogas.    ADVANTAGE - The method increases utilization ratio of biogas and reduces pollution risk.
NOVELTY - Cultivation material comprises (in pts.wt.): bran (80-100), cotton seed husk (3-6), wooden meal (2-6), corn core (4-10), corn powder (2-6), rice bran (3-16), soybean powder (2-5), lime (1-2), gypsum (1-3), salt (0.2-0.6), sugar (1-3), urea (1-3), magnesium sulfate (0.5-1) and calcium super-phosphate (0.2-0.6).    USE - Cultivation material used for growing edible mushroom, Coprinus and fungus.    ADVANTAGE - The cultivation material shows improved yield for edible mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing cultivation material, which involves:    (A) crushing and drying the raw materials, and then mixing them uniformly;    (B) fermenting then obtained material at pH 8-8.5 for 12-20 hours;    (C) repeating the fermentation process for thrice; and    (D) sterilizing the obtained material to obtain the finished product.
NOVELTY - Biological organic fertilizer preparation involves using microbial growth-promoting nutrition package I and II with growth-promoting rhizobacteria, and then mixing fresh chicken manure, corn straw and mushroom residue, and then decomposing them. The obtained material is fermented with yeast (5-12%) for 10-14 days at 60-80 degrees C. The fermented material is cooled to 20-30 degrees C, and then the obtained material is fermented for 1-3 days, and then nutrition bag II is added to the obtained material. The obtained mixture is fermented for 4-6 days at 26-50 degrees C.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare biological organic fertilizer in cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Biological organic fertilizer preparation involves using microbial growth-promoting nutrition package I and II with growth-promoting rhizobacteria, and then mixing fresh chicken manure, corn straw and mushroom residue, and then decomposing them. The obtained material is fermented with yeast (5-12%) for 10-14 days at 60-80 degrees C. The fermented material is cooled to 20-30 degrees C, and then the obtained material is fermented for 1-3 days, and then nutrition bag II is added to the obtained material. The obtained mixture is fermented for 4-6 days at 26-50 degrees C. The obtained material is crushed, and then granulated to obtain the finished product.
NOVELTY - Production of organic fertilizer comprises adding farm animal manure and biogas residue into fermentation tank and separating solid and liquid to obtain fecal waste; uniformly mixing with crop straw powder to obtain fermentation substrate; uniformly mixing with first microbial fermentation agent; piling material, naturally fermenting, and turning; mixing with second microbial fermentation agent, fermenting, and naturally cooling; and crushing, sieving, granulating, dehumidifying, and packaging.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The fertilizer has humic odor smell and no odor, cultivating cabbage seed germination rate of 90%, and organic matter content of 50-60%.    DETAILED DESCRIPTION - Production of organic fertilizer comprises adding farm animal manure and biogas residue into fermentation tank and separating solid and liquid to obtain fecal waste at moisture content of 62-65%; uniformly mixing with crop straw powder at weight ratio of 6-10:1 to obtain fermentation substrate; uniformly mixing with first microbial fermentation agent at weight ratio of 1000:3-5; piling 1.5-2 m high material, naturally fermenting, and turning for 2-3 times once every 2 days if temperature reaches 50-60 degrees C; mixing with second microbial fermentation agent at weight ratio of 1000:0.5-1, fermenting at 50-60 degrees C for 3-4 days, and naturally cooling; and crushing, sieving, granulating, dehumidifying, and packaging. An INDEPENDENT CLAIM is included for fermentation tank comprising crusher, discharge port, hopper, scraper, scraper driving belt, feeding port, cylinder sieve, cylindrical-shaped screen exit, first conveyer belt, mixer, second conveying belt, granulator, vacuum feeding machine, and cooling machine.
NOVELTY - Rotary furnace air inlet system comprises carbonizing furnace shell (1), rotating cylinder (5), carbonization section (7), drying section (6), feed outlet, discharge outlet, motor driven, shoveling or cooling plate (25), heating room, revolving drum, material connecting cabinet, air inlet system, carbonization pyrolysis gas outlet, cyclone separator, furnace tail draft fan, air inlet, gas three-way guide pipe, biomass boiler, combustion furnace, regulating valve, hot mix room, tail gas pipeline, tail gas mix gate door, converter air inlet device, and converter air outlet device.    USE - Rotary furnace air inlet system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of rotary furnace air inlet system.    Carbonizing furnace shell (1)    Rotating cylinder (5)    Drying section (6)    Carbonization section (7)    Shoveling or cooling plate (25)
NOVELTY - A tobacco waste organic matter-decomposing inoculant comprises 15-20 pts. wt. Bacillus subtilis, 10-15 pts. wt. Aspergillus oryzae, 10-15 pts. wt. Aspergillus niger, 10-15 pts. wt. green Trichoderma, 10-15 pts. wt. Bacillus mucilaginosus, 10-15 pts. wt. Saccharomyces cerevisiae yeast, 5 pts. wt. Thermophilic bacillus, 5 pts. wt. Arthrobacter nicotinovorans, and 10-25 pts. wt. Actinomyces.    USE - Tobacco waste organic matter-decomposing inoculant used for decomposition of organic matter, nitrogen, phosphorus and potassium element in plants (claimed).    ADVANTAGE - The inoculant reduces nicotine content of tobacco and hazards of tobacco waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of biological organic fertilizer comprising mixing tobacco waste, distillers grain and calcium-magnesia phosphate fertilizer, fermenting, aging, adding microbial inoculum to obtain biological organic fertilizer; uniformly mixing with tobacco waste organic matter-decomposing inoculant, composting, and fermenting; turning, continuously composting, turning if temperature reaches to 65-75 degrees C, stacking, and cooling to room temperature; and    (2) application method of organic fertilizer comprising mixing 250-350 kg/acre biological organic fertilizer in soil on dry land crops.
NOVELTY - Improving method of Asparagus planting soil comprises taking livestock manure and gasket material, feed residue and agricultural waste, mixing, and anaerobically decomposing to obtain bio-organic fertilizer; mixing 10-50 wt.% bio-organic fertilizer and soil; adding 45 wt.% compound fertilizer in 2-5 wt.% bio-organic fertilizer; and dropping 45 wt.% urea fertilizer and 10-20 wt.% compound fertilizer.    USE - Method for improving Asparagus planting soil (claimed).    ADVANTAGE - The method increases Asparagus yield and quality and reduces waste and environment pollution.
NOVELTY - Manufacture of high nitrogen-containing composite fertilizer anti-caking agent comprises mixing 10-30 wt.% 12-22C long chain fatty alkyl primary amine, 10-18 wt.% fatty acid monoglyceride, and 10-20 wt.% higher fatty acid; adding 60-80 wt.% waste animal and plant triglycerides; heating to completely dissolve; and filtering.    USE - Method for manufacturing high nitrogen-containing composite fertilizer anti-caking agent (claimed).    ADVANTAGE - The method is simple and environment-friendly and has less raw materials and low cost. The raw materials used is susceptible to soil microbial degradation.
NOVELTY - An antiboiling, antifouling and antifreezing liquid comprises 100-120 pts. wt. ethylene glycol, 60-80 pts. wt. deionized water, 15-30 pts. wt. corrosion inhibitor, 5-10 pts. wt. silicate, 6-8 pts. wt. silicate stabilizer, 2-4 pts. wt. mildew preventive, 5-10 pts. wt. pH adjusting agent, 1-3 pts. wt. antifoaming agent and 1-5 pts. wt. colorant. The pH adjusting agent is disodium hydrogen phosphate.    USE - Antiboiling, antifouling and antifreezing liquid (claimed).    ADVANTAGE - The environmentally-friendly antiboiling, antifouling and antifreezing liquid has high quality with suppressed generation of precipitates, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of antiboiling, antifouling and antifreezing liquid, which involves mixing ethylene glycol and deionized water, obtaining antifreezing agent, adding silicate, silicate stabilizer, mildew preventive, antifoaming agent and colorant, filtering, adjusting the pH value using pH adjusting agent, and stirring.
NOVELTY - The furnace has a combustion chamber wall (2) that is set on outer layer wall (1). A bottom of inner concave taper is set with a combustion room wall (3) which is set with upper air hole (10). A carbon interlayer (6) is produced between combustion chamber wall and outer layer wall. A top annular cover (5) is covered on outer layer. The combustion chamber wall portion is higher than outer layer wall set with a primary air hole (9). Secondary air hole is set for semi-gasification combustion. The combustion room wall is lower than outer layer wall set with fuel gas hole (8).    USE - Carbon furnace for producing semi-gasification biomass.    ADVANTAGE - The design of carbon furnace for producing semi-gasification biomass can be valid using castoff of agriculture and forestry production with biological carbon of multi-application, and sufficient combustion, clean and environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon furface.    Outer layer wall (1)    Combustion chamber wall (2)    Combustion room wall (3)    Top annular cover (5)    Carbon interlayer (6)    Fuel gas hole (8)    Primary air hole (9)    Upper air hole (10)
NOVELTY - The bamboo carbonization furnace having a smoke gas waste heat utilization function comprises a chamber formed by a set of refractory bricks. The chamber comprises an opening cover, a combustion chamber, a pre-heating chamber and a drying chamber. The pre-heating chamber is connected with the drying chamber through a smoke gas channel. The combustion chamber is set with an area for placing firewood within the combustion chamber. The combustion chamber is set with a plate and a fire grate. The drying chamber is connected with a smoke gas purification device through the smoke gas channel.    USE - The bamboo carbonization furnace is useful for producing charcoal.    ADVANTAGE - The bamboo carbonization furnace rapidly produces the charcoal with high yield, and has improved energy utilization rate.    DETAILED DESCRIPTION - The bamboo carbonization furnace having a smoke gas waste heat utilization function comprises a chamber formed by a set of refractory bricks. The chamber comprises an opening cover, a combustion chamber, a pre-heating chamber and a drying chamber. The pre-heating chamber is connected with the drying chamber through a smoke gas channel. The combustion chamber is set with an area for placing firewood within the combustion chamber. The combustion chamber is set with a plate and a fire grate. The drying chamber is connected with a smoke gas purification device through the smoke gas channel. The smoke gas purification device is set with a draught fan. The smoke gas purification device is connected with a chimney through the smoke gas channel. The smoke gas channel is located in an upper part of the combustion chamber. The pre-heating chamber and the drying room are arranged on an upper half part and a lower half part of the chamber, respectively. An inner side of the combustion chamber is set with a gas pipeline. The chamber is set with a first temperature measurement port. The chimney is set with a second temperature measurement port.
NOVELTY - The system has rubbish stacking chamber from which rubbish is conveyed to cutting system for cutting and crushing process. A stirrer is provided for mixing crushed rubbish material using compressor to obtain mixed fuel cake. The mixed fuel cake is conveyed to drying room for water drying process. The dried mixed fuel cake is again dried using decomposing machine for forming granular fuel structure that is stored in finished product bin. A sterilizing room is connected to water collecting tank. A test chamber is provided for inspecting rear discharge of granular fuel structure.    USE - System for treating rubbish in waste water for providing fuel to hydraulic power station.    ADVANTAGE - The waste water-rubbish treatment system is provided with improved treating efficiency, reduced pollution to environment, reduced treating time and improved economic efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for treating rubbish in waste water for providing fuel to hydraulic power station. (Drawing includes non-English language text)
NOVELTY - This new type utility claims one biological diesel oil of a multistage distillation system, belonging to the biology diesel oil preparation technology field. This utility new type comprise middle tank, rectifying and purifying mechanism and a product collecting mechanism, the rectifying and purifying mechanism comprise first-stage rectifying and purifying sub-mechanism, a level rectifying and purifying sub-mechanism and three level rectifying and purifying sub-mechanism, one level rectifying and purifying sub-mechanism, a level rectifying and purifying sub-mechanism and three level rectifying and purifying sub-mechanism in turn in series, a middle tank and a first-stage rectifying and purifying sub-mechanism connected with a product collecting mechanism comprise a first-stage product collecting tank, a product collecting tank level and three-level product collecting tank, a first-stage product collecting tank, a product collecting tank level and three-level product collecting tank a is connected with the rectifying and purifying sub-mechanism of corresponding level number. This utility new type of biological diesel oil yield is high, a short rectifying and purifying the product and a separate light effect and high quality.
NOVELTY - This utility new type belongs to the environment protection and waste resource utilization technology field of one a farm waste comprehensive utilization system. Structure of the system is as follows: the septic tank in turn is connected with the preprocessing pool, a cutting pump and measuring heating tank, heating tank through metering pump and the feed CSTR reactor, CSTR reactor and the discharge tank, discharge tank and reflux pump, reflux pump is connected with the a septic tank and dewatering machine and dehydrating machine is connected with a biogas slurry and biogas residue storage tank, storage CSTR reactor is also connected with the water sealing device, water sealing in turn is connected with the steam-water separator, a desulfurizing tower, a wet pneuma storage cabinet and electric generator, the electric generator through transmission pipeline and a CSTR reactor and measuring heating tank. This utility new type of application can be a waste of farm a harmless and recycling treatment, improve farm environment and promoting sustainable development of farm.
NOVELTY - This utility new type claims a multi-layer one coated urea granule fertilizer, include a urea granule, wherein said urea granule is covered with outer water layer, outer water layer in turn is coated with a bentonite, zeolite powder and attapulgite, and bentonite, zeolite powder and attapulgite each layer thickness ratio is 1: 1: 2, said attapulgite is covered with matrine component envelope and outer a matrine component envelope is covered with sodium nitrate. This utility new type structure design is reasonable, it does not need large amount of organic solvent, a green environment-friendly process has no pollution, the product nutrient can satisfy a plant nutrition requirement, coating material would not bring pollution to the environment and capable of improving soil, production cost is low, the industrialization difficulty is small.
NOVELTY - This utility new type claims a biomass gas return natural air-cooling dust-removing device, comprise cooling tube, a shell and a water seal tank, two the cooling end of a tube is an air inlet and an air outlet, a cooling tube is multi-tube parallel four-pass cooling tube, first return cooling tube and lower end of second return cooling tube is fixedly set with the first sink in the water seal tank of inner seal a ash bucket, third return cooling tube and lower end of fourth return cooling tube and fixed set with hopper seal connecting the second sink ash water seal tank of inner, second return cooling tube and upper end of third cooling tube and the air return cover seal connect. This utility new type having heat radiating effect is good, and it has a good dust-removing function.
NOVELTY - This utility new type claims a kitchen garbage processing device one and the marsh gas tank. A marsh gas tank, wherein comprise first reaction tank, reaction tank and second water pump, wherein the first reaction tank top end is provided with feed inlet and discharge opening, the bottom is provided with first reactant exhaust valve, second reaction tank top end is opened with the reactant entrance, the bottom end is opened. First reaction tank is set in the second reaction pool upper end, discharge valve with the reactant entrance, kitchen garbage after first preset time./fermentation rear, open reactant exhaust valve, by second reaction tank to continue the fermentation, open a slag discharging a reaction residue in second reaction the third preset time in the first reaction tank inner. A water pump in the first reaction tank and second reaction tank, from the second reaction tank for extracting reaction liquid in a predetermined amount to the first reaction tank, which can increase the fermentation efficiency of raw material inner first reaction tank, and saves the water resource. This new type utility also claims a one kitchen garbage processing device.
NOVELTY - This utility new type is a one dimensional environment-friendly fermenting system, comprise the conveying unit, a feeding device, a crushing device, a ventilation device, a tail pneuma purification device of fermenting material transfer, the conveying unit set with multiple group, each group by a plurality of conveyor layered by a low high solid mounting is formed by in turn, mounting a plurality straight line of a conveyor, a conveyor between the adjacent layer are staggered set up on the vertical to a surface, each group of each layer set with a crushing device, the further comprise material molding device, mounting the feeding end of top feed conveyor above the feeding device. This utility new type of three-dimensional environment-friendly fermentation system a greatly increase a fermentation efficiency.
NOVELTY - This new type utility claims one retaining a biological herbicide type value-added urea, wherein a multi-comprise a poly-ammonia acid urea granule, said poly-ammonia acid urea granule outer in turn is covered with a water-retaining layer of microbial inoculum and nitrification inhibitor layer slow release layer, and in turn is covered of microbial inoculum and nitrification inhibitor layer rear slow release layer of a multi-poly-ammonia acid urea granule through bonding and as a whole, the herbicide is coated layer. This utility new type structure design is reasonable, the fertilizer not only can be a multi-soil fertilizer and increase the water utilization rate, reduces the environment pollution, but also a wiping field, promoting the growth of crops, increase yield, improving product quality, increase soil fertility, improving and repairing soil is suitable for our country drought, drought and semi-drought area of seasonal, a multi-crop as a base fertilizer or additional fertilizer.
NOVELTY - One a biomass fuel gasification ash water cooling scraper slag removing device, it comprise the ash collecting box, a slag collecting box by an upper cover plate, lower cover plate and side water cooling wall is surrounded by seal, upper part and lower part of said ash collecting box set with a cooling water inlet tube and cooling base water discharging tube base, a upper cover plate set with a biomass pneuma for furnace slag is connected with a slag liquid entrance, said upper cover plate is further set with a extending to a stirrer inner ash collecting box, a lower upper cover plate set with solid ash exit, said solid slag exit is set on the ash collecting box of scraper slag remover, a side water cooling wall by several arranged in parallel a cooling medium conveying tube and combination is formed by a flat steel is welded between the adjacent cooling medium conveying tube. The design not only can cool ash, but also can prevent dust and toxic substance in a flue gas directly entering into the atmospheric environment, a fully cooled slag material, operation cost is low, the energy utilization ratio is high, which meets the national energy conservation and emission reduction of.
NOVELTY - This new utility model claims a kind of marsh gas processing system one, category marsh gas processing area. The system comprises the marsh gas storage cabinet and wet desulphurization unit, gas water separator, dry desulphurization unit, air filter and a booster fan in turn connected with the gas input port and marsh gas compressor, cold dryer, intercept pre filter, the primary oil water separator, precision filter, beyond precision filter, heat exchanger and one grade membrane group is orderly connected with a booster fan, output port and second level membrane group, natural gas compressor and add gas column in turn connected with the one grade film group equipped with recycling the carbon dioxide-rich gas wherein the gas input port connected with natural gas skid install vehicle equipped with the above filling column and one grade film group. The system can make city organic waste Anaerobic fermentation and methane purifying back to back for compressing natural gas (GB18047-2000) standard, after solving the city organic waste Anaerobic fermentation production of marsh gas purifying system existing investment and operation cost high, complex control, fault rate and high floor area is big problem.
NOVELTY - This utility new type refers to one having a heating and stir function of marsh gas fermentation tank construction, include a marsh gas fermentation tank (1), heating device 2, a rotating shaft 3, by-shaped heating pipe 4, heat preservation layer 5, the outer colour steel plate 6, 7, an air outlet 8, a feeding tube 9 and discharge tube 10. Mainly solving the marsh gas fermentation process with the fermentation temperature and a material in the shell layer affect fermentation effect of the problem, the one with a heating and a stir of marsh gas fermentation tank. The structure is novel, it is convenient and practical, the fermentation gas is not by the surrounding natural environment temperature, it can control the fermentation temperature, a material mix uniform, which avoids layering phenomenon, high yield, stable and is suitable for rural integrated marsh gas production, but also suitable for the agricultural production the methane supplied, which is one type of a marsh gas fermenting device.
NOVELTY - This utility new type is a straw excrement one dual-purpose raw material marsh gas tank, by fermentation room (1), wall (2), a movable cover (3), gas-guide tube (4), a discharge tube (5), a feeding tube (6), a filter plate (7), gas-guide tube (8), water pressure chamber (9), a pressure (10), pneuma room (11), a cover plate (12), water storage tank (13), plate (14), a discharge tank (15), a feeding tank (16), a material storage tank (17). This utility new type is a new and improved a raw water pressure type marsh gas tank, special for poultry fermenting of marsh gas pool to ferment for preparing marsh gas improved the rear, used for fermenting crop straw for preparing marsh gas between a gas-guide tube with two pipeline, biogas generated for kitchen life with energy. A marsh gas tank not only can the livestock and poultry excrement, but also the crop straw, solves the problem that our country rural marsh gas pool to ferment raw material less than a.
NOVELTY - This utility new type claims a marsh gas fermentation cylinder double-tube one overflow system, include marsh gas fermentation tank, an overflow tube, device, pipeline bracket, said overflow tube of a port is inclined downwards at one end, and with the marsh gas fermentation tank connected, and the other end the overflow tube of the connected device, a bottom set with biogas slurry tube device and a biogas tube b, a biogas tube of a liquid entrance is lower than liquid tube b of liquid entrance, a liquid tube a mounting said gate valve and electric valve. With the existing overflow a phase compare, this utility new type using first rear discharge mode of operation, the device a valid interception of activated sludge inner tank, increase the fermentation efficiency. When the electric valve in time e or need maintenance, or through other c a remove biogas pipeline, especially can prevent pipeline blockage, according to time sequence control removing biogas of activated sludge is good for inner cut-off pneuma biogas fermentation tank, increase the fermentation efficiency.
NOVELTY - This utility new type relates to a one a biogas pneuma tower, it comprise a methane tank and methane storage tower. A marsh gas tank comprise 1 # to 4 # preprocessing pool, slag-liquid tank, a separate tank underground, the 1 # tank through preprocessing fermenting tank is connected with 1 # 1 # transportation well, the 2 # tank through preprocessing fermenting tank is connected with 2 # 2 # transportation well, the 3 # tank through preprocessing fermenting tank is connected with 3 # 3 # transportation well, the 4 # tank through preprocessing fermenting tank is connected with 4 # 4 # transportation well, the 1 # to 4 # fermenting tank is connected with the underground slag discharging a liquid pool, underground separate tank, 1 # to 4 # transportation well is connected with a underground separate tank, 1 # to 4 # preprocessing tank, 1 # to 4 # fermenting tank in turn through annular channel connecting an annular tank, the 1 # to 4 # preprocessing tank, 1 # to 4 # tank top of the fermentation tank are set with a solar shed, marsh gas storage tower comprise the pneuma biogas tank and connecting with a 1 # to 3 # storage pneuma; the pneuma biogas tank and a 1 # to 4 # preprocessing tank, 1 # to 4 # is connected with the fermentation tank, the 3 # top part of storage cabin set with pneuma, one side thereof set with the biogas pneuma. This utility new type gas amount is large, a industrial production.
NOVELTY - This utility new type claims a garbage body one from a heat preservation degradation experiment device, containing garbage comprise body of the sampling bottle, temperature sensor, temperature sensor collect device and a gas collecting device, a temperature sensor on the inner sampling bottle, temperature sensor and temperature sensor data collect device connect, the sample bottle and the gas collecting device through connected pipe, temperature sensor collect garbage body temperature transfer to the temperature sensor data collect device, sample bottle produce gas by a gas collecting device collecting the sample bottle use a stopper seal. This utility new type one of a garbage body self heat preservation heat degradation experiment device, regulating water content, organic matter content, garbage degradation itself producing heat and the heat insulating bottle itself of a loss, simulate actual form a balance of garbage landfill body degradation producing a gas balancing system, form a typical of a one-liquid-coupling effect a pneuma, and using different monitoring method of each yield a gas component.
NOVELTY - This utility new type relates to manufacturing biomass energy using device, especially one manufacturing straw gas with a cooler, comprise a shell, set on the shell of a water inlet tube, a water tube, the air inlet tube and the pneuma tube, wherein the top part of said shell is fixed with a seal cover, the bottom of the seal cover fixed with the seal cover are of a clapboard between said clapboard and the upper seal cover form an air inlet cavity, a bottom of the inner cavity of the shell set with a lower baffle plate, the lower plate and the upper plate form a sealed water-containing cavity, a lower baffle plate and the inner cavity of the shell wall forming the air outlet cavity, in a water-containing cavity set with at least one of " U "-shaped disk tube, the rear U-shaped coil tube of the air inlet end passes through the upper baffle plate is connected with the air inlet cavity, the air outlet end of rear U-shaped coil tube passes through the lower baffle plate and the air outlet cavity; said water inlet tube and the water tube of the shell side wall, a water inlet tube and the external water source. This utility new type because of said structure has the following advantages: a cooling completely, reduces the energy consumption and reduces the manufacturing cost.
NOVELTY - This utility new type relates to manufacturing biomass energy using device, especially one manufacturing straw gas with a translation type energy-saving roasting furnace, comprise inner shell, a flue and furnace door, wherein the inner shell of said outer wall to outside in turn set with a insulating layer and a refractory brick layer, the inner shell and the insulating layer and a refractory brick layer are integrally form the furnace main body, a furnace top main body fixed with a base, the furnace main body and a base form a whole body, the furnace body is divided into mutually independent semicircular fixing body and a semicircular movable furnace body, between said inner shell and the heat insulating layer is set with reinforcing rib, said inner bottom fixed with a furnace core mounting platform, the furnace core mounting platform a set with at least one a furnace core, the furnace core through pipeline and gas source; a furnace body set with a rail. This utility new type because of said structure has the advantages of as follows: increase the safety, which increases the dry distillation kettle volume, reduces the energy consumption, shortens the production time, reduces the labour intensity and increase the environment protection.
NOVELTY - This utility new type inner one relates to a high efficient cavitation, include one tubular main body (1), the main body (1) inner cavity wall along the circumference direction is set one circle of bulge (2), the bump (2) of longitudinal section is triangle, (2) to make the main body (1) of the inner cavity forming one diameter of jet hole (5), the jet hole (5) forming by large to small inner diameter of front taper pipeline (2-1), a jet hole after forming by small to large inner diameter of rear taper pipeline (2-2), the rear tapered pipeline (2-2) is set with cone-shaped impeller (3). Time when the medium oil to a certain pressure and flow rate through cavitation effect generator, produce strong cavitation effect, so that grease, catalyste with methanol can fully contact, strengthening the mass transfer and heat transfer process in the esterification reaction process.
NOVELTY - This utility new type relates to the living sewage treatment device technology field, especially relates to a self-returning one biological rotating cage device. The self-returning rotating device include shell and biological contact tank set with a cage interior turning of a shell body, a shell, a cage of a one part is immersed in a liquid inside of a contact tank in, a cage set with a gravity return mix liquid for a self-returning device, the inner of said cage for forming biological film set with a filler. The self-returning rotating device using biological membrane biological rotating cage for a sewage treatment, with gravity self-flowing function, which is suitable for rural small domestic sewage treatment, a water outlet water quality high, it has low investment, quick effect, small floor area, simple mounting, convenient operation, long service life of use.
NOVELTY - Manufacturing a catalyst involves providing noble metal based particles, and in a reaction chamber exposing the noble metal based catalyst to a reaction mixture including an amine, and forming the catalyst.    USE - In alkyne hydrogenation reactions.    ADVANTAGE - The method enables a balance between absorption energetics of alkenes at the surface of nanoparticles as compared to nonselective capping ligands to thereby provide highly selective nanocatalysts for alkene in alkene hydrogenation reactions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) article of manufacture of a catalyst comprising a noble metal based catalyst material having a primary alkylamine coating on it; and    (2) performing a hydrogenation process of a hydrocarbon feedstock involving obtaining a noble metal based catalyst by (1) providing noble metal containing particles and (2) in a reaction chamber exposing the noble metal containing particles to a primary alkylamine to obtain a product catalyst, and flowing a feedstock over the product catalyst to hydrogenate the hydrocarbon feedstock to form a selectively hydrogenated product.
NOVELTY - Separation of solid involves comminuting a mixture of the solid in a liquid (L1) in which one of the components is lyophilic and the other component is lyophobic, and in a liquid (L2) which is immiscible with the liquid (L1) and which wets the lyophobic component to form agglomerates or floes of the lyophobic component and the liquid (L2) in a mill (10) having positive transport capability, in single step and in which the liquid (L2) comprises bio-oil and/or bio-diesel, and separating the agglomerates from the mixture.    USE - Separation of solid during beneficiation of coal containing ash (claimed).    ADVANTAGE - The method enables efficient and economical separation of solids with increased heating value, reduced sulfur content, reduced abrasion, and minimized ash handling and boiler derating.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process for beneficiating coal containing ash, which involves comminuting a mixture of coal, aqueous solvent and bio-oil and/or bio-diesel, to liberate at least a portion of the ash and coal in particulate form, and to form agglomerates or floes of the coal particles and the bio-oil or bio-diesel in a mill having positive transport capability, and separating the agglomerates or floes from the mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of mill.    Mill (10)    Housing (12)    Grinding surface (14)    Central shaft (18)    Vertical shaft (26)
NOVELTY - The method involves synthesizing a solid oxide fuel cell fuel anode through hydrazine reduction based on resultant temperature and pH change. The solid oxide fuel cell fuel anode is stirred in distilled water. A metal salt is made of copper(II) chloride, chromium(III) chloride, cobalt(II) chloride and iron(II) chloride. Hydrazine is dissolved in nickel chloride solution and sodium hydroxide at speed of 30ml/min. Initial temperature of starting material nickel chloride solution is controlled at 60 degree solution. Initial pH of the starting material nickel chloride solution is 6.5.    USE - Method for preparing high mass activity nickel-metal alloy nano powder that is utilized during synthesizing of a solid oxide fuel cell anode.    ADVANTAGE - The method enables increasing yield rate and crystallinity of nickel. The method enables controlling temperature and pH of a starting material. The method enables increasing hydrazine reduction. The method enables manufacturing spherical nano-size powder in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating relationship between intensity and temperature of a high mass activity nickel-metal alloy nano powder and photographic view of a high mass activity nickel-metal alloy nano powder.
NOVELTY - A candle scoop (200) comprises heat resistant handle (202); removably attachable thermally conductive scoop (204); and unit for attaching thermally conductive scoop to heat source.    USE - For scooping candle wax; and for making wax tarts for use with candle warmers.    ADVANTAGE - The present candle scoop provides effective way to remove the candle from the jar; thus user is able to find desired tart for use in their warmer, even though desired scent is available as candle. The present candle scoop is detachable and thermally conductive; thus it can be easily fits into the opening of the candle or other wax container.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of using candle scoop involving heating the scoop to desired temperature using heating unit; holding the scoop by handle; and scooping wax from candle or jar; and    (2) method of using thermally conductive scoop with soldering iron involving coupling thermally conductive scoop to soldering iron; allowing the scoop to reach desired temperature; and using the scoop to remove wax from candle or jar.    DESCRIPTION OF DRAWING(S) - The figure shows perspective side view of heated candle scoop with removable scoop.    Candle scoop (200)    Handle (202)    Removable scoop (204)    Shaft (206)    Securing mechanism (210)
NOVELTY - The system (1) has a gas engine (6) whose exhaust gas outlet (65) is connected with an inlet (71) of a post-combustion chamber (7). An exhaust gas outlet (75) of the post-combustion chamber is connected with a heating gas inlet (23) of a pyrolysis reactor (2). A pyrolysis gas outlet (25) of the pyrolysis reactor is connected with an inlet (31) of an oxidization chamber (3). A coke outlet (26) of the pyrolysis reactor is connected with an inlet of a reduction furnace (4). A product gas outlet (45) of the reduction furnace is connected with an inlet (61) of the gas engine.    USE - System for gasifying lumpy fuels i.e. biomass fuel such as timber or herbaceous substances.    ADVANTAGE - The system utilizes the gas engine and the pyrolysis reactor to easily heat a power-heat coupling, so that the system gasifies the lumpy fuels in a highly efficient manner. The heat transfer in the pyrolysis reactor can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasifying lumpy fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for gasifying lumpy fuels.    System for gasifying lumpy fuels (1)    Pyrolysis reactor (2)    Oxidization chamber (3)    Reduction furnace (4)    Gas engine (6)    Post-combustion chamber (7)    Heating gas inlet of pyrolysis reactor (23)    Pyrolysis gas outlet of pyrolysis reactor (25)    Coke outlet of pyrolysis reactor (26)    Inlet of oxidization chamber (31)    Product gas outlet of reduction furnace (45)    Inlet of gas engine (61)    Exhaust gas outlet of gas engine (65)    Inlet of post-combustion chamber (71)    Exhaust gas outlet of post-combustion chamber (75)
NOVELTY - A dehumidifier comprises electrolytic cell (10) which produces oxygen and hydrogen by electrolyzing electrolyte solution, and gas-liquid contact tank (20) which contacts dehumidification gas containing at least any one of oxygen and hydrogen produced in the electrolytic cell, with liquid, and removes the moisture content in the dehumidification gas.    USE - Dehumidifier is used for dehumidification of gas (claimed) obtained by electrolyzing water.    ADVANTAGE - The dehumidification of gas is simply and reliably performed using the dehumidifier, by an economical process, eliminating corrosion of piping.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dehumidification of gas, which involves producing oxygen and hydrogen by electrolyzing electrolyte solution, removing the moisture content contained in the dehumidification gas by introducing the dehumidification gas containing at least any one of oxygen and hydrogen produced during electrolysis process, and contacting with the liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the dehumidifier.    Electrolytic cell (10)    Gas-liquid contact tank (20)    Cooler (23)    Counterflow contact component (30)    Supply piping (31)
NOVELTY - The hydrogen generator comprises a surge tank for the electrolytic production of hydrogen-oxygen gas, which is connected horizontally with a first hydrogen generator. A second hydrogen generator is firmly connected and located behind the surge tank in a horizontal line to the first hydrogen generator in conjunction with a flow gasifier arranged perpendicularly such that water exchange operation is carried out by the hydrogen generator.    USE - Hydrogen generator.    ADVANTAGE - The hydrogen generator is highly mobile, and the need for an extra expansion tank is not necessary. The device is compact, and mobile supply of hydrogen-oxygen gas is enabled.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)
NOVELTY - Cultivating Dendrobium huoshanense comprises (i) taking heterologous fungal protein, Beauveria bassiana raw liquid, photosynthetic bacteria raw liquid and bioorganic fertilizer (nutritional water); and (ii) taking effective microorganism original dew and brown sugar, adding into cold boiled water, fermenting, adding Bacillus subtilis raw liquid, egg, milk powder, soybean powder, bone powder, fish meal, seaweed powder, white wine and rice vinegar, adding water, and preparing into spraying liquid, watering liquid and irrigating.    USE - The method is useful for cultivating Dendrobium huoshanense (claimed).    ADVANTAGE - The method increases the survival rate of Dendrobium huoshanense (claimed).    DETAILED DESCRIPTION - Cultivating Dendrobium huoshanense comprises (i) taking heterologous fungal protein with viable count of 0.02-0.1 hundred million/g, Beauveria bassiana raw liquid with viable count of 20-100 hundred million/g, photosynthetic bacteria raw liquid with viable count of 1-100 hundred million/g and bioorganic fertilizer (nutritional water); and (ii) taking 0.5-1.5 kg effective microorganism original dew and 4-6 kg brown sugar, adding into cold boiled water, fermenting for 24-30 hours at 18-25 degrees C, adding 0.5-1 kg Bacillus subtilis raw liquid (of viable count 10-100 hundred million/g), 2.5-5 kg egg, 2.5-5 kg milk powder, 2.5-5 kg soybean powder, 2.5-5 kg bone powder, 2.5-5 kg fish meal, 2.5-5 kg seaweed powder, 5-8 kg white wine of alcohol degree of 40-70 degrees , and 5-8 kg rice vinegar, adding 8-10% of water, according to weight of heterologous fungal protein, Beauveria bassiana raw liquid, photosynthetic bacteria raw liquid and bioorganic fertilizer (nutritional water) adding 100-1000 pts. water as spraying liquid for spraying, adding 100-500 pts. water as watering liquid for watering and adding 10-50 pts. water as irrigating liquid for irrigating.
NOVELTY - Quick production of greening substrate material comprises (i) dissolving sucrose in warm water and cooling to obtain sucrose solution, (ii) adding sucrose solution into clean container, stirring, statically placing for 1-2 days, adding complex bacterial liquid, stirring, sealing and culturing in clean and dark environment at room temperature for 25-30 days to obtain microbial fermentation liquid, and (iii) spraying microbial fermentation liquid on surface of fermented organic substance using sprayer, cover with thin film clinker and fermenting for 25-45 days to obtain substrate material.    USE - The method is useful for quick production of greening substrate material (claimed).    ADVANTAGE - The method utilizes variety of organic wastes, reduces nutrient loss caused by waste, solves composting problems and problems associated with livestock manure, sludge and other organic waste, reduces rate of infectious disease and is environmentally friendly.
NOVELTY - A fuel material is molded by carrying out compression-processing or heat-compression processing of material containing a plant-derived powdery main material and heat-generating material with fine coal having electrical conductivity. The obtained molded material is irradiated with microwave such that heat-generating material generates heat, and obtained product is solidified into rod-shape, spherical shape, aggregated form or granular form. The whole fuel material is heated and heat-processed using heat-generating material as a nucleus.    USE - Heat-processing of fuel material e.g. non-carbonized material, high-temperature hard charcoal, low-temperature soft charcoal and artificial material wood (all claimed), and carbonated material.    ADVANTAGE - The method enables safe heat-processing of fuel material by controlling the temperature of the heating with microwave, without microwave leakage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbonization apparatus of artificial material wood, which consists of electromagnetically-shielded casing for mixing (AA) plant-derived powdery raw material and fine coal as heat-generating material, and microwave heating furnace (2) for carbonizing the artificial material wood formed by compression molding and heat-compression molding plant-derived powdery raw material. The microwave heating furnace is formed using material having nonmagnetic property and heat resistance. The microwave heating furnace is extended in the casing from the inlet port and exit of the artificial material wood formed in the casing, and provides the guide pipe for shielding air tightly between internal space and the space in the casing.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining manufacture of fuel material. (Drawing includes non-English language text)    Ogalite molding machine (1)    Microwave heating furnace (2)    Mixing (AA)
NOVELTY - Extracting ferulic acid present in an aqueous phase, comprises (a) treating a plant material followed by solid/liquid separation to recover a solid phase and an aqueous phase comprising ferulic acid and polysaccharides, (b) treating the liquid phase for selectively separating the polysaccharides and ferulic acid, (c) optionally, concentrating the aqueous fraction containing ferulic acid to recover concentrated ferulic acid, and (d) recovering solid form ferulic acid.    USE - The method is useful for extracting ferulic acid present in an aqueous phase. The ferulic acid is useful in a bio-fermentation process to produce natural vanillin in the presence of microorganisms (all claimed), and in chemical, cosmetic, pharmaceutical, biotechnology and food industry. No biological data given.    ADVANTAGE - The method eco-friendly and economically extracts the ferulic acid with a purity of greater than 95%, preferably greater than 99%, high yield and improved recovery of co-processing products and using reduced amount of water.
NOVELTY - Converting a contaminated liquefied petroleum gas (LPG) stream comprising 3C and/or 4C, and further comprising 80-20 mol.% of dimethyl ether (DME) into a purified LPG stream, comprises: extracting the DME from contaminated LPG stream with an extractant, that results in a purified LPG stream, and an extract stream comprising the DME and the extractant; and feeding the extract stream to an oxygenate-to-olefin (OTO) process at conditions, so that the DME reacts to form olefins.    USE - The process is useful for converting contaminated LPG stream into purified LPG stream, and extracting olefins (claimed) including ethylene or propylene.    ADVANTAGE - The process: provides the LPG stream with improved purity; and reduces the operating and capital expenses, as compared to conventional processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing oil and/or gas from an underground formation, including: a well above the formation; a mechanism to inject an enhanced oil or gas recovery formulation into the formation; an extraction installation; and an OTO reactor.
NOVELTY - Extracting ferulic acid present in an aqueous phase, comprises (1) treating a plant material followed by a solid/liquid separation to recover a solid phase and an aqueous liquid phase comprising the ferulic acid and polysaccharides; (2) treating the liquid phase to selectively separate the polysaccharides and the ferulic acid present in an aqueous fraction; (3) concentrating the aqueous fraction containing the ferulic acid so as to recover a ferulic acid-concentrated stream; and (4) recovering the ferulic acid in solid form.    USE - The method is useful for extracting ferulic acid present in an aqueous phase, where the ferulic acid is useful in the bio-fermentation process to produce natural vanillin in the presence of microorganisms (all claimed), and as a raw material in a chemical industry, cosmetic industry, pharmaceutical industry and biotechnology or food industry. No biological data given.    ADVANTAGE - The method is capable of eco-friendly and economically extracting the ferulic acid present in the aqueous phase with high yield, high purity of higher than 80%, preferably 99% and improved recovery of co-processing products, using reduced amount of water.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for extracting ferulic acid present in an aqueous phase (Drawing includes non-English language text).
NOVELTY - The purification unit has a first bed comprising an adsorbent layer (A) to stop partial impurity and a second bed successively including nitrogen layers (B1, B2) with adsorbents structure and cationic composition. A third bed includes an adsorbent layer i.e. zeolite layer (C1), where volume of adsorbent contained in the first bed represents less than 15% of total volume of adsorbent contained in an adsorber. The adsorbent layer of the first bed presents a same structure and a same cationic composition as the nitrogen layer of the second bed.    USE - Purification unit for purifying a gaseous mixture containing hydrogen, carbon dioxide and gas selected from methane, carbon monoxide and nitrogen, and impurity solution of water, methanol, formic acid, heavy hydrocarbons, ammonia and hydrogen sulfide.    ADVANTAGE - The bed has nitrogen layers with adsorbents structure and cationic composition, and another bed includes adsorbent layer, thus improving separation and purification of the gaseous mixture with better quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a production unit    (2) a method for purifying a gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a purification unit.'(Drawing includes non-English language text)'    Adsorbent layers (A)    Nitrogen layers (B1, B2)    Zeolite layers (C1, C2)
NOVELTY - Treating aqueous organic, ammonia and/or ammonium ion-containing residues (2) comprises concentrating the ammonia and/or ammonium ion-containing residues by evaporation to produce a concentrate and ammonia-containing vapors (6), and introducing the resulting ammonia-containing vapors into a vapor washer (50) containing an acid (9), which reacts with the ammonia to form an ammonium solution such that the vapors exiting from the vapor washer are free of ammonia.    USE - The method is useful for treating aqueous organic, ammonia and/or ammonium ion-containing residues from the anaerobic processes such as biogas production and/or anaerobic digesters of sewage treatment plants and/or from animal husbandry (claimed), to prepare a fertilizer.    ADVANTAGE - The method is capable of treating the aqueous organic, ammonia and/or ammonium ion-containing residues in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for treating aqueous organic, ammonia and/or ammonium ion-containing residues comprising an evaporator in which the residues are introduced and heated, so that the residues are thickened to produce concentrate and ammonia-containing vapors, a vapor washer connected to the evaporator, and an acid metering unit for adding acid to the vapor washer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for treating aqueous organic, ammonia and/or ammonium ion-containing residues.    Ammonia and/or ammonium ion-containing residues (2)    Ammonia-containing vapors (6)    Acid (9)    Capacitor (11)    Vapor washer. (50)
NOVELTY - Each block comprises organic components of different kind and plant mass (waste) of initial moisture with height of 50-60 cm. Each block is covered with a layer of soil with the height of 8-10 cm and kept for 4-5 days. Before laying the next block the previous blocks are mixed. The first block consists of a layer of straw with height of 70-80 cm, poured with liquid manure and covered with a layer of plant mass. In the subsequent blocks - first layer is the plant mass, at that the second and third blocks are layers of peat and sawdust, respectively, with height of 50-60 cm, poured with post-distillery stillage, and the fourth block is chicken manure with height of 30-40 cm.    USE - Agriculture.    ADVANTAGE - Rapid maturation of compost, environmental friendliness and increase in soil fertility.1 dwg
NOVELTY - Methane tank comprises a vertical cylindrical container enclosed in the heat-insulating jacket, with conical bottom and spherical case, where the container is equipped with branch pipe having not greater than 1/3 height of container, as the input of organic waste, and the processed substrate is unloaded from the branched pipe for the withdrawal of biogas.    USE - The methane tank is useful in anaerobic digestion of the diluted organic waste (claimed).
NOVELTY - Composition comprises a mixture of bacteria that can produce hydrogen gas which contains 20-60% of Rhodobium sp. and 40-80% of Marichromatium sp..    USE - The composition is useful for producing pure hydrogen gas from a substrate that is carbohydrates and waste biomass, preferably in the form of glucose (all claimed).    ADVANTAGE - The composition produces hydrogen gas which is clean, safe and sustainable, does not leave toxic compounds, and reduces greenhouse gas emissions in the air.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for using a mixture of bacteria with the composition producing hydrogen gas from a substrate in a solution of media comprising: making a solution of a mixed bacterial culture media and cultivation of bacteria mixture; making hydrogenases media solution for the growth of bacteria mixture; photo-fermentation of the hydrogenases media solution in a bioreactor; and draining and purifying the resulting gas mixture by using absorbent carbon dioxide gas to obtain pure hydrogen gas.
NOVELTY - Composition comprises at least: a mixture of bacteria Bacillus mojavensis TMG04 and Streptomyces malayensis VC100 containing as much as 5x 106-5x 1010 (preferably 5x 108) spores for each plant; a medium for the growth of bacterial mixture, which is a sporulation broth; a mixture of other bacteria such as Pseudomonas, Azotobacter and Flavobacterium; and fertilizers comprising 10-50% of the total composition.    USE - The soil improvement composition is useful for application on degraded land, mined land, deforested land, less fertile land, sandy soil land, and dry and nutrient-deficient land to stabilize and protect plants root, stimulate root growth, maintain soil aggregates to hold water, inhibit pathogenic fungi, remodel organic matter into nutrients ready for the plant, support the availability of nutrients such as carbon, nitrogen, phosphate, minerals and phytohormones, and as natural pesticide (claimed). Test details are described but no results given.    ADVANTAGE - The composition: improves the soil fertility by supporting and stabilizing soil aggregates; protects plant roots; and improves the efficiency of fertilizer for plant growth in critical land area.
NOVELTY - Bioinoculant consortium biofertilizer comprises (a) organic peat-based carrier material, and (b) active ingredient comprising Azotobacter, Azospirillum, Pseudomonas and Bacillus isolated from rice field with density of at least 107 colony forming unit (cfu)/g.    USE - The bioinoculant consortium biofertilizer is useful for wetland ecosystem (claimed).    ADVANTAGE - The bioinoculant consortium biofertilizer increases availability of nutrients, rice crop yield, and soil fertility.
NOVELTY - Method of preparing plant-derived organic fertilizer involves (a) choosing plant biomass chosen from soybean and corn, and sterilizing the resulting raw materials, (b) inoculating Bacillus sp strain J10.20 and Pseudomonas diminuta strain onto the sterilized raw materials and allowing multiplication of bacterial strains in nutrient broth medium, (c) culturing the inoculum, and (d) incubating the resulting biomass to obtain product.    USE - The method is useful for preparing plant-derived organic fertilizer (claimed).    DETAILED DESCRIPTION - Method of preparing plant-derived organic fertilizer involves (a) choosing plant biomass chosen from soybean and corn, cutting chosen raw materials to have size of 1 cm or less and sterilizing the resulting raw materials, (b) inoculating Bacillus sp strain J10.20 and Pseudomonas diminuta strain onto the sterilized raw materials and allowing multiplication of bacterial strains in nutrient broth medium for 3 days, (c) culturing the inoculum till the biomass reaches 1008 or more colony-forming unit (CFU)/g of raw material, and (d) incubating the resulting biomass for 2-3 days to obtain product.
NOVELTY - The gasifier has a pellet granulator (5) that is provided in hot gas furnace to mold a biomass feedstock into pellet form. The furnace is provided to heat gasification reaction installation which gasifies biomass feedstock. The granulator is provided with a throwing in portion (54) for throwing in biomass feedstock between dies (52) in which some holes (51) are formed and roller (53) which is turned while revolving the dies top. The biomass feedstock is molded into pellet form by passing through the hole while the feedstock inserted between dies and roller is pressurized by roller.    USE - Gasifier for gasifying biomass such as wood chip, paper garbage, organic refuse, used tea leaves, and coffee husk, and producing clean high calorie gas used in gas engine for electric power generation.    ADVANTAGE - Since the biomass feedstock of hot gas furnace is molded into pellet form, the conveyance and supply of biomass feedstock at hot gas furnace is performed smoothly. The biomass is gasified and clean high calorie gas is provided efficiently with improved gasifier.    DETAILED DESCRIPTION - The pellet granulator is provided as a non-hydration type granulator to pressurize the biomass feedstock only with the moisture content of biomass feedstock, and mold into pellet form. The biomass feedstock is included with a mixture of city area waste materials other than paper garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the pellet granulator.    Pellet granulator (5)    Hole (51)    Die (52)    Roller (53)    Throwing-in portion (54)
NOVELTY - Manufacturing wood vinegar involves utilizing timber (50 wt.%) which is subjected to dry distillation process at 180-250 degrees C and then 500-650 degrees C to form vapor. The vapor is condensed to obtain the desired product.    USE - Method for manufacturing wood vinegar (claimed).    ADVANTAGE - The method enables to manufacture wood vinegar that has antiviral property and no harmful effect on human or animal.
NOVELTY - Method for processing biomass, involves crushing biomass coarsely to obtain powder with predetermined particle size, milling coarse powder into fine particles, treating fine powder with solution containing acetic acid and inorganic acid, obtaining residual mixture containing cellulose and hemicellulose, and removing residues from solution.    USE - The method is useful for processing biomass (claimed).    ADVANTAGE - The method produces high yield of bioethanol and lignin in cost-effective manner, consumes less power and energy, and is simple.
NOVELTY - Liquid mixture is prepared by mixing (a) extract of bamboo and extract of plant containing an antioxidant, and (b) culture solution of photosynthetic bacteria and lactic acid bacteria.    USE - The liquid mixture is useful in fertilizer or soil conditioner (claimed) for deodorizing and stimulating fermentation of activated sludge and manure in soil, improving soil, promoting growth of agricultural product, and controlling insect pest and plant diseases.    ADVANTAGE - The liquid mixture exhibits rapid growth promotion effect on the agricultural products.
NOVELTY - The apparatus (1A) has several cylinders (31-38) which are arranged in parallel to each other, and connection sections (42-48) each of which connects adjacent two of the cylinders to form a water channel. Each cylinder is provided with a bio-filtration section using an aerobic bacterium, and one cylinder is provided with a biological filtration section using an anaerobic bacterium. A regulating valve (5) is provided in the connection section, for arbitrarily controlling flow volume of water to be purified which flows into the bio-filtration section.    USE - Purification apparatus e.g. filter apparatus for purifying water such as domestic waste water and sewage.    ADVANTAGE - By utilizing closed elongate water channel, the purification efficiency of the filter apparatus is improved, and the purification apparatus is maintained easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the filter apparatus.    Filter apparatus (1A)    Pump (2)    Regulating valve (5)    Cylinders (31-38)    Connection sections (42-48)
NOVELTY - Operating a biogas plant for continuous single-stage fermentation of a substrate mixture comprising a biogas fermenter and a separation unit, comprises separating the digestate and process water fermented in fermentation substrate of the biogas fermenter in the separation unit, and recycling the process water is into the biogas fermenter. The substrate mixture contains predominantly animal manure and the amount of recycled process water is adjusted such that fermenter contents in the biogas digester has a dry residue of at least 16%.    USE - The method is useful for operating a biogas plant for continuous single-stage fermentation of a substrate mixture (claimed).    ADVANTAGE - The method: is simple; and allows separation of highly viscous process water from the sand-containing fermentation substrate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) operating a biogas plant for continuous fermentation of animal manure with a biogas fermenter, comprising circulating the fermenter contents by a main laminar gear, and recycling fermenter contents with a turbulent sub agitator in the region adjacent to the upper surface; and    (2) a biogas plant for continuous fermentation of animal manure comprising a single-stage biogas fermenter, separation, a recycling line provided to recycle process water in the biogas fermenter and a flow device provided to adjust the stream of recycled process water.
NOVELTY - The reactor has thermal pipes whose sections of the zones of the condensation of the heat-transfer agent are placed in the biomass, and the portions of the areas of boiling of the heat-transfer agent of heat pipes are installed in heating chamber. A variable container whose built-in gas holder is fixed under the case of the rector through suspension, and dome consists of the cables fixed by ends to mortgage elements of housing wall and the upper mounting flange that installed on the support column, whose base is fixed on the bottom of reactor.    USE - Biological reactor for anaerobic processing of biomass from agricultural and industrial wastes.
NOVELTY - The present invention addresses methods and equipments for a high-rate production and improvement of the quality of organic fertilizers from organic wastes, by processes including Screening, Mechanical Pretreatment, Physical-Chemical Pretreatment, High-Rate Stabilization Process, High-Rate Activation Process, and Product Refining Processes, and adding seven types of chemical agents including: Wetting Agents, Debonding Agents, Organic Stabilization Agents, Inorganic Stabilization Agents, Fluffing Agents, Activation Agents, and Nutrient Agents in order to enhance six major properties which activated characteristics of composts: (a) moisture absorption and holding capability, (b) nutrients adsorption and holding capability, (c) soil particles holding and conserving capability, (d) soil air ventilation capability, (e) soil water transmission capability, and (f) soil thermal insulation capability, as well as other minor quality improvements such as complete sterilization of pathogens and parasites, detoxification of many hazardous chemical species, and removal of excess heavy metal contents, if any, from the activated organic fertilizer products.
NOVELTY - Microorganism composite fertilizer comprises (in pts.wt.): bamboo leaf (60-90), pig manure (20-40), soybean meal (22-26), egg shell (10-14), lees (12-20), medical stone (22-26), attapulgite (19-23), gypsum (6-8), hummus (10-12), calcium superphosphate (10-15), urea (8-10), ammonium sulfate (5-8), potassium chloride (4-7), zinc sulfate (2-4), ferrous sulfate (2-4), borax (2-4), ammonium citrate (2-4), microbial inoculum (2-6), brown sugar (2-6) and rest amount of water.    USE - Microorganism composite fertilizer.    ADVANTAGE - The microorganism composite fertilizer is manufactured in a simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing microorganism composite fertilizer, which involves:    (A) crushing bamboo leaf to obtain bamboo leaf powder;    (B) mixing microbial inoculum and brown sugar to the bamboo leaf powder;    (C) culturing the mixture for 24 hours;    (D) crushing pig manure, soybean meal and egg shell;    (E) adding the mixture to the cultured material;    (F) adding urea, ammonium sulfate, calcium superphosphate, potassium chloride, potassium sulfate, zinc sulfate, ferrous sulfate, borax and ammonium citrate to the mixture; and    (G) fermenting the mixture for 20-40 days to obtain the microorganism composite fertilizer.
NOVELTY - Waste water treatment material comprises 30-50 pts. wt. magnesium carbonate, 10-30 pts. wt. calcium hydroxide, 10-30 pts. wt. activated carbon, and 10-30 pts. wt. calcium chloride with respect to 100 pts. wt. zeolite.    USE - The treatment material is useful for removing phosphorus (claimed), ammonium nitrogen, nitrite nitrogen, organic material and heavy metal.    ADVANTAGE - The treatment material reduces sludge; has low chemical consumption; maximizes removal effect in short time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing waste water treatment material, comprising (a) mixing water in 100 pts. wt. zeolite including silica, alumina, magnesium oxide, calcium oxide, sodium oxide and iron oxide, 30-50 pts. wt. magnesium carbonate, 10-30 pts. wt. calcium hydroxide, 10-30 pts. wt. activated carbon, and 10-30 pts. wt. calcium chloride at 58-65 degrees C for 50-70 min to obtain mixture , (b) solidifying the obtained mixture by drying, and (c) crushing the solidified mixture.
NOVELTY - A polyethylene container comprises polyethylene resin, hindered amine compound (A) containing triazine-type repeating unit (I), hindered amine compound (B), stabilizer comprising amine compound and antioxidant.    USE - Polyethylene container is used for storing biodiesel.    ADVANTAGE - The polyethylene container has excellent flexural strength, impact strength and durability.    DETAILED DESCRIPTION - A polyethylene container comprises polyethylene resin, hindered amine compound (A) containing triazine-type repeating unit of formula (I), hindered amine compound (B), stabilizer comprising amine compound and antioxidant.
NOVELTY - Manufacturing liquid organic fertilizer, involves preparation of fertilizer materials, mixing, fermentation for 7 days, and packaging.    USE - The process is useful for manufacturing liquid organic fertilizer, which is useful as a nutrient for plants, and as organic pesticides to crops more resistant to pests and plant diseases (claimed). No biological data given.    ADVANTAGE - The organic fertilizer: contains high amount of macro- and micro-elements needed by plants; is in the form of liquid, that can be absorbed more quickly and directly by the roots of plants; increases the activity of beneficial soil microorganisms; and improves soil structure, so that the land becomes fertile, safe and environmentally friendly.
NOVELTY - Increasing production of bioethanol on starch hydrolyzate medium using Saccharomyces bacteria, comprises: preparing starch hydrolyzate, which is sago starch hydrolyzate, with certain sugar concentration; introducing hydrolyzate into bottle bioreactors; adjusting pH of liquid substrate; sterilizing; adding ammonium sulfate as source of nitrogen and trace elements; inoculating media with inoculum yeast Saccharomyces ellipsoideus; cultivating by adjusting pH and room temperature; agitating and aerating; and stopping agitation and aeration after cultivation.    USE - The process is useful for increasing production of bioethanol on starch hydrolyzate medium using Saccharomyces bacteria.    ADVANTAGE - The process increases yield of bioethanol in batch cultivation.    DETAILED DESCRIPTION - Increasing the production of bioethanol on starch hydrolyzate medium using Saccharomyces bacteria, comprises: preparing starch hydrolyzate, which is sago starch hydrolyzate, with certain sugar concentration; introducing hydrolyzate into bottle bioreactors; adjusting pH of liquid substrate; sterilizing the hydrolyzate medium; cooling and adding ammonium sulfate after as a source of nitrogen and trace elements; inoculating the media with inoculum yeast Saccharomyces ellipsoideus in an aseptic conditions; cultivating by adjusting pH and room temperature; agitating and aerating; and stopping the agitation and aeration after cultivation for certain time to increase the production of bioethanol.
NOVELTY - The apparatus has air supply assemblies (200,300) and heat exchange unit that are equipped in reactor (100). An air supply amount is controlled during oxidative process according to constellation of biomass put into reactor. A gasification process reuses high sensible heat of synthetic gas that is ejected via heat exchange unit (400) according to constellation of biomass put into reactor. The sensible heat of ejected synthetic gas is collected and temperature of air supplied to oxidizing agent during the gasification process is increased.    USE - Gasification reaction apparatus.    ADVANTAGE - The biomass put into the reactor is enabled to increase the energy efficiency of apparatus, and the productivity of synthetic gas is enlarged in highly efficient manner. The wastage of unnecessary energy is minimized, and the production efficiency of synthetic gas is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the gasification reaction apparatus.    Reactor (100)    Air supply assemblies (200,300)    Heat exchange unit (400)    Exhaust unit (600)    Grate assembly (630)
NOVELTY - One a municipal drain pipe network sewage flow processing system, comprise flow inspection well, refluxing and inspection well sewage distributing well array and sewage flow process a message node, sewage distributing well array in turn connected in series comprise a sediment well, water well and a clean water well, well through flow tube and the shunting a inspection well, water well through the recycling tube connect sewage recycling system, by a backflow tube a return inspection well, a water well by biogas pneuma tube a marsh gas collecting system, to return the inspection well set with the sewage main pipe, main pipe or the branch tube and a sewage treatment plant and connected, a message set with the shunt tube a. This utility new type a rear sewage source sewage all the discharge, reduces process for municipal water pollution, a local processing and recycling sewage, which is good for a municipal regional benign water circulation to avoid dramatically construction investment and a long-term empty waste and sewage classification process is good for reducing sludge and the increase of centralized sewage treatment facility water quality.
NOVELTY - Method for performing thermal digestion of biomass, involves supplying fresh biomass, preheating supplied fresh biomass, hydrolyzing preheated biomass, cooling hydrolyzed biomass, and discharging cooled biomass, where the supplied biomass is preheated by mixing at least supplied biomass with at least portion of the hydrolyzed biomass.    USE - The method is useful for performing thermal digestion of biomass (claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for installation system.
NOVELTY - This utility new type provide a one capable of a biological active substance propagation of biological paddle low in natural state, a multifunctional propagation and biological pesticide application device, biological medicine applying device set storage function, a stir, biological activity is a propagation function as a whole, the design is simple, economical, and can make the biological activity is a fast propagation low in natural state, so that the biological activity is the most large valid biological equivalent is a short inner, valid reduces use cost and applied to the drug particles of small particle diameter, , object valid can be absorbed is a set one time, saving water, saving aritificial, energy-saving, convenient, environment-friendly and so on in a medicine applying device, the current technology is saved relative drug at least 30 to 70% or more, a widely used for agricultural application, the air humidifying, sterilizing and air pollution treatment and so on.
NOVELTY - Method of producing betulinic acid 3-sulphate derivatives by reacting betulinic acid with a sulphating agent while continuously mixing and heating, where the sulphating agent used is a mixture of sulphamic acid and urea in N,N-dimethylformamide, sulphation is carried out under defined conditions, and the product is separated by cooling, diluting the reaction mass with water, extraction with butyl or isoamyl alcohol, washing with water, treating the alcohol extract, followed by concentration of the alcohol layer and separating the end product.    USE - Chemistry.    ADVANTAGE - Method is environmentally friendly and widens the range of sulphated betulinic acid derivatives.
NOVELTY - Separation and purification of cordycepin involves: homogenizing deer hoof safflower extract by inducing enzyme hydrolysis to obtain solid substance; extracting the solid substance using negative pressure cavitation extracting technology process; extracting the induction and hydrolysis liquid and rear negative pressure cavitation extracting liquid by combining the concentrate through ultrasonic oscillation flocculation technology, and a liquid-solid extraction technology; followed by separating a plum hat cordycepin crude product and crystallizing.    USE - For separation and purification of cordycepin (claimed) for treating cardiovascular disease.    ADVANTAGE - The method provides cordycepin having purity of more than 95%; is simple and easy process, produces cordycepin with high yield; is economical, safe and environment-friendly; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Separation and purification of cordycepin from deer hoof safflower extract involves: (1) obtaining solid substance: homogenizing deer hoof safflower extract by inducing enzyme hydrolysis; (2) extracting the solid substance using negative pressure cavitation extracting technology process; extracting the induction and hydrolysis liquid and rear negative pressure cavitation extracting liquid by combining the concentrate through ultrasonic oscillation flocculation technology, and a liquid-solid extraction technology; (3) separating a plum hat cordycepin crude product from the extract liquid using a secondary pressure normal phase silicon glue column chromatography; and (4) crystallizing the crude product of plum hat cordycepin at low temperature crystallization and recrystallization technology to obtain cordycepin having purity of 95%.
NOVELTY - Bacillus tequilensis (ZSGD5), comprising a preservation number CCTCC NO: M2014004, is new.    USE - The complex microecological preparation is useful in aquaculture product for treating pond bottom water; controlling aquaculture water bait material residue and fecal contamination, maintaining increased dissolved oxygen, inhibiting bottom moss, and reducing ammonia nitrogen, amount of nitrite and hydrogen sulfide; and managing municipal channel black water and muddy water (claimed).    ADVANTAGE - The complex microecological preparation: can improve state of dead black river and reduces the river water chemical oxygen demand value to 40% (claimed). The strain is introduced into the bottom water-body to be purified with high decomposition rate, thus reducing sludge.    DETAILED DESCRIPTION - . An INDEPENDENT CLAIM is also included for a complex micro-ecological preparation, comprising Bacillus tequilensis (ZSGD5), first class Bacillus subtilis, second class Bacillus subtilis, first class Bacillus licheniformis, second class Bacillus licheniformis, Bacillus pumilus and Bacillus megaterium. The Bacillus tequilensis, first class Bacillus subtilis and first class Bacillus licheniformis has a preservation number respectively of CCTCC NO: M 2014004, CCCTC NO: 2011443 and CCTCC NO: M 2012458.
NOVELTY - A NTRO oxidoreductase comprising a 259 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The NTRO oxidoreductase is useful for converting oxidized coenzyme NAD+ to reduced coenzyme NADH, and oxidized coenzyme NADH+ into reduced coenzyme NADPH, and useful in ketone-alcohol conversion (all claimed).    ADVANTAGE - The NTRO oxidoreductase is energy-saving and environmentally-friendly.
NOVELTY - A PIC pig green farming method involves performing solid-liquid separation on pig manure, separating solid part of fermentation liquid, discharging marsh gas from the tank part of a marsh gas production, fermenting pig manure to the field as fertilizer for crops, marsh gas for fuel into the digester, passing precipitate before entering into a marsh gas tank to the field as fertilizer of crops in the sedimentation tank.    USE - PIC pig green farming method.    ADVANTAGE - The method enables strengthening the health and epidemic prevention, manure and dead livestock handling, reducing the generation of pollutants, and turning waste into treasure.
NOVELTY - This utility new type claims a piggery marsh gas waste liquid one farmland irrigating system, comprising a marsh gas generating device, the liquid outlet of marsh gas generating device through a pump and a liquid tube and liquid tank connected, or, the liquid outlet with the sedimentation tank of said marsh gas generating device connected, sedimentation tank through a pump and a liquid tube and liquid tank connected, a storage liquid tank side is set with liquid storage tank, a liquid inlet of the liquid storage tank through liquor pump and liquor tube and a marsh gas-liquid inner said tank connected, one end with the main discharging tube of infusion of a liquid storage tank connected, a main transfusion tube of the other end and the branch transfusion tube connected, up each branch transfusion tube are set with a control valve. The end port of said branch transfusion tube is higher than the ground. This utility new type liquid storage tank connected with the multi-time a marsh gas generating device, which can for marsh gas of the pig field waste liquid treatment process and storing the farmland drought time, liquor pump and infusion tube through the marsh gas waste liquid transportation to farmland in, a irrigation, high comprehensive utilization rate.
NOVELTY - This utility model new supply of one of horizontal biomass grain machine and machine head mechanism, comprising organic head plate, a discharging end head plate is provided with a discharging passage, upper head plate between fixed between installation with, head plate and top end provided with supporting plate, machine head plate is set with fixed plate, supporting plate and fixing plate is connected with main way hole, supporting plate and fixing plate equipped with at least one gap of the same reinforcing plate. This new utility model the product as horizontal machine, production time grinding plate not rotate, only pressure rotary disc through high temperature process production, material is alloy steel, hole diameter of compression than the extrusion hole on the disc, this reasonable design and high safety, yield is more reasonable.
NOVELTY - This utility model new supply of one of horizontal biomass grain machine and scraper supporting device, comprises with setting on disc of the scrape material cylinder, upper scrape material cylinder out side set with round, scrape material cylinder out side on the bottom by fixed bolt set with at least one of support block. This new utility model the product as horizontal machine, this can make scraping support mechanism is more stable, so can avoid the time of rotating scraper scraping driving supporting mechanism rotate, but result in machine, at the same time can support normal operation of scraping device, so increase of production efficiency, scraping device is set above the speed reducing electrical machine can make the scraping speed would not too fast, scraping compare uniform, so can reducing of production of particle, saving of resource, increase of production efficiency.
NOVELTY - This utility new type provide the one horizontal biomass granule machine of a main shaft device, and the other end comprise one end with the chassis frame, the chassis frame set with a motor, a chassis frame set with a distribution box, bottom end of chassis frame set with the main shaft transmission mechanism, a chassis frame machine disk head, a discharging end of the head disk is connected with a discharge channel, discharging end of machine head inner disk is set with leaking openings, machine head disk through bearing mounting with a main shaft mechanism. This utility new type the product is a horizontal machine, a time grinding disk does not rotate, only the pressure rotary, so that design is reasonable, the safety performance is high, yield is high, increase the production efficiency, at the same time, extend the use life of machine.
NOVELTY - This utility model new supply of one of horizontal biomass, the other end comprises one end with the chassis frame, the chassis frame is equipped with motor, the chassis frame is equipped with distribution box, bottom end of chassis frame provided with a main shaft transmission mechanism, a chassis frame of machine head plate, the discharging end of the head plate is connected with the discharge passage, a discharge end head plate to set with the leaking openings, upper head plate card inside, provided with machine head plate via shaft mount can carry out rotation with the main shaft mechanism. This new utility model the product as horizontal machine, grinding the extruded hole of hole diameter and compression ratio is variable, this reasonable design and high safety, yield is more reasonable, and the scraping device is set above the speed reducing electrical machine can make the scraping speed would not too fast, scraping compare uniform, so can reducing of production of aggregates, saving of resource, increase of production efficiency and prolongs the using life of the machine, at the same time when save more labour force.
NOVELTY - Preparing fermented bagasse product, involves (a) crushing sugarcane bagasse, mixing the crushed product with potassium sulfate and lignite, and mixing the obtained mixture with phosphorus, (b) dissolving nitrogen in water to obtain aqueous solution of nitrogen, mixing the solution with the product obtained in step (a), (c) culturing Bacillus subtilis and adding the culture to the solution obtained in step (b), (d) mixing obtained product with pre-fermentation material, and stirring the mixture, and (e) fermenting the obtained product.    USE - The method is useful for preparing fermented bagasse product (claimed).    ADVANTAGE - The method is rapid, and cost-effective, and prepares fermented bagasse product at high yield. The fermentation tank used in the method requires less space.    DETAILED DESCRIPTION - Method for preparing fermented bagasse product, involves (a) crushing 60-80 pts. wt. sugarcane bagasse, mixing the crushed product with 5-15 pts. wt. potassium sulfate and 10-30 pts. wt. lignite, and mixing the obtained mixture with 1-2 pts. wt. phosphorus, (b) dissolving 2-3 parts nitrogen in 20 parts water to obtain aqueous solution of nitrogen, mixing the solution with the product obtained in step (a) in a ratio of 25:1-30:1, (c) culturing Bacillus subtilis and adding the culture to the solution obtained in step (b), (d) mixing obtained product with 80-118 %mass pre-fermentation material, and stirring the mixture for 5-10 minutes, and (e) fermenting the obtained product in fermentation tank under natural conditions for 50-60 days.
NOVELTY - Preparing seedling soil for soil transfer disease involves forming fresh eating bran, garden and cow dung according to the volume ratio of 2 to 3.5: 1 to 1.5: 0.1 to 0.5, uniformly mixing to form mixture, regulating water content to the mixture, adding water, heating the mixture at 55-65 degrees C, fermenting the mixture, and decomposing for 38-42 days.    USE - For preparing seedling soil for soil transfer disease (claimed).    ADVANTAGE - The method is simple; has mild condition; fully kills harmful pathogenic micro-organism; greatly reduces the influence of plant diseases and insect pests; improves the growth environment of crop; and reduces disease of crop.
NOVELTY - In this utility new type relates to one suitable for a water hyacinth fermentation fishing tank of high-efficient circulation module using stacking, include substrate layer (10), water block layer (20) and a straw layer (30), substrate layer (10) is straw layer of 10 cm thick (10) upper surface add one layer water block layer (20), water block layer (20) add sheep 0.70 cm, water bottle layer (20) upper surface add one layer of straw layer (30), a straw layer (30) thickness is 2 cm. The straw layer (30) upper surface add one layer water block layer (20), in turn straw layer (30) and water bottle layer (20) using 6 layer are overlapped. This utility new type has simple structure, through water hyacinth extract rich in nutrition, the hyacinth is transferred to , through natural fermentation, then mixing into in culture earthworm manure of organic substrates, turtle to eat the organic substrate culture from a of earthworm, turtle of enhance adaptability, disease, increase survival rate, bait coefficient reduced.
NOVELTY - This utility model new supply of one of horizontal biomass grain machine and scraping device, comprising has is equipped with short rod provided with at least one through gap of the same scraper on the scraper, scraper gear bottom end of scraper support device, and adjacent two scraper between the upper gear plate by the scraper rods provided with roller. This new utility model is horizontal machine, the upper scraper roller gear plate rolling over on scraper support device, so this can decrease friction force, scraping device of scraper machine operating at the set speed reducing electrical machine can make the scraping speed would not too fast, scraping compare uniform, so can reducing of production of aggregates, saving of resource, increase of production efficiency.
NOVELTY - This utility new type provide the one horizontal biomass granule machine of a scraper driving device, comprise one end with a chassis frame, a chassis frame of fixed mounting with a scraper transmission mechanism, a scraper transmission mechanism comprise a mounting with a decelerating electrical machine mounting on a speed reducing motor, a speed reducing electrical machine frame upper chassis frame one end, one side output end of a speed reducing motor through transmission shaft is connected with transmission mechanism base, transmission base mechanism set with a support pole, transmission mechanism base set with transmission mechanism, transmission mechanism through the rotating shaft set with scraper driving gear. This utility new type can ensure the rotating shaft more stable time turning, so it ensures stability, speed reducing motor of the scraper driving gear such that speed of scraping would not too fast, scraping compare uniform, so reduces the produce of particle, it saves the resource, increase the production efficiency.
NOVELTY - This utility new type provide the one horizontal biomass granule machine of a seal mechanism, include organic head disk, a discharging end of the head disk is connected with a discharge channel, a discharging end of the machine head is set with leaking openings disk, upper disk head through at least one a seal lock mounting shell, top of the shell end through seal ring mounting with machine cover, the shell and the machine cover through at least one between a seal lock seal mounting, machine cover top end set with feeding port. This utility new type the product is a horizontal machine, the seal effect is better, so it can ensure the temperature of inner shell held by a product of the production time, so increase the production efficiency and residual material to prevent leakage, which can ensure the production environment of workshop inner compare clean, at the same time, it can save resource.
NOVELTY - This utility model new supply of one of horizontal biomass granulator spiral dust-removing device, comprising a discharging end of organism and spiral dust-removing tank, a machine body provided with a discharging pipe, the discharging pipe is connected with a dust-removing pipe, upper machine body equipped with shell, upper shell set with heat abstractor hole, heat abstractor of hole is connected with the air outlet pipe, one outlet end of pipeline and dust-removing pipeline at, one end dust removing pipe is connected with the recycling pipe, recycling pipe one end is connected with a discharge pipe in spiral dust tank top end of spiral dust-removing tank top end. This new utility model this would at once will not forming grain and dust recycling utilize again, at the same time the heat air for discharging in a machine body, holding of a constant temperature inside the machine body, so can can ensure continuous generation of product, can at the same time would increase quality of fuel particle, the combustion performance of fuel, increase complete combustion rate of fuel, which avoids to cause a certain and pollute environment.
NOVELTY - This utility model new supply of one of horizontal biomass grain machine and for oil device, comprising organic head plate, the discharging end of the head plate is connected with the discharge passage, a discharge end head plate to set with the leaking openings, by at least one of sealing lock installed with shell head plate of the top end shell via seal ring installed with machine cover, cover of engine equipped with feedstock wherein, on machine cover set with oil port, oil port of oil provided with cover. This new utility model the product as horizontal machine, machine cover of the oil port can be to oil of machine, ensures normal running of machine, machine equipped with the upper oil port can make machine several days to one time of pressing oil is, so when so can switch machine to carry out machine is reasonable, prolong the using life of the machine, at the same time when save more labour force when in use.
NOVELTY - This utility new type relates to a one mould, especially claims a biomass granule one mould. It comprise comprise mould main body and a feeding hole, a feeding hole with several a, a feeding hole by a straight until the original property change is a three-level step, the feeding hole by a conical hole in turn the three and one of a straight hole are a, the height of which is not one. This utility new type yield, reduce the production cost, increase the single-time yield, reduces the feeding resistance, reduces the driving force energy consumption, enhance the wear resistance of mould and prolong the use life of mould, at the same time through three step, a density is gradually increased, and fast light of low biomass molding process in the density is gradually increased, the improved rear mould of the original density is increased by 0.2 percentage points, a same raw material heat value is increased by 200 to 300 a large card.
NOVELTY - Tea fertilizer comprises 35-45 wt.% lees, 8-12 wt.% rapeseed oil cake, 18-25 wt.% quail manure, 8-12 wt.% chicken manure, 12-15 wt.% urea, 4-6 wt.% phosphate rock and 1-3 wt.% biological bacterial strain. The preparation comprises e.g. mixing comprises lees, rapeseed oil cake, quail manure, chicken manure and biological bacteria, and stirring by adding biological bacterial strain to mix, and maintaining the moisture content at 50-55%, and stacking to ferment for 10 days, and fermenting by transferring the materials into a fermentation tower; and (ii) carrying out aerobic fermentation.    USE - Used as tea fertilizer.    ADVANTAGE - The fertilizer can not only can increase the percentage weight of bud, but also can simultaneously provide disease resistance to tea plants; and increases the tea yield by 20%.    DETAILED DESCRIPTION - Tea fertilizer comprises 35-45 wt.% lees, 8-12 wt.% rapeseed oil cake, 18-25 wt.% quail manure, 8-12 wt.% chicken manure, 12-15 wt.% urea, 4-6 wt.% phosphate rock and 1-3 wt.% biological bacterial strain. The preparation comprises (i) mixing comprises lees, rapeseed oil cake, quail manure, chicken manure and biological bacteria, and uniformly stirring by adding biological bacterial strain to mix, and maintaining the moisture content at 50-55%, and stacking to ferment for 10 days, and fermenting by transferring the materials into a fermentation tower for 12 days; (ii) carrying out aerobic fermentation by turning plate, mixing lees after carrying out fermentation process, and adding rapeseed oil cake, quail manure, fermented chicken manure, phosphate rock having moisture content of 25%; and (iii) discharging the materials into the fermentation tower once the materials becomes odorless, uniformly mixing by adding urea, crushing, sieving, checking, and finally granulating or powdering to obtain the finished product.
NOVELTY - High performance alcohol based fuel comprises 60-80 pts. wt. methanol, 10-30 pts. wt. plant pine oil, 5-10 pts. wt. water, 1-3 pts. wt. ethanol, 0.3-0.6 pts. wt. toluene, 0.1-0.5 pts. wt. acetone, and 0.1-0.4 pts. wt. colorant.    USE - High performance alcohol based fuel.    ADVANTAGE - The alcohol based fuel can be prepared from renewable raw materials with reduced time consumption, hence is inexpensive. The fuel produce less harmful substance on combustion, hence cause reduced environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the alcohol based fuel comprising uniformly mixing ethanol, toluene and methylene blue to obtain solution I, uniformly mixing acetone and methanol to obtain solution II, uniformly mixing solution I and solution II to obtain solution III, adding water and colorant to the solution III, uniformly mixing, adding plant pine oil to the mixture, uniformly mixing, and standing.
NOVELTY - The ecological toilet (10) has an energy collection portion set in toilet main portion, for collecting solar energy and chemical energy in organic matter. An energy conversion unit is used to convert solar energy into electric energy. A microbial cell is connected to conversion unit for producing electric energy. A rainwater collecting unit is united to main portion. A regeneration unit is used for recycling urine. A micro-organism electrolytic cell unit is located in anaerobic baffle pool (15), to perform electrochemical degradation of excrement and urine into organic matter.    USE - Ecological toilet for degrading excrement and urine into organic matter.    ADVANTAGE - The green energy is used as electrical energy source, so as to provide environmentally-friendly toilet. The degradation of excrement and urine into organic matter is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ecological toilet. (Drawing includes non-English language text)    Ecological toilet (10)    Storage battery (12)    LED lamp (13)    Water pump (14)    Anaerobic baffle pool (15)
NOVELTY - Following this utility new type claims a farm one marsh gas generating device with sealed pressure water tank, comprising a shell, the lower end of said shell is set with a water inlet tube, the upper end of said shell is set with a discharge tube and the pneuma tube, and lower end of said air inlet tube nozzle is located at the inner of the shell, lower end of a discharge tube opening above the water surface, said upper shell is set with a water level meter, upper end and the pig marsh gas generating device of said air inlet tube of air outlet connected, upper end and with pneuma device of said discharge tube connected said inner shell is set with a pressure sensor, a pressure sensor and through a controller, said controller is connected with the alarm and upper position machine connect. A discharge tube mounting with a check valve to prevent the discharged gas flow to said shell body inner. This utility new type marsh gas can be a water filter, removing of impurity, purification gas in marsh gas, increase the combustion value, in addition, a discharge tube mounting with a check valve to prevent the gas, increase use of safety.
NOVELTY - Culture material comprises 10-20% sawdust, 35-40% corn core, 10-20% bagasse, 15-25% bran, 3-8% corn powder, 2-7% soybean meal, 1-5% calcium carbonate and 1-5% lime. Preparation of the culture material comprises (i) dry mixing sawdust, corn core, bagasse, bran, corn powder, soybean meal, calcium carbonate and lime, and stirring for 5 minutes to obtain dry mixed material, and (ii) pre-wet processing the dry mixed material, adding water, stirring for 15 minutes, and adjusting moisture content to 65 plus minus 1% and pH value to 7-9.    USE - The culture material is useful for culturing Pleurotus eryngii (claimed).    ADVANTAGE - The culture material has good color and nutritional value, reduces cost and increases yield. The method improves production speed.
NOVELTY - Preparing Camellia nutritive soil comprises e.g. selecting humus soil and sawdust as principal substance, and substrate comprising e.g. burnt clay ash, river sand and bone powder, mixing the substrate, fermenting, stirring one time, adding rice husk ash in fermented substrate, mixing uniformly, adjusting the pH value to 6.5-6.8, adding phosphate fertilizer and urea in obtained product, stirring uniformly, sterilizing, where the sterilizing method comprises uniformly placing product in 20-25 ml 40% formalin solution, sealing, airing, crushing, and sieving.    USE - The method is useful for preparing Camellia nutritive soil (claimed).    ADVANTAGE - The method is simple; and prepares nutritive soil rich in nitrogen, phosphorus, and potassium, having good water and air permeability suitable for the growth and development of tea.    DETAILED DESCRIPTION - Preparing Camellia nutritive soil comprises (i) mixing raw material: selecting humus soil and sawdust as principal substance, where the material comprise 40-45 pts. wt. humus soil, 30-35 pts. wt. sawdust, 10-15 pts. wt. burnt clay ash, 20-25 pts. wt. river sand, and 1-2 pts. wt. bone powder as substrate, (ii) mixing evenly the substrate, fermenting for 15-20 days at 50-60 degrees C, stirring one time for every 5-6 days, (iii) regulating pH value: adding little amount of 5-8 parts rice husk ash in fermented substrate, mixing uniformly, adjusting the pH value to 6.5-6.8, (iv) adding 0.5-1 parts phosphate fertilizer and 1-2 parts urea in step (iii) obtained product, stirring uniformly, (v) sterilizing the step (iv) obtained product, where the sterilizing method comprises uniformly placing product in 20-25 ml 40% formalin solution, sealing each 1 kg product for 2-3 days, after unsealing, airing for 15-20 days, and (vi) crushing the step (v) product, sieving according to a grain size of 2-3 cm to obtain the nutritive soil.
NOVELTY - Preparing biodiesel using 8-12 mass% of methanol and without catalyst at high voltage electric field by plasma technology, is claimed.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method safely prepares the biodiesel with high quality, good lubricating properties, improved reliability and reduced time consumption and pollution, and maintains good power control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the biodiesel prepared by the above method using an electrode.
NOVELTY - Reducing freezing point of biodiesel comprises mixing 5 mass% of citric acid, 5-10 mass% of sodium chloride solution and a mixture of hydrocarbon compound and 1 mass% of magnesium silicate into a reactor, pre-treating the mixture for 10 minutes and controlling rotational speed of the reactor to 300 revolutions per minute.    USE - The method is useful for reducing freezing point of biodiesel (claimed).    ADVANTAGE - The method rapidly reduces freezing point of biodiesel with improved heat stability, oxidation stability, storage stability, combustion properties and fluidity.
NOVELTY - Preparing glabridin beta -cyclodextrin inclusion compound comprises taking 1 pts. wt. glabridin, extracting glabridin from Glycyrrhiza glabra residue, drying the extract material, adding 1.5-5 pts. wt. beta -cyclodextrin into 10-70 pts. wt. water, performing heating reflux extraction for 4-12 hours and then filtering to obtain filtered liquid at room temperature, separating out the crystal, again filtering, and drying obtained product.    USE - The method is useful for preparing glabridin beta -cyclodextrin inclusion compound (claimed).    ADVANTAGE - The method is capable of economically and eco-friendly preparing glabridin beta -cyclodextrin compound with high inclusion rate and without using any organic solvent.
NOVELTY - Preparation of biomass tar heavy weight reduction hydrocarbon catalyst, involves: impregnating waste of carbon-based sorbent in magnesium bicarbonate solution for 2-6 hours at 40-60 degrees C, drying under nitrogen atmosphere, baking at 600-850 degrees C for 2-4 hours to obtain lightweight catalyst. The waste carbon-based sorbent is saturated absorbing hydrogen sulfide after the semi-coke as an adsorbent carrier, loaded with metal elements of carbon-based desulfurization sorbent metal element in its semi-coke adsorbent support in the form of a load of metal oxides and metal sulfides.    USE - For preparation of biomass tar heavy weight reduction hydrocarbon catalyst (claimed) useful for catalyzing biomass tar reforming reaction.    ADVANTAGE - In mixed atmosphere and a catalyst comprising hydrogen and water vapor, biomass tar heavies can be reformed to better light components. Deactivated catalyst after the catalytic reforming reaction without regeneration, can be directly used as a raw material for combustion or gasification.    DETAILED DESCRIPTION - Preparation of biomass tar heavy weight reduction hydrocarbon catalyst, involves: impregnating waste of carbon-based sorbent in magnesium bicarbonate solution for 2-6 hours at 40-60 degrees C, drying under nitrogen atmosphere, baking at 600-850 degrees C for 2-4 hours to obtain lightweight catalyst. The waste carbon-based sorbent is saturated absorbing hydrogen sulfide after the semi-coke as an adsorbent carrier, loaded with metal elements of carbon-based desulfurization sorbent metal element in its semi-coke adsorbent support in the form of a load of metal oxides and metal sulfides, where the metal sulfide is carbon-based desulfurization sorbent metal oxides with hydrogen sulfide after the reaction product.
NOVELTY - Production of tripotassium phosphate comprises taking urea phosphate and potassium hydroxide at molar ratio of 1:2.95-3.05, reacting at 40-80 degrees C, and stirring at 30 revolutions/minute for 30-60 minutes.    USE - Method for producing tripotassium phosphate (claimed).    ADVANTAGE - The method has low energy consumption requirement and easy to obtain raw materials, is simple and short, reduces production cost, and meets industrial potassium product standards.
NOVELTY - Heavy metal ions reducing involves taking bioactive livestock manure, and then stirring the obtained manure under constant conditions. Diethyldithiocarbamate solution is sprayed, where the pH value is 6-7. The obtained material is kept for 2-3 hours. The exchangeable manganese, copper, zinc and chromium (heavy metal ions) are reacted with diethyldithiocarbamate complex, and then passivated, where the passivation rate of manganese is 40%, and the passivation rate of copper, zinc and chromium is 60%.    USE - Method for reducing heavy metal ions (claimed) in livestock and poultry excrement.    ADVANTAGE - The method is eco-friendly, and has improved heavy metal passivation rate.
NOVELTY - Organic fertilizer comprises effective microorganism and a fermentation material, where the content of effective microorganism is 5-7 grams per cubic meter of fermentation product. The fermentation material is plant straw and animal feces, where the plant straw comprises crop straw, mushroom residue or their mixtures.    USE - Organic fertilizer used for fertilizing disease resistant crops.    ADVANTAGE - The organic fertilizer is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) crushing plant straw;    (B) adding effective microorganism to the crushed product;    (C) fermenting the obtained mixture;    (D) drying animal feces; and    (E) mixing the obtained material with fermented plant straw to obtain the desired product, where the ratio of plant straw and animal feces is 1:1.
NOVELTY - Organic fertilizer additive comprises (in wt.%): liquorice (4), rice bran (2), silkworm excrement (2), corn (2), oligosaccharide (1), dry yeast (1.5) and water (87.5).    USE - Fertilizer additive used for providing nutrition for crops and promoting microbe breeding.    ADVANTAGE - The fertilizer additive has improved fertilizer effect by increasing organic matter content in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer additive, which involves:    (A) heating rice bran, silkworm excrement, corn and liquorice with water at 100 degrees C for 6 hours;    (B) leaching the obtained material;    (C) filtering the obtained material;    (D) standing the obtained material for 20-30 minutes;    (E) putting dry yeast and oligosaccharide in the obtained material;    (F) fermenting the obtained mixture for 30 days; and    (G) filtering the fermented liquid to obtain the desired product.
NOVELTY - Culture material preparation involves utilizing kitchen waste material as non-organic component. The obtained material is crushed, and then centrifuged to remove water and oil, where the content of water is 55-75%. The content of water in kitchen waste material is controlled by dehydration, where non-organic component comprises rock and glass. The obtained kitchen waste material is inoculated using microbial inoculum. Carbon source is added to the obtained mixture, and then stacked for 5-7 days. The obtained culture material is dried at 60-80 degrees C in hot air to obtain desired product.    USE - Method for preparing culture material used for culturing edible fungus (claimed).    ADVANTAGE - The method enables to prepare the culture material that is eco-friendly and cost-effective.
NOVELTY - Fertilizer comprises 10-15 pts. wt. humic acid, 20-25 pts. wt. crop waste, 5-10 pts. wt. biological microbial inoculum, 10-15 pts. wt. algae, 10-15 pts. wt. filter mud, 5-15 pts. wt. synergistic agent, 5-10 pts. wt. nitrogen fertilizer, 5-10 pts. wt. phosphate fertilizer and 5-10 pts. wt. potash fertilizer.    USE - The fertilizer is useful for promoting growth of plant.    ADVANTAGE - The fertilizer increases fertility of soil and reduces agricultural pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising adding humic acid, crop waste and algae into a reaction kettle and then mixing, crushing the material, uniformly stirring to obtain powder mixture, adding biological microbial inoculum, filter mud and powder mixture into a reaction pool, stirring the mixture and then fermenting at normal pressure, low temperature of 45-55 degrees C for 3-5 days, raising the temperature of the fermented mixture to 44-55 degrees C and then cooling at 30-40 degrees C and adding synergistic agent, continuously stirring at room temperature, then finally adding nitrogen fertilizer, phosphorus fertilizer and potash fertilizer, drying the mixture, and granulating the dried mixture and then sieving and vacuum packaging with aluminum foil.
NOVELTY - Mushroom culture medium comprises (in pts.wt.): fermented organic matter (80-100), wooden meal (150-200), plant ash (10-20), and calcium, phosphorus and magnesium mineral fertilizer (3-6).    USE - Mushroom culture medium used for promoting the fast growth of mushroom.    ADVANTAGE - The mushroom culture medium is cost-effective and eco-friendly.
NOVELTY - Garlic special organic microbial fertilizer comprises 45.62 pts. wt. furfural residue, 8.36 pts. wt. fungal bran, 2.68 pts. wt. complex microbial agent, 7.23 pts. wt. ammonium bicarbonate, 6.44 pts. wt. calcium superphosphate, 16.28 pts. wt. potassium chloride, 0.78 pts. wt. zinc sulfate, 14.27 pts. wt. plant ash, 11.48 pts. wt. potassium sulfate, 12.68 pts. wt. livestock manure, 3.45 pts. wt. potassium humate, 5.89 pts. wt. rice hull powder, and 6.28 pts. wt. rape seed cake, where the rice hull powder is obtained by smashing rice hull to 20-40 meshes to obtain powder.    USE - Used as garlic special organic microbial fertilizer.    ADVANTAGE - The fertilizer contains large amount of nutrition component, microelement and amino acid needed for the growth, is efficient and durable, improves soil, soil fertility, and disease resistance effect, assures better absorption of nutritional component, can continuously repair soil micro-ecological environment, and can increase garlic yield by 20-30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing garlic special organic microbial fertilizer comprising preparing fungal fertilizer by mixing uniformly furfural residue, fungal bran, ammonium bicarbonate, calcium superphosphate, potassium chloride, zinc sulfate, plant ash, potassium sulfate, livestock manure, potassium humate, rice hull powder, rape seed cake, and radix sophorae flavescentis slag according to the weight ratio, adding 80 pts. wt. water uniformly to obtain basal fertilizer solution, then mixing with the complex microbial agent uniformly, where the weight parts of complex microbial agent is 2.68, stacking the mixed fertilizer at 37 degrees C at room temperature and fermenting for 2-3 days, each day reversing and turning for 1 time, then stacking for 3-4 days and fermenting at 45 degrees C to obtain the garlic special microbial organic fertilizer.
NOVELTY - Recovering method of anion exchange resin comprises using medium, anion exchange resin, and catalyst for thermal cracking to get pyrolysates.    USE - Method for recovering anion exchange resin used for preparing styrene, ethylbenzene, benzene, propane, and divinylbenzene (claimed).    ADVANTAGE - The method solves problems such as low recycling and decomposition efficiency, high usage of decomposition medium, and high cost, has no waste produced, and complies circulating and low carbon economy.
NOVELTY - A biomass pyrolysis carbonization device comprises feeding device, pyrolysis unit, charring apparatus; heater (21); and pyrolysis device and carbonization device (8), where the pyrolysis device comprises pyrolysis furnace (26), through pyrolysis tube (24) disposed within the pyrolysis screw conveyor; the pyrolysis tube is connected to the output device and charring; the carbonization apparatus includes housing and heat transfer tubes (9) disposed in the housing.    USE - As continuous agriculture and forestry biomass pyrolysis carbonization device.    ADVANTAGE - The device uses two independent, pyrolysis and carbonization controllable devices; quickly and efficiently implement biomass continuous, stable pyrolysis; significantly improves transportation efficiency; and utilizes the product distribution and product quality control with high energy efficiency.    DESCRIPTION OF DRAWING(S) - The figure shows biomass pyrolysis carbonization device.    Carbonization device (8)    Heat exchange tube (9)    Heater (21)    Combustion furnace (22)    Pyrolysis tube (24)    Pyrolysis furnace (26)
NOVELTY - A low-carbon M50 methanol-gasoline composition comprises 500 kg methanol, 440 kg No. 93 gasoline and 60 kg agent containing 5 kg formaldehyde-butyl acetate, 10 kg low-temperature-resistance isopropanol, 5 kg methanol/tert-butanol, 2 kg pH adjusting agent-ethanolamine, lubricant-refined castor oil, 0.5 kg antioxidant/antioxidant 101, 2 kg preservative/phenylalanyl triazole, 15 kg reconciling agent-petroleum ether and 20 kg compatibilizer-methyl tert-butyl ether.    USE - Low-carbon methanol-gasoline composition used as fuel for car (claimed).    ADVANTAGE - The low-carbon methanol-gasoline composition is environmentally-friendly, and has excellent anticorrosion property.
NOVELTY - Organics aerobic oxidation resources (OAR) processing device comprises a fermenting vehicle (1), an insulating chamber (2), a pedestal (10), a spraying system (3), a discharge system (4), an aeration system (9), a solar energy power generation system, control system and a filtered liquid tube (11), where the fermenting vehicle comprises a fermentation cabin and a turn stack, where the fermentation cabin body is welded by a frame and a box plate. Device comprises a plate, an aeration pedestal, a transmission gear, a rocker arm and a pushing handle, which comprises a heat insulating chamber.    USE - OAR processing device used for processing solid waste of organic matter.    ADVANTAGE - The OAR processing device is simple and convenient with simple structure, and decreases energy consumption with improved efficiency and energy-saving capacity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an organics aerobic oxidation resources processing device.    Fermenting vehicle (1)    Insulating chamber (2)    Spraying system (3)    Discharge system (4)    Aeration system (9)    Pedestal (10)    Filtered liquid tube (11)
NOVELTY - Tea plant fertilizer additive comprises a covering layer and the fertilizer granule, where the fertilizer granule includes 3-5 pts. wt. copper sulfate, 3-5 pts. wt. ferrous sulfate, 3-5 pts. wt. zinc sulfate, 3-5 pts. wt. manganese sulfate, 10-15 pts. wt. compost fermentation silkworm excrement, and 10-15 pts. wt. molasses alcohol fermentation liquid; the covering layer is slow release carrier, including stearic acid, adhesive and mineral powder.    USE - Used as tea plant fertilizer additive.    ADVANTAGE - The additive reduces loss rate of fertilizer, increases utilization rate of fertilizer, and uses slow release carrier which does not cause white pollution.
NOVELTY - Ecological fertilizer comprises 6-50 pts. wt. organic fertilizer, mineral salt comprising 6.5-65 pts. wt. crude salt and 3.5-35 pts. wt. lime powder, and Chinese herbal medicine comprising 2-25 pts. wt. belladonna, 2-15 pts. wt. poinsettia, 2-25 pts. wt. Alocasia, 2-15 pts. wt. Rohdea, 2-25 pts. wt. Datura flower, 2-20 pts. wt. hot pepper, and 2-25 pts. wt. garlic. The organic fertilizer comprises animal excrement, plant root, plant stem, plant leaf, plant ash, kitchen waste and/or aged grain.    USE - Used as ecological fertilizer.    ADVANTAGE - The fertilizer is safe and environmentally friendly, has no toxicity and side effects, and does not harm human health. The method is simple and utilizes raw materials which are widely distributed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the ecological fertilizer, comprising (i) crushing components of the Chinese herbal medicine, mixing with organic fertilizer, crude salt and lime powder, and stirring, (ii) pouring the raw material mixture into a fermentation tank, sprinkling water accounting for 65-75% of total mass of raw material mixture, sealing and composting for 50-60 days, (iii) taking out and drying, and (iv) preparing the dry material into liquid, paste or granular form; and    (2) use method of ecological fertilizer as foliar fertilizer, comprising diluting 1 kg of fertilizer with 300-400 kg of water and spraying directly on crop foliage.
NOVELTY - Carbon monoxide and potassium hydroxide are reacted, desulfurized, compressed, potassium hydroxide solution is introduced into the reactor, and reacted to obtain potassium formate. Solid yellow phosphorus extracted from phosphorus rock is added to a melting tank, heated, obtained liquid phosphorus is injected into combustion atomization tower using compressed air, and phosphorus pentoxide is generated. Potassium formate and phosphorus pentoxide are reacted, to obtain potassium dihydrogen phosphate and formic acid solution.    USE - Production of formic acid and potassium dihydrogen phosphate (claimed).    ADVANTAGE - The method enables economical production of formic acid and potassium dihydrogen phosphate, with reduced energy consumption by simple process.    DETAILED DESCRIPTION - Carbon monoxide and potassium hydroxide are reacted at 160-200 degrees C under pressure of 1.4-1.8 MPa, desulfurized, compressed, 20-30% potassium hydroxide solution is introduced into the reactor, and reacted to obtain potassium formate. The reaction is completed when carbon monoxide absorption is terminated. Solid yellow phosphorus extracted from phosphorus rock is added to a melting tank, heated under pressure of 0.2-0.5 MPa, obtained liquid phosphorus is injected into combustion atomization tower using compressed air, and phosphorus pentoxide is generated. Potassium formate and phosphorus pentoxide are reacted at room temperature to 80 degrees C under atmospheric pressure, obtained potassium dihydrogen phosphate and formic acid solution is added to a evaporator, heated to 130-260 degrees C under atmospheric pressure conditions to -0.085 MPa, concentrated by evaporation for 2 hours, and cooled to obtain potassium dihydrogen phosphate, and steam condensate containing more than 85% formic acid solution.
NOVELTY - Preparation of 2-chloro-1-(6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl)ethan-1-one (I) involves reacting 2-(dimethanesulfinylidene)-1-(6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl)ethan-1-one (II) and hydrogen chloride. Hydrogen chloride is obtained by reacting water and thionyl chloride.    USE - Preparation of 2-chloro-1-6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl-ethan-1-one used as intermediate product for preparing nebivolol.    ADVANTAGE - The method enables simple preparation of 2-chloro-1-6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl-ethan-1-one with a purity of 99% or more and a yield of more than 85%.    DETAILED DESCRIPTION - Preparation of 2-chloro-1-(6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl)ethan-1-one of formula (I) involves reacting 2-(dimethanesulfinylidene)-1-(6-fluoro-3,4-dihydro-2H-1-benzopyran-2-yl)ethan-1-one of formula (II) and hydrogen chloride. Hydrogen chloride is obtained by reacting water and thionyl chloride.
NOVELTY - Synthesizing pomalidomide, comprises (i) adding 3-nitro-phthalic acid and acetic anhydride into a reactor, and adding a solvent, reacting by heating, and re-crystallizing; (ii) adding 3-nitro-phthalic anhydride and L-glutamine, adding solvent and an alkali, and reacting by heating, adding acetic anhydride, heating, cooling, and filtering, to obtain N-(2,6-dioxo-3-piperidyl)-3-nitrophthalimide; and (iii) adding N-(2,6-dioxo-3-piperidyl)-3-nitrophthalimide, adding solvent and metal catalyst, introducing hydrogen gas, heating during reaction, and evaporating the filtered liquid.    USE - The method is useful for synthesizing pomalidomide (claimed).    ADVANTAGE - The method has simple operation, high production yield, and desired pressure and temperature which are in normal range; produces product with high purity; does not require harsh reaction conditions e.g. vacuum conditions; utilizes reagents having slight toxicity and causes less pollution; and is economical.    DETAILED DESCRIPTION - Synthesizing pomalidomide, comprises (i) adding 3-nitro-phthalic acid and acetic anhydride into a reactor, and adding a solvent, reacting by heating, cooling once the reaction is complete, evaporating the solvent, drying the resulting solid, and re-crystallizing to obtain 3-nitro phthalic anhydride; (ii) adding 3-nitro-phthalic anhydride and L-glutamine into the reactor, adding solvent and an alkali, and reacting by heating, cooling once the reaction is complete, adding acetic anhydride in dropwise manner, continuously heating after dropwise addition, and cooling, and filtering, to obtain resulting solid of N-(2,6-dioxo-3-piperidyl)-3-nitrophthalimide; and (iii) adding N-(2,6-dioxo-3-piperidyl)-3-nitrophthalimide into the reactor, adding solvent and metal catalyst, introducing hydrogen gas, controlling pressure, heating during reaction, filtering, and evaporating the filtered liquid to obtain the product.
NOVELTY - Preparing indiplon involves preparing 2-acetyl-thiophene as a starting material, using basic quaternary ammonium catalyst, N,N-dimethylformamide dimethyl acetal (DMFDMA) condensation reaction, cyclization reaction by amino guanidine nitrate with hydroxylamine salt, and adding N-(3-(3-(dimethylamino)-1-oxy-2-propenyl-phenyl)-N-methyl acetamide.    USE - The method is useful for preparing indiplon (claimed) used for treating insomnia.    ADVANTAGE - The method has simple process operation, good technical performance, and no environmental pollution.    DETAILED DESCRIPTION - Preparing indiplon involves preparing 2-acetyl-thiophene of formula II as a starting material, using basic quaternary ammonium catalyst, N,N-dimethylformamide dimethyl acetal (DMFDMA) condensation reaction, cyclization reaction by amino guanidine nitrate with hydroxylamine salt, and adding N-(3-(3-(dimethylamino)-1-oxy-2-propenyl-phenyl)-N-methyl acetamide of formula (I).    R=1-10C of N, N-dimethyl substituted alkyl.
NOVELTY - Separation of camptothecin involves testing quality of Camptotheca acuminata extract, calculating number of mole of camptothecin in the extract, mixing the extract with ethanol, stirring, adding resultant suspension and long-chain guanidine compound (I) in foam separation column, stirring, blowing air from bottom of the column, forming bubbles, collecting foam until no foam is generated, discharging foam from the top of the column, centrifuging resultant foam, adding obtained camptothecin precipitate to an aqueous solution of inorganic acid, stirring, filtering, and drying.    USE - Separation of camptothecin (claimed).    ADVANTAGE - The method enables economical separation of camptothecin with reduced energy consumption, by stable, environmentally-friendly and simple process.    DETAILED DESCRIPTION - Separation of camptothecin involves testing quality of Camptotheca acuminata extract, calculating number of mole of camptothecin in the extract, mixing the extract with ethanol, stirring, adding resultant suspension and long-chain guanidine compound of formula (I) in foam separation column, stirring, blowing air from bottom of the column, forming bubbles, collecting foam until no foam is generated, discharging foam from the top of the column, centrifuging resultant foam, adding obtained camptothecin precipitate to an aqueous solution of inorganic acid, stirring, filtering, and drying filter cake. The amount of air blown into column is 300-600 mL/(minute.L) with respect to total volume of liquid raw material. The usage amount of ethanol is 2-3 mL/g with respect to Camptotheca acuminata extract. The molar ratio of long-chain guanidine compound and camptothecin is 1-3:1.    R1,R2=H or 10-18C alkyl.    R1 and R2 are not H simultaneously.
NOVELTY - Preparing entecavir intermediate involves: (a) reacting organic solvent, entecavir intermediate, and (1R,2R)-2-amino-1-(4-nitrophenyl) propane-1,3-diol; and (b) subjecting to esterification reaction under the action of concentrated sulfuric acid.    USE - The method is useful for preparing entecavir intermediate (claimed) used for preparing anti-AIDS and anti-hepatitis B drugs.    ADVANTAGE - The method uses cheap and easy to obtain raw material. It provides mild reaction condition, less side reaction, high yield, small environmental pollution, and easy purification and separation, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing entecavir intermediate of formula X involves: (a) reacting organic solvent, entecavir intermediate of formula XI, and (1R,2R)-2-amino-1-(4-nitrophenyl) propane-1,3-diol; and (b) subjecting to esterification reaction with Ra'OH under the action of concentrated sulfuric acid.    Ra'=1-4C straight chain alkyl group;    R2=a substituted group of formula 1;    R21=a substituted or unsubstituted pyridyl group, or a substituted or unsubstituted 6-10C aryl group, said substituted pyridyl group is substituted with 1-3C alkyl, halogen, or 1-3C alkoxy group; and    Y'=connected or not to other substituents or carbon, or Y' is connected or not to other substituents, and to Si to form a substituted or unsubstituted 4 to 10-membered saturated or unsaturated carbocyclic ring of silicon atoms and hetero atoms, or to form a substituted or unsubstituted 4 to 10-membered saturated or unsaturated heterocyclic ring of carbon.    An INDEPENDENT CLAIM is included for entecavir intermediates of formula XI or formula XII..
NOVELTY - Preparation of heterocyclic intermediate compound (I) or (II) involves removing amino-protecting group and hydroxy-protecting group of pyrimidine-containing compound (III) in solvent in presence of protonic acid.    USE - Preparation of heterocyclic intermediate compound used for preparing entecavir.    ADVANTAGE - The method enables preparation of heterocyclic intermediate compound with high yield by economical and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of heterocyclic intermediate compound of formula (I) or (II) involves removing amino-protecting group and hydroxy-protecting group of pyrimidine-containing compound of formula (III) in solvent in presence of protonic acid.    Ra=1-4C alkyl;    Rb=H, benzyl, methoxy, methyl or halo;    Rc=methyl;    R2=group of formula (i);    R21=pyridyl optionally substituted with 1-3C alkyl, halo or 1-3C alkoxy, or 6-10C aryl optionally substituted with 1-3C alkyl, halo or 1-3C alkoxy;and    Y'=optionally substituted saturated or unsaturated 4-10-membered carbocyclyl or optionally substituted saturated or unsaturated 4-10-membered heterocyclyl, in which the heteroatom is chosen from O, S and N.    An INDEPENDENT CLAIM is included for heterocyclic intermediate compound (I) and (II) and tautomer pyrimidine-containing compound (III) or cyclopentanone-containing compound of formula (IV).
NOVELTY - Continuous agricultural and forestry biomass pyrolytic carbonization involves a continuous process of biomass preliminary pyrolysis, and then using a fixed-bed carbonization process on the initial pyrolysis products, specifically involves: (a) conveying biomass feedstock by feeding unit to dryer; (b) drying biomass raw material; (c) collect biomass charcoal; (d) discharging pyrolysis volatiles and semi-coke volatiles, and cooling; and (e) collecting tar and wood vinegar; and (f) performing pyrolysis and combustion in a combustion device input.    USE - The method is useful for continuous agricultural and forestry biomass pyrolytic carbonization (claimed).    ADVANTAGE - The method has stable pyrolytic carbonization and has high energy efficiency. The pyrolysis step and carbonization step are finished in the same system. The conveying efficiency is significant increased. The reaction condition is controllable.    DETAILED DESCRIPTION - Continuous agricultural and forestry biomass pyrolytic carbonization involves a continuous process of biomass preliminary pyrolysis, and then using a fixed-bed carbonization process on the initial pyrolysis products, specifically involves: (a) conveying biomass feedstock by feeding unit to dryer; (b) drying biomass raw material; (c) collect biomass charcoal; (d) discharging pyrolysis volatiles and semi-coke volatiles, and cooling; (e) collecting tar and wood vinegar; (f) performing pyrolysis and combustion in a combustion device input to obtain a high temperature flue gas; and (f) placing high-temperature flue gas in dispensing valve unit and carbonization pyrolysis unit and heat carbonization apparatus, and then the flue gas is delivered to the dryer.
NOVELTY - The system has a circulation fluidized bed reactor i.e. uplink type fluidized bed reactor whose lower part is provided with a raw material inlet and top part is connected with a cyclone separator. The cyclone separator is connected with a lower part of an air burner that is fixed with an air inlet i.e. split-type burner. The cyclone separator is fixed with a condenser i.e. heat exchanger, which is divided into three branches, where the three branches are the connected with the circulation fluidized bed reactor, the air burner and a subsequent unit, respectively.    USE - Circulation-type fluidized bed biomass catalytic pyrolysis system.    ADVANTAGE - The system achieves low energy consumption by using a gas phase product and a solid-phase product under biomass oil function and better circulation oil efficiency using the circulation fluidized bed reactor through a liquid phase part of the condenser, and ensures high utilization rate and better biological oil yielding efficiency.    DETAILED DESCRIPTION - The cyclone separator is provided in a vertical-type cylinder structure. An INDEPENDENT CLAIM is also included for a circulation-type fluidized bed biomass catalytic pyrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a circulation-type fluidized bed biomass catalytic pyrolysis system.
NOVELTY - The system has a finished product tower (5) fixed with a light liquid layer evaporator. A side of the light liquid layer evaporator is connected with a condenser (2-1), a middle tank and a first discharging pump (6-1). A bottom part of the finished product tower is fixed with a second discharge pump (6-3). A sucker is provided with a liquid collecting disk, a heating pallet and a heating coil pipe. A center part of the liquid collecting disk is fixed with a drainage tube. A filling material of the finished product tower is fixed with an annular liquid collector (8).    USE - Light liquid layer evaporator based biological fuel continuous rectification system.    ADVANTAGE - The system ensures high target biological fuel product quality, reduces thickness of heating pallet liquid layer and temperature of heating medium, increases distillation yield and heating vaporization amount so as to reduce residence time, and reduces energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a light liquid layer evaporator based biological fuel continuous rectification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a light liquid layer evaporator based biological fuel continuous rectification system.'(Drawing includes non-English language text)'    Condenser (2-1)    Finished product tower (5)    Discharging pumps (6-1, 6-3)    Annular liquid collector (8)    Light tower vapor phase inlet (10)
NOVELTY - A methanol-based diesel oil comprises 70-85 pts. wt. methanol and 10-25 diesel oil composition comprising 3-5 pts. wt. combustion accelerating agent and 5-10 pts. wt. additive chosen from ignition agent, cleaning agent, surfactant, co-surfactant, fatty alcohols, corrosion inhibitor and lubricant.    USE - Methanol-based diesel oil is used in vehicle.    ADVANTAGE - The methanol-based diesel oil has high combustion efficiency and reduces carbon deposit.
NOVELTY - Biomass glyceryl blended fuel is researched by adding mesoporous solid acid catalyst and dehydrating agent to biomass glyceryl system containing glycerol and tert.-butanol, heating, stirring, refluxing to obtain blended fuel, directly researching, and researching density, low heat value, flash point, cetane number, color, and other physical and chemical properties of blended fuel at different proportions of gasoline, ethanol, and biomass glyceryl.    USE - Research of biomass glyceryl blended fuel (claimed).
NOVELTY - Biogas is produced by adding inoculum to pure pig manure raw material, starting reaction, placing pig manure:Camellia oleifera shell with dry weight ratio of 1-4:1 in fermenter, mixing, soaking and fermenting, crushing C. oleifera shell, sieving through 40 mesh sieve, and fermenting while constantly stirring under anaerobic conditions at 50 degrees C with pH of 6-8 and material hydraulic retention tie of 15 days in which fermenter is controllable constant-temperature anaerobic stainless steel fermentation tank containing tank body (1), tank top (2), and feed inlet (3).    USE - Production of biogas (claimed).    ADVANTAGE - Production of biogas has accelerated reaction rate, short reaction cycle, and improved hydrogen yield, raw material utilization ratio, and energy conversion efficiency.    DETAILED DESCRIPTION - Biogas is produced by adding inoculum to pure pig manure raw material, starting reaction, placing pig manure:Camellia oleifera shell with dry weight ratio of 1-4:1 in fermenter, mixing, soaking and fermenting, crushing C. oleifera shell, sieving through 40 mesh sieve, and fermenting while constantly stirring under anaerobic conditions at 50 degrees C with pH of 6-8 and material hydraulic retention tie of 15 days in which fermenter is controllable constant-temperature anaerobic stainless steel fermentation tank containing tank body (1), tank top (2), feed inlet (3), gas outlet (4), motor (5), screw sealing port (6), water outlet (7), liquid seal tube (8), drain outlet (9), heating rod (10), and fence (11), and gas outlet is connected to gas flowmeter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fermenter.    Tank body (1)    Tank top (2)    Feed inlet (3)    Gas outlet (4)    Motor (5)    Screw sealing port (6)    Water outlet (7)    Liquid seal tube (8)    Drain outlet (9)    Heating rod (10)    Fence (11)
NOVELTY - Sludge is discharged from sewage treatment plant, dehydrated using filter press, moisture content of sludge is adjusted to 40-60%, magnetic separation is carried out to remove scrap metal, plant sludge is separated and scrap metal is removed. Waste fabric from garment factory is crushed to particle diameter of less than 10 mm, sorting and magnetic separation of obtained mixture is carried out, and scrap metal is removed. Leather waste is subjected to sorting process, magnetic separation is carried out, and scrap metal and other impurities are removed to obtain regenerated coal.    USE - Manufacture of regenerated coal (claimed).    ADVANTAGE - The method provides regenerated coal by economical and environmentally-friendly process.    DETAILED DESCRIPTION - Sludge is discharged from sewage treatment plant, dehydrated using filter press, moisture content of sludge is adjusted to 40-60%, magnetic separation is carried out to remove scrap metal, plant sludge is separated and scrap metal is removed. Waste fabric from garment factory is crushed to particle diameter of less than 10 mm, sorting and magnetic separation of obtained mixture is carried out, and scrap metal is removed. Leather waste is subjected to sorting process, magnetic separation is carried out, scrap metal and other impurities are removed and crushed to particles having particle diameter of less than 10 mm to obtain regenerated coal. The coal is regenerated from 35-60 Pts. wt. sewage-treated plant sludge having moisture content of 40-60%, 15-40 pts. wt. waste plant powder, 15-35 pts. wt. waste fabric powder, 5-10 pts. wt. waste plastic powder, 5-10 pts. wt. leather waste powder, 8-17 pts. wt. calcium oxide, 2-6 pts. wt. calcium sulfate, 0.5-1 pt. wt. ferrous sulfate, 4-11 pts. wt. magnesium sulfate, 1.3-5 pts. wt. waste oil and 3-10 pts. wt. water.
NOVELTY - Petroleum hydrocarbon degrading Corynebacterium glutamicum strain (I) having a preservation number of CGMCC 8647, is new.    USE - (I) is useful as sludge purifying agent for degrading petroleum hydrocarbon in oily sludge (claimed).    ADVANTAGE - (I) degrades the rate: of saturated hydrocarbon to 20.74%; and petroleum hydrocarbon to 39.69%.
NOVELTY - Two-step enzymatic method for increasing production of ethanol by fermentation of food waste, comprises: (a) preliminary sorting kitchen garbage, adding 0.5-1 weight proportion of water, crushing into a slurry; (b) adding 0.001-0.003 weight proportion of acid protease and 0.002-0.005 weight proportion of pectinase to the slurry, heat-preserving at 45-55 degrees C for 1-1.5 hours, then cooling to 28-35 degrees C; and (c) adding 0.002-0.004 weight proportion of glucoamylase, and using Saccharomyces cerevisiae for alcoholic fermentation process.    USE - The two-step enzymatic method is useful for increasing production of ethanol by fermentation of food waste (claimed).    ADVANTAGE - The method can increase nutrient utilization rate, can reduce mash viscosity, can shorten fermentation period of 4-6 hours, and increase ethanol yield by 1-4%.
NOVELTY - Method for enzymatic preparation of rosuvastatin intermediate involves (a) reacting chiral amine (A) and lipase with hydroxy group containing compound (I) as substrate in presence of organic solvent, and (b) adding chitosan or chitosan complex and reacting to obtain rosuvastatin chiral intermediate (II).    USE - The method is useful for enzymatic preparation of rosuvastatin intermediate (claimed).    ADVANTAGE - The method is simple, cost-effective, convenient to perform and suitable for industrial production, and enables to produce nontoxic enzyme byproducts in high quantity.    DETAILED DESCRIPTION - Method for enzymatic preparation of rosuvastatin intermediate involves (a) reacting chiral amine of formula (A) and lipase with hydroxy group containing compound of formula (I) as substrate in presence of organic solvent, and (b) adding chitosan or chitosan complex and reacting to obtain rosuvastatin chiral intermediate of formula (II).    R1=1-4C linear or branched alkyl, methyl or ethyl.
NOVELTY - Method for producing natamycin using Crypthecodinium cohnii (ATCC 30772) and bacterial fermented waste residue, involves (a) culturing C.cohnii for 200-240 hours, centrifuging culture liquid, obtaining cell sediment, washing cell sediment for 3 times with distilled water, drying cell sediment in an oven at 80 degrees C and crushing dried sediment into powder, and (b) obtaining fermented waste residue after 0-72 hours fermentation by Streptomyces natalensis, adding C.cohnii powder to the waste residue and fermenting mixture.    USE - The method is useful for producing natamycin using C.cohnii (claimed).    ADVANTAGE - The method produces natamycin with high yield and is simple, cost-effective, energy-saving and environmentally-friendly.
NOVELTY - A bamboo charcoal is prepared by carbonizing bamboo, crushing bamboo carbide into less than or equal to 1 mm particle of bamboo carbon powder, adding 1.5-4.5 pts. wt. plant starch, 1.5-3 pts. wt. polyvinyl acetate, and 0.1-0.5 pt. wt. preservative into container, stirring 2-5 parts of boiling water, diluting with water, uniformly stirring for 20-40 minutes to obtain dextrin powder, uniformly stirring 60-80 pts. wt. bamboo carbon powder and 1.5-4.5 pts. wt. dextrin powder in stirring mill, extruding, cutting, drying, molding bamboo charcoal into container with ethanol and standing, and removing sealed packing.    USE - Preparation of bamboo charcoal (claimed).    ADVANTAGE - Product is easy to ignite, environment-friendly, and low-cost, has long heat preservation and no pollution and pungent smell, and increases combustion.    DETAILED DESCRIPTION - A bamboo charcoal is prepared by carbonizing bamboo, crushing bamboo carbide into less than or equal to 1 mm particle of bamboo carbon powder, adding 1.5-4.5 pts. wt. plant starch, 1.5-3 pts. wt. polyvinyl acetate, and 0.1-0.5 pt. wt. preservative into container, stirring 2-5 parts of boiling water which has temperature of 85-100 degrees C, diluting with 2-5 parts water, uniformly stirring for 20-40 minutes to obtain dextrin powder, uniformly stirring 60-80 pts. wt. bamboo carbon powder and 1.5-4.5 pts. wt. dextrin powder in stirring mill, extruding mixture into block, sphere, or hollow rod by extruder at pressure of 2-4 ton/m2, cutting, drying to remove water, molding bamboo charcoal into container with ethanol and standing for 2-24 hours, and removing sealed packing in which mass ratio of ethanol and molded bamboo carbon is 3:7 and water temperature is room temperature.
NOVELTY - Biodiesel production involves selecting and drying fragrant tree seeds at 30-80 degrees C, crushing dried fragrant tree seeds, and then extracting crushed material for 10-60 minutes to obtain extract. The extract is treated with methanol at 10-60 degrees C 1-10 times (each time60 minutes). The obtained product is mixed with glycerol to obtain the desired product.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables producing biodiesel in an eco-friendly manner.
NOVELTY - Culture medium for recovering viable but nonculturable (VBNC) ODSLC13 Arthrobacter strain having preservation of CCTCC No M2014074, comprises 1-3 g nutrition meat soup culture medium, 0.2-0.5 g yeast extract, 1.5-5 g glucose, 0.5-5 g sodium chloride, 1-4% agar, 0.2-20% activating promoting factor (rpf), and 1000 ml deionized water.    USE - For recovering viable but nonculturable ODSLC13 Arthrobacter strain for denitrifying nitrate-containing matrix (claimed).    ADVANTAGE - The viable but nonculturable ODSLC13 Arthrobacter strain converts 63.7% nitrate into nitrogen; and has 57.9% nitrogen reduction rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of culture medium involving mixing 1-3 g nutrition meat soup culture medium, 0.2-0.5 g yeast extract, 1.5-5 g glucose, 0.5-5 g sodium chloride, 0.2-20% activating promoting factor (Rpf), and 1000 ml deionized water; adjusting pH to 7, adding 1-4% agar, high pressure sterilizing at 110-130 degrees C for 10-30 minutes, then cooling to room temperature, adding 2-20 vol./vol. Arthrobacter at pH of 7, stirring, mixing, and preserving.
NOVELTY - Facultative anaerobic fermentation of kitchen waste for producing volatile fatty acids comprises crushing kitchen waste to have a particle size of less than 3 mm; adding bacteria where volume ratio of bacteria and kitchen waste is 1:1.5-2; regulating kitchen waste moisture content to 88-91%; mixing uniformly; and performing facultative anaerobic fermentation at 34-37 degrees C.    USE - The method is useful for facultative anaerobic fermentation of kitchen waste for producing volatile fatty acids (claimed).    ADVANTAGE - The method provides short time for hydrolysis, and high hydrolysis rate. It provides high yield of volatile fatty acids. It can perform efficient resource utilization.
NOVELTY - One of magnesium ore slag filler bed phosphorus recycling system, comprising water inlet area and water inlet area and connected with the reactor, the reactor is inner and outer double barrel structure, inner barrel top opening, comprising position in crystal reaction reactor inner cylinder and the set capture area, and crystal separation zone below the inner cylinder, a crystal zone and the area upper part of outside cylinder, the crystallization reaction and capture zone collected, separating crystal and crystal deposition area arranged from up to down, a water inlet zone and the crystallization reaction and capture zone collected by can disassemble pipe. crystallization reaction and bottom in capture district set filling magnesium ore slag grain forming magnesium ore slag grain filler layer, magnesium ore slag filler layer set with screen and oscillating base. The utility model is not need to add new chemistry medicament, recovery cost low, of magnesium ammonium phosphate crystallization recovery for phosphorus containing magnesium dependent and medicine preparation, would not cause second time pollute and chemistry product solid waste, magnesium ammonium phosphate and phosphorus adsorption saturated magnesium ore slag grain can is directly used as fertilizer enrichment, economic and high efficient of recycling phosphorus from sewage and.
NOVELTY - This utility new type claims a one farm sewage solid-liquid separate rear waste liquid comprehensive utilization system, comprising a marsh gas generating device, the air outlet is connected with water of a marsh gas generating device sealed pressure tank of air inlet tube connected, a water-sealed discharge tube with the pneuma bag of pressure tank connected, a pneuma collecting bag set on the storing tank in the gas collecting bag through a gas tube with pneuma and connecting device, said air tube mounting with a control valve and a pressure table. Said collecting pneuma inner bag set with a pressure sensor, a pressure sensor and through a controller, said controller is connected with the alarm and upper position machine connect. This utility new type water pressure tank set between the marsh gas generating device and collecting pneuma bag, the inner tank shell of water pressure, it can process the marsh gas water filter, removing impurity of the purification gas in marsh gas, increase combustion value.
NOVELTY - This new type utility claims one for a biomass gasification furnace of feeding device, comprise: a tubular mix room and the cone shape of a carrier pneuma, inner diameter of a carrier pneuma air inlet pipe top end is less than a carrier pneuma inlet tail end of inner diameter of the feeding port of mix room of the biomass gasification furnace is connected with mix room air inlet through a carrier with a carrier pneuma pneuma pipeline close to the mix room discharging port in a mix room set with catalyste entering into, mix room close to the air inlet set with biomass raw material entering into a port in the mix room, a carrier inlet end from the pneuma mix room air into mix chamber rear extending to biomass raw material entering into a port. This utility new type has simple structure and biomass raw material and catalyste mix uniformity and contact heat exchange, catalysis of catalyste efficiency high, gasification rear produce of combustion gas of a thermal value is high.
NOVELTY - This utility new type relates to biomass fuel gasification field, especially relates to a biomass fuel gasification production line one with pneuma storage cabinet, include pneuma storage cabinet main body, a pneuma storage cabinet main body and the fine filter cylinder through gas pipeline a, connecting said upper pneuma storage cabinet main body and a gas pipeline between a fine filter cylinder set on fire device, a fire device include pipeline and set with the fire burning head of said upper fire pipeline, connecting a pneuma storage cabinet main body and a gas pipeline between a fine filter cylinder upper connecting with an exhaust gas pipeline, a waste gas pipeline set with a first connected valve, a connecting a storage cabinet main body and pneuma of gas pipeline between a fine filter cylinder set with a second connected valve. Because the mass quality of gasification furnace generate gas and can not be always maintain the same set with the fire device, the storage cabinet inner pneuma pneuma of combustion quality.
NOVELTY - Separating hydrogen radicals through electric field-induced hydrolysis involves utilizing water, where electric field is induced by a reaction equipment. The induced electric field causes hydrolysis of water and produces hydrogen radicals and hydroxyl radicals in presence of transition metal ion catalyst. The hydroxyl radicals are converted into water and oxygen.    USE - Method for separating hydrogen radicals through electric field-induced hydrolysis (claimed).    ADVANTAGE - The method increases the production efficiency of hydrogen free radical.
NOVELTY - This utility new type relates to a sewage processing device one, specifically biological film-UASB a reactor a, reactor tube include, biological film electrode system, an electrochemical test system and a cathode potential device, reactor inner tube from lower to top in turn comprise distribution, biological film electrode system, biological film electrode system and the three phase separator is sludge bed area, biological film system comprise an anode, a cathode, a cathode potential device comprise a reference electrode, the electrolyte seal, near the cathode sludge bed area of the seal electrolyte connected, reference a one end and seal the electrolyte connecting the other end with the electrochemical test system connect. This utility new type provide a biological film-UASB a coupling reactor, through a function of the electric field, promoting microorganism for organic pollutant of oxidative metabolism, increase COD removal rate, at the same time, a promoting inner electric field system, a pollutant degradation rate increase.
NOVELTY - This utility new type provide a one of organic fertilizer preparation system, include: crop straw crushing mix tank and waste poultry feather storage pool, the a connecting to the first steam-exploded tank and second steam-exploded tank, a first tank for explosion of crushing the crop straw steam explosion treatment process, a second steam tank for the poultry feather process steam explosion treatment, a first steam-exploded tank and exit of second steam tank through a pipeline to mix stirrer; said mix further include entrance of one connecting active sludge storage tank, a mix stirring the said straw blasting material and a feather blasting material and aerobic active sludge mix, a mixture, exit of mix mixer through a pipeline in turn a fermenting tank, a drying tank and a rear device. This utility new type provide the a one of organic fertilizer preparation system, structure is simple, production efficiency is high, a;
NOVELTY - This utility new type relates to a one a collecting gas of aerobic compost reactor. Structure of the reactor is not enough. This utility new type reaction cylinder in the top through a flange cover sealing cover, upper flange cover connect with pneuma tube, flange cover head mounting a gas joint, cylinder of reaction cylinder bottom connecting with a water collecting tube and inner reaction cylinder is horizontal set with a porous water distribution network pneuma, side wall of air inlet buffering cavity is divided into a connecting tube with an air inlet, one air inlet end of the pneuma pump connecting tube, side wall of reaction cavity by upper to lower in turn with equal temperature sampling port, the upper layer temperature measuring sampling port in the lower temperature sampling port, lower reaction cavity part of side wall of the solid outlet. This utility new type not only can a valid organic solid waste in a parameter condition in stacking process to ensure the compost completely, a organic solid waste composting process, and capable of collecting compost each stage produce a gas, for deeply researching carbon, conversion mechanism and carbon fixation of nitrogen, nitrogen supply device measures.
NOVELTY - This utility new type relates to a one room two aerobic compost experiment device, comprise reaction device and gas treatment device, reaction device comprise a top cover and fermentation chamber, the fermentation chamber through divided into two room, set with shaped;, shaped; the fermentation chamber is divided into a compost reaction room and gas room wall set with sampling hole, inner set with temperature sensor, first fermenting chamber above a top cover set with a discharge hole, the second fermenting chamber above a top cover set with a spray head, clapboard set with malodorous gas gas-guide tube, gas distribution room is inclined, the inclined end port is set with leachate collecting port, and the collecting bucket is connected with collecting bucket and the pump is connected with the nozzle connecting pump, one side gas distribution room set with a gas inlet, an air inlet and a air blower, a gas treatment device is the three-dimensional cylindrical structure from up to the upper part of lower in turn set with absorbing layer and filling layer, gas treatment device set with an air outlet. This utility new type has two room structure, good effect, convenient for a teaching and scientific research.
NOVELTY - This new type utility claims one a biomass carbonization device, according to the folding mode in the vertical direction set up between each two conveyor through a connecting pipe, an electric heating device is covered on the outer surface of conveyor set with insulating layer outside of the conveyor and corrugated pipe, heat preservation layer the whole conveyor and corrugated pipe is completely covered, a gap between the heating device and the heat insulating layer is a heating space, temperature probe set with the inner corrugated pipe, set with inner conveyer connected with the cavity for oil gas conveying tube of a conveyor, a oil-gas transporting tube up a conveyor and each set of jet combustion mechanism on the heating inner space connect with cooling mechanism connected. This utility new type solves the problem that the current technology exist of oil gas pipeline blocking, and silicon carbide heating uniformity, temperature gradient over the problem of carbide mass difference is small or there is no gradient caused by a low energy consumption, no pollution, a application of all kinds of biomass.
NOVELTY - This utility new type relates to a one burning household garbage processing device, especially a pyrogenation gastification furnace for life garbage one furnace. The furnace body by outer inner comprise a furnace shell, refractory brick layer, furnace inner liner, furnace bottom slag discharging part, set with water seal part, the furnace body upper part set with air inlet, gas exit, the furnace body set with water vapour inlet, the top of the furnace body set with water vapour exit, set with one hollow interlayer between the fire-resisting brick layer and furnace inner liner, the interlayer of the bottom of the inner furnace body connected the interlayer and the upper gas exit connected, in the interlayer set with air inlet channel, the air inlet channel upper part and upper part of the furnace body is of a connected air inlet, lower part inner furnace body and the bottom of air inlet channel connected. This utility new type a the municipal pyrogenation gastification furnace for life garbage into a combustion gas and slag, a generate a combustion gas of a recovery, a of a slag as a building bone material to be used.
NOVELTY - This new type utility claims one in a biomass gasification furnace of high temperature dust-removing device, comprise the biomass gasification furnace body, a top cover is set with a total air outlet of the biomass gasification furnace top of the furnace body, set with a support shaft, the support shaft of the biomass gasification furnace top of the furnace body rear end passes through the top cover by a first drive device driving the fixed end is sleeved in the lower support shaft is equipped with a cylindrical filter core, is densely distributed with several up and down through a through hole on the upper filter core, and the diameter of the through hole is 4 plus or minus 0.5 mm, height of filter control inner core is 250 to 350 mm range. This utility new type has simple structure, it can lower the high temperature directly to a condition of dust in a combustion gas separate, the efficient of dust removing and greatly reduces the heat loss of the combustible gas.
NOVELTY - Silkworm sand biological organic fertilizer granulating mix device, by stirrer, electrical machine, a feeding port, a double-spiral extruder, drying expansion cylinder, an air outlet, a dust remover, a first-stage round polishing machine, a polishing round machine level, three level circular polishing machine, a conveyor, a powder collecting tank, stir pole, a heater, a spiral feeding machine, a conveyor belt, wherein the centre position of upper end set with motor stirrer, one side of motor set with feeding port, a first-stage round polishing machine lower side of one end set with two level circular polishing machine, a polishing level round machine one end of lower side set with three level circular polishing machine, polishing level round machine one end of lower side set with a conveyor, one level circular polishing machine, a polishing level round machine, lower side of three-level polishing circular machine set with transmission belt, lower end of transmission belt set with powder collecting tank, this utility new type is a silkworm sand biological organic fertilizer granulating mix device structure is simple, the drying process for produce in a fertilizer micro dust by the dust remover is discharged to the lower one production process in, there is no dust, it does not affect the environment, but also increase the utilization ratio of fertilizer, and it is economical and environment-friendly.
NOVELTY - This utility new type claims a one movable organic fertilizer production device, include safety cover, a bottom plate, a safety cover and bottom plate of connecting seal of the cavity internal support plate through mounting a mix device, side edge of mix device set with a feeding transfer material through a feeding device, the lower part of mix c. crushing the uniform mix of fertilizer molding a granulation unit, granulating unit through the lower part set with a transmission belt molding fertilizer to the feeding transmission device, a feeding transmission device connecting packing. The organic fertilizer production process of all integrated together, which avoids the extra transport into a large amount of manpower and material resources, but also according to actual need of the device can be a mobile flexibility can, using machinery of feeding way, automatic degree high, novel design, which is a good one of innovation, it has market popularization prospect.
NOVELTY - This new type utility claims one has a methane fermentation tank, a fermentation tank of a feeding structure comprise two seal is of a tank body, a top cover and pedestal, a tank body upper part set with dry-type feeder, the bottom of the tank body set with a liquid feeder, a dry feeder comprise dry feed inlet and feeding dry tube, a dry-type feed tube and the tank body connecting part set with a closeness of one-way valve, a liquid feeder comprise the bottom of the tank body connected with a liquid feeding tube and used for support liquid feeding tube of the bracket. This utility new type set with double feeding structure for feeding and dry feeding a fluid on the basis of a traditional tank body, a fluid material and dry material from feeding, concentration of fermented dry material does not need a diluting the regulating pool directly entering into fermentation tank, the tank body to dry through biogas regulating, a comprehensive utilization of each a material, at the same time, saves a lot of regulating pool preparation of the energy.
NOVELTY - This utility new type claims a new-type integrative one anaerobic fermentation device, comprise the water device, an integrated anaerobic fermentation reactor, the water device, an anaerobic filling for filter pond, a sludge device, marsh gas collecting device, an integrated anaerobic fermentation reactor comprise anti-seepage bottom film, floating, anaerobic fermenting tank, a bottom film is set at the bottom and inner wall of anaerobic fermentation tank, floating a film on the top of the anaerobic fermenting tank, and between the floating tectorial membrane and anti-seepage bottom film forming one a methane storage space, the water device is set on the left side of anaerobic fermentation reactor, the water device is set at the right side of integrated anaerobic fermentation reactor, anaerobic suspension filling for filter pond inner anaerobic fermentation pool, sludge discharging device is set on a side edge anaerobic fermenting tank, marsh gas collecting device is set on side edge of anaerobic fermentation tank. This utility new type anaerobic fermentation tank through one of a large volume, sewage retention time long a treatment for livestock and poultry excrement sewage, so that organic pollutant in sewage of a completely of a, storing more marsh gas.
NOVELTY - This utility new type claims a one continuous biological carbon production device of a device, it comprise cracking tank, semicircular tube, an oil collecting-and-conveying tube, a combustion furnace, metal shell, box, support frame, feeding and discharging system, an air supplying system, a cooling system and a temperature measuring system, a wind system include air blower and air supply pipeline, each one set with a wind quantity adjusting valve two branch air supply pipeline of tube, a feeding spiral conveying machine, drive motor of spiral conveyor and discharging cooling spiral conveying machine are using variable-frequency motor, temperature sensor and controller connecting wire, a controller and a variable-frequency motor, an air quantity adjusting valve lead. This utility new type temperature sensor through a biological carbon production device of working temperature, and the temperature feedback to controller, controller by a rotating speed and wind amount of variable-frequency motor regulating opening degree of valve, a working speed and a temperature and a regulating so as to obtain ideal of biomass carbonization quality and efficiency.
NOVELTY - Bio-organic fertilizer comprises 10-30 pts. wt. Chinchilla excrement, 1-10 pts. wt. Auricula strain, 10-20 pts. wt. effective microorganisms (EM), 10-30 pts. wt. birch mushroom, 5-10 pts. wt. Armillaria tabescens, 30-50 pts. wt. waste material, 10-30 pts. wt. peat, 20-40 pts. wt. urea, 20-40 pts. wt. calcium superphosphate, 1-3 pts. wt. microbial fermentation inoculum and 1-5 pts. wt. adhesive.    USE - Used as a bio-organic fertilizer.    ADVANTAGE - The fertilizer can completely promote the fermentation of manure due to the presence of variety of bacteria, and thus it produces a variety of useful microorganisms during the fermentation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fertilizer, comprising (i) dissolving Auricula strain, effective microorganisms, birch mushroom, Armillaria tabescens and waste material in water, and adding microbial fermentation inoculum, then adding brown sugar, shaking under sealed conditions, and illuminating while cultivating for 18- 24 hours, maintaining the temperature at 25-30 degrees C, stopping the illumination process, regulating pH at 4 or less, and completing the cultivation process, and obtaining liquid broth; (ii) mixing peat, urea and calcium superphosphate, and naturally fermenting the mixture in a fermentation tank, fermenting for 10-15 hours, and separating aliquots of bacterial solution in the fermentation tank for every hour; (iii) raising the temperature of the fermentation product to 80 degrees C, taking overthrows, overthrowing towards left-right for 5-7 times, and completing the fermentation process; (iv) drying lavender, Viburnum macrocephalum and jasmine flower, and grinding into powder, and adding to the fermentation product, and stirring the mixture by placing in a stirrer, and uniformly stirring, and flattening out, drying, and crushing to powder form, and sieving to obtain the finished product.
NOVELTY - Production of hydrogen involves reacting aqueous-based raw material in an electric field-induced reactor, hydrolyzing to generate hydrogen radicals and hydroxide radicals, combining hydrogen radicals in presence of transition metal ion as catalyst to produce hydrogen, and converting hydroxide radicals to water and oxygen.    USE - Production of hydrogen (claimed).    ADVANTAGE - The hydrogen is produced with improved production efficiency and low energy consumption.
NOVELTY - Utilization of wet phosphoric acid residue involves mixing 100 pts. wt. wet phosphoric acid residue and 368-397 pts. wt. 65-70% sulfuric acid aqueous solution, decomposing and converting for 3 minutes, adding 500 pts. wt. phosphate rock with phosphorus pentoxide concentration of 29%, stirring, curing, and obtaining powdered superphosphate.    USE - Utilization of wet phosphoric acid residue and producing powdered superphosphate used for preparing fertilizer (claimed).    ADVANTAGE - Powdered superphosphate is economically produced using wet phosphoric acid residue by simple and environmentally-friendly process.
NOVELTY - Waste liquid utilization involves neutralizing synthetic rutile produced waste liquid into an ammoniation reactor with ammonia. The obtained material is precipitated to obtain iron compound. The obtained waste liquid is aged in an aging tank. The obtained material slurry is filtered through a filter press to obtain solid phase, and then washed with water, The obtained wet filter cake is separated, and then dried in a calcining kiln to obtain primary iron pigment. The washed liquids are combined to obtain a solution of magnesium chloride. Magnesium chloride solution is concentrated.    USE - Method for utilizing synthetic rutile produced waste liquid (claimed).    ADVANTAGE - The method is simple, cost-effective and eco-friendly.    DETAILED DESCRIPTION - Waste liquid utilization involves neutralizing synthetic rutile produced waste liquid into an ammoniation reactor with ammonia. The obtained material is precipitated to obtain iron compound. The obtained waste liquid is aged in an aging tank. The obtained material slurry is filtered through a filter press to obtain solid phase, and then washed with water, The obtained wet filter cake is separated, and then dried in a calcining kiln to obtain primary iron pigment. The washed liquids are combined to obtain a solution of magnesium chloride. Magnesium chloride solution is concentrated by evaporation systems, and then cooled the obtained material to crystallize. The obtained slurry is centrifuged, and then dried in a system to obtain ammonium chloride products. The mother liquid is concentrated in a system. The liquid magnesium chloride is dissolved to obtain a mixture of ammonium chloride and magnesium chloride.
NOVELTY - The processor comprises a water collecting system, a first level sewage channel, a second level sewage channel and a third level sewage channel. The first, second and third sewage channels: are connected with clapboard; provided with a baffle plate; and distributed with three suspension ball filler and a biological micropore aerator. The water collecting system comprises a water inlet pipe, a water outlet pipe, a regulating tank and a biological filter tank. The water inlet tube is connected with the regulating tank. The water outlet tube is connected with the filter tank.    USE - The processor is useful for treating wastewater (claimed).    ADVANTAGE - The processor treats the wastewater with large floor area in an economical manner.    DETAILED DESCRIPTION - The processor comprises a water collecting system, a first level sewage channel, a second level sewage channel and a third level sewage channel. The first, second and third sewage channels: are connected with clapboard; provided with a baffle plate; and distributed with three suspension ball filler and a biological micropore aerator. A length ratio of the first level sewage channel, a second level sewage channel and a third level sewage channel is 2-3:1:4-5. The water collecting system comprises a water inlet pipe, a water outlet pipe, a regulating tank and a biological filter tank. The water inlet tube is connected with the regulating tank. The water outlet tube is connected with the filter tank. An aperture of the filler is 0.5-3 cm. A length ratio of the first level sewage channel and third level sewage channel is 1:4. The filling rate of the first-level sewage channel is 40-50 vol.%. The filling rate of the third level sewage channel is 50-60 vol.%. An INDEPENDENT CLAIM is included for use of processor for treating wastewater.
NOVELTY - Anaerobic fermentation device comprises a fermenting tank (1), a heat preservation layer (4), a structure base (5), a support frame (7) and an inflation film (8), where the fermenting tank is embedded with the top of a side wall (2) of the fermenting tank. The inner wall of fermenting tank is set with a seal cover. The discharge hole is set with the top of the seal cover. The outer wall of fermenting tank is set with a heat preservation layer. An outer heat preservation layer is set with a support structure. The heat preservation layer and base structure of a support frame is set with ground.    USE - Anaerobic fermentation device used for preparing biogas and organic fertilizer from human and animal waste (claimed).    ADVANTAGE - The anaerobic fermentation device is prepared simply, and ensures improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biogas and organic fertilizer, which involves:    (A) mixing human and animal waste (5-10%) with bacterial fermentation residue uniformly in a fermentation tank;    (B) adding organic waste, where the water content of mixture is 45-65%, pH value 6.8-7.5, and temperature is 35-45 degrees C to obtain biogas;    (C) adding plant straw to the obtained mixture;    (D) mixing the obtained mixture, where the water content is 20-35%;    (E) fermenting the obtained mixture at 35-45 degrees C, and then fermenting the obtained material at 50-60 degrees C to obtain organic fertilizer; and    (F) mixing the obtained materials to obtain the desired product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an anaerobic fermentation device.    Fermenting tank (1)    Side wall (2)    Heat preservation layer (4)    Structure base (5)    Support frame (7)    Inflation film (8)
NOVELTY - Fertilizer additive comprises (in pts.wt.): wheat bran (10), silkworm excrement (50), corn (20), dried hawthorn leaf (50), dry yeast (1), oligosaccharide (10) and water (100).    USE - Fertilizer additive used for cultivating mushroom (claimed).    ADVANTAGE - The fertilizer additive has improved fertilizer effect and nutrition conversion rate in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer additive, which involves:    (A) heating wheat bran, silkworm excrement, corn and dried hawthorn leaf surface with water at 100 degrees C for 6 hours;    (B) leaching the obtained material;    (C) filtering the obtained material;    (D) standing the obtained material for 20-30 minutes;    (E) putting dry yeast and oligosaccharide in the obtained material;    (F) fermenting the obtained mixture for more than 10 days; and    (G) filtering the fermented liquid to obtain the desired product.
NOVELTY - Fertilizer additive comprises (in pts.wt.): silkworm excrement (4-10), molasses alcohol ferment liquid (4-10), oligosaccharide (0.5-1.5), dry yeast (1-2) and water (40-70).    USE - Fertilizer additive used for promoting microbe breeding.    ADVANTAGE - The fertilizer additive provides nutrition for crops, and activates soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer additive, which involves:    (A) leaching silkworm with water at 100 degrees C for 6 hours;    (B) pouring molasses alcohol ferment liquid to the obtained mixture;    (C) stirring the obtained mixture uniformly;    (D) standing the obtained mixture for 20-30 minutes at shady place;    (E) putting dry yeast and oligosaccharide to the obtained mixture;    (F) fermenting the obtained mixture for 30 days; and    (G) filtering the fermented liquid to obtain the desired product.
NOVELTY - Organic fertilizer additive comprises 10 pts. wt. wheat bran, 50 pts. wt. silkworm excrement, 20 pts. wt. cornmeal and 0.1 pts. wt. microbial strains.    USE - The additive is useful for promoting microbial growth.    ADVANTAGE - The additive can not only can provide comprehensive nutrition to crops, and increase the fertilizer efficiency, but also can increase and update the soil organic matter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the additive, comprising (i) mixing wheat bran, cornmeal and silkworm excrement by adding microbial strains, and uniformly stirring to compost by fermenting, and regulating the water content to 60%; and (ii) ventilating once the temperature is increased to 70 degrees C, turning once in every 24 hours, and completing the fermentation process for 18-20 days, to obtain the product.
NOVELTY - Organic fertilizer comprises organic matter, organic alcohol waste liquid and trace element. The alcohol waste liquid is preprocessed by heating alcohol waste liquid. The obtained liquid is concentrated, where the organic matter content is 40-75%. The pH of concentrated liquid is regulated to 5-6.5 using alkali agent or acid solution. Probiotic bacteria seed liquid is added to obtained liquid, and then fermented the obtained material for 20-48 hour. The fermented liquid is dried, where water content is less than 30%.    USE - Organic fertilizer used for black sugarcane (claimed).    ADVANTAGE - The organic fertilizer is economical and eco-friendly, and promotes root seedling, activates soil and promotes production of black sugar cane.
NOVELTY - Substrate comprises fermented vinegar residue, peat and vermiculite complex, where the volume fraction of fermented vinegar residue, grass carbon (peat) and vermiculite is -1-70, 1-30 and 1-30, respectively.    USE - Substrate used for cultivating cherry tomato (claimed).    ADVANTAGE - The substrate is cost-effective, eco-friendly and prepared in simple manner, and increases tomato plant growth index, chlorophyll content, yield and quality of cherry tomato.
NOVELTY - Composite fertilizer preparation involves selecting potassium chloride (100 g) and sulfuric acid (30-60 ml). The selected material is heated at 100-110 degrees C for 15-30 minutes to obtain potassium bisulfate, and then diluted with dilute solution of phosphoric acid. The mixed acid is mixed with synthetic ammonia liquid in a tubular reactor to obtain compound fertilizer slurry. Organic complex fertilizer (10-20%), plant ash (5-10%) and magnesium aluminum silicate powder (2-8%) are added, and then stirred uniformly at 25-40 degrees C. The obtained material is granulated in a spraying rotary drum granulator.    USE - Method for preparing composite fertilizer (claimed).    ADVANTAGE - The method enables to prepare composite fertilizer that is economical, cost-effective and eco-friendly, and promotes root seedling and activates soil.
NOVELTY - Tea tree fertilizer comprises covering layer and inner fertilizer particles. The fertilizer particle includes 2-3 pts. nitrogen fertilizer, 2-3 pts. phosphate fertilizer, 2-3 pts. potash fertilizer, 10-15 pts. rotten fermented silkworm excrement, and 10-15 pts. molasses alcohol fermentation liquid. The covering layer is a slow release carrier containing stearic acid, adhesive and ore powder.    USE - Used as tea tree fertilizer.    ADVANTAGE - The fertilizer provides essential nutrients required for growth of tea tree, contains slow release carrier thus achieves slow release and reduces loss of fertilizer components, increase utilization rate, and does not cause white pollution.
NOVELTY - Bio-fertilizer comprises 20-40% phosphate fertilizer, 20-40% nitrogen fertilizer, 10-30% organic matter, 5-25% strain (arbuscular mycorrhiza, phosphate-solubilizing bacteria and Rhizobium), 0-15% potash fertilizer, 2-8% synergist, 0.5-4% trace elements and 0.5-2% adhesive, where the bio-fertilizer is a porous granule.    USE - Used as bio-fertilizer.    ADVANTAGE - The bio-fertilizer enhances absorption of phosphate fertilizer by crops, reduces dosage amount, rapidly dissolves in water, does not cause pollution and suitable for modern agriculture and fertilizer integration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing bio-fertilizer, comprising: (a) adding arbuscular mycorrhiza, phosphate-solubilizing bacteria and Rhizobium into a reactor, then adding phosphate fertilizer, organic matter and adhesive into the reactor and carrying out fermentation adsorption for 3 days to obtain organic mixed flora; (b) adding nitrogen fertilizer, potassium fertilizer, trace elements and synergist into resultant organic mixed flora, stirring at 80-100 rotations/minute under room temperature for 30-60 minutes to obtain organic mixed fertilizer; and (c) adding organic mixed fertilizer into a microporous extrusion granulator and extruding into cake-shaped strips via double-roller, subjecting to needling via micro-hole of porous granulator, cutting into granules by circular cutter, screening, drying at 40-60 degrees C and cooling.
NOVELTY - Preparing Beauveria bassiana biological complex fertilizer comprises mixing 60-80 pts. wt. culture medium and 20-43 pts. wt. auxiliary carbon source, adding water, adjusting moisture content of mixture to 35-45 wt.%, adding the aqueous mixture into a solid state fermentation tank, and fermenting at 20-35 degrees C in ventilated environment for 9-11 days by stirring once for every 26-32 hours, drying the fermented mixture at 50-80 degrees C, crushing, checking quality, and granulating to obtain fertilizer granule.    USE - The method is useful for preparing Beauveria bassiana biological complex fertilizer (claimed).    ADVANTAGE - The fertilizer reduces use amount of chemical pesticide, increases fertility of soil, improves product quality and reduces environmental pollution.    DETAILED DESCRIPTION - Preparing Beauveria bassiana biological complex fertilizer comprises (i) mixing 60-80 pts. wt. culture medium and 20-43 pts. wt. auxiliary carbon source, adding water, adjusting moisture content of mixture to 35-45 wt.%, adding the aqueous mixture into a solid state fermentation tank, and fermenting at 20-35 degrees C in ventilated environment for 9-11 days by stirring once for every 26-32 hours; (ii) drying the fermented mixture at 50-80 degrees C, crushing, checking quality, and granulating to obtain fertilizer granule; and (iii) separating and purifying Beauveria bassiana hyphae and spores and inoculating on the fertilizer granule, where the fertilizer granule is used as solid fermentation culture medium. An INDEPENDENT CLAIM is also included for Beauveria bassiana biological complex fertilizer, comprising 60-80 pts. wt. culture medium and 20-43 pts. wt. auxiliary carbon source
NOVELTY - Device comprises a waste collecting reservoir (1), where the waste collecting reservoir is connected with a waste jar (6) through a pipeline (4). The waste jar is set with multi-outlet (5,7). The secondary chicken waste utilization device also comprises an electric control valve (2), a coop (3), and a water flow channel (8). The multi-outlet of the waste jar is connected with a marsh gas generating cell.    USE - Device used for utilizing waste from chicken farm (claimed).    ADVANTAGE - The device is eco-friendly, cost-effective, and has reduced labor intensity and improved working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a chicken waste utilization device.    Waste collecting reservoir (1)    Electric control valve (2)    Coop (3)    Pipeline (4)    Multi-outlets (5,7)    Waste jar (6)    Water flow channel (8)
NOVELTY - Fertilizer comprises (in pts. wt.): silkworm excrement (50-60), duck manure (30-40), pig manure (20-30), rapeseed cake (10-15), straw particle (300-400), river sludge (30-40) and potassium fertilizer (20-30).    USE - Fertilizer used for increasing the yield of white pepper (claimed).    ADVANTAGE - The fertilizer increases absorption of nutrition, accelerates the growth speed, and shortens the market period.
NOVELTY - Microbial organic fertilizer comprises agricultural solid organic waste produced using Bacillus subtilis with 2x 108 colony forming unit (CFU) and moisture content of less than 30%.    USE - The microbial organic fertilizer useful for controlling cropping obstacles (claimed).    ADVANTAGE - The microbial organic fertilizer accelerates decomposition of Artemisia stubble, inhibits proliferation of soil pathogens, accelerates crop growth, reduces Artemisia by 91% and increases Artemisia production by 3.3 times.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the microbial organic fertilizer, comprising (a) inoculating Bacillus subtilis in Bacillus subtilis liquid fermentation culture medium to obtain fermentation broth, where the fermentation conditions include: initial PH of 6.5-7.2, culture temperature of 35-37 degrees C, air amount of 30-100 wt.%, rotating speed of 120-180 revolutions per minute, and fermenting for 18 hours, fermenting until the liquid spore number is greater than or equal to 2x 108 CFU/ml, (b) adding 10% fermentation broth into a solid fermentation culture medium, fermenting at 37 degrees C for 5 days, stirring once in every 10-20 hours during the fermentation process, crushing the fermented solid substances by a crusher, sieving via 10 meshes sieve to obtain solid fermentation strain of Bacillus subtilis, and (c) mixing Bacillus subtilis solid fermentation strain with 5-8% pig manure compost, decomposed cattle manure, compositing at 20-35 degrees C, turning once in every 7 days, stacking for 12-25 days, composting until the microbial organic fertilizer water content is less than 30%, and content of organic substances is more than 30%, and packing.
NOVELTY - Agricultural fertilizer comprises (in pts.wt.): corn straw (10-20), corncob (10-15), cottonseed hulls (15-30), soyabean cake (10-20), microelement (2-4), sugarcane meal (12-18), effective microorganisms (EM) bacteria (0.5-2) and food debris (20-30).    USE - Agricultural fertilizer.    ADVANTAGE - The agricultural fertilizer is eco-friendly, cost-effective, and increases the fertility of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing agricultural fertilizer, which involves:    (A) crushing corn straw, corn cob and soybean cake;    (B) mixing the crushed material with microelement, cotton seed hulls, sugarcane meal and food debris uniformly;    (C) adding water to the obtained mixture;    (D) adding EM bacteria to the obtained mixture;    (E) fermenting the obtained mixture for 10-30 days; and    (F) packing the obtained material to obtain the desired product.
NOVELTY - Eucalyptus fertilizer additive comprises 2-10 pts. trace element, 6-12 pts. molasses alcohol fermenting liquid and 1.6-2 pts. slow release agent; where molasses alcohol fermenting liquid has concentration of 20-40%; and the slow release agent is stearic acid melt, adhesive and mineral powder.    USE - Used as an Eucalyptus fertilizer additive.    ADVANTAGE - The additive promotes fast growth of eucalyptus, is rich in amino acid, humic acid and organic matter, which are required for improving soil, supplementing nutrients and promoting fast growth of tree; slowly release the components; reduces the loss rate of fertilizer; and increase utilization rate of fertilizer.
NOVELTY - Recycling glyphosate by processing waste water, comprises (i) preprocessing glyphosate waste water by filtering; (ii) filling an absorption resin into pre-treated waste water at 10-40 degrees C at a flow rate of 0.5-3 bed volume (BV)/hour conditions into or filling column with absorbing resin and an ion exchange resin to carry out adsorption treatment; (iii) subjecting resin to desorption process, adding a desorption agent at a flow rate of 0.5-2 BV/hour, where the desorption temperature is 20-60 degrees C; and (iv) processing the desorbed product by concentrating, and re-crystallizing.    USE - The method is useful for recycling glyphosate by processing waste water (claimed).    ADVANTAGE - The method has high recovery rate of glyphosate produced in waste water; and guarantee subsequent depth standard of waste water treatment or water recycling process, and treatment of waste water simultaneously with no waste of resources.
NOVELTY - Organic fertilizer, is claimed. The organic fertilizer is prepared by fermenting pond sludge, straw, chicken manure and mushroom residue at 65-80 degrees C for 10-15 days, then carrying out secondary fermentation at 35-45 degrees C for 20-30 days, adding microbial inoculum and mixing uniformly.    USE - Used as organic fertilizer.    ADVANTAGE - The fertilizer is environmentally-friendly, nontoxic, economical and easily absorbed.
NOVELTY - Method of biogas obtaining includes preliminary processing of an organic substrate by bringing it to 92% humidity with further crushing, introduction of a catalyst, fermentation in an anaerobic medium, and accumulation of biogas. As the catalyst used is a four-component mixture, which contains four classes of enzymes: protease, amylase, lipase and cellulase with their weight ratio of 3.2:0.3:15.6:1.0, the catalyst is introduced in a volume of 0.01 g/kg of weight of the dry organic substrate, and fermentation in the anaerobic medium is realised at a temperature from 17 degrees C to 20 degrees C. The application of the claimed method of biogas obtaining will make it possible to obtain a good methane output with comparatively low concentrations of the enzyme mixture.    USE - Chemistry.    ADVANTAGE - Intensification of the process of methane manure fermentation with an increase of the biogas output and increased content of methane in it.1 dwg, 1 tbl
NOVELTY - Producing a biodiesel, comprises: (a) providing animal or vegetable oil to create a first component; (b) combining a short chain alcohol with a strong base to create a second component; and (c) combining the first and second components together in the presence of a mesh i.e. in contact with the combined components.    USE - The method is useful for producing the biodiesel (claimed).    ADVANTAGE - The method is capable of efficiently, economically and rapidly producing the biodiesel with improved yield and lubricating properties, and without requiring expensive machinery such as centrifuges, decanters and ultrasonic devices.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) reacting a natural oil with a short chain alcohol in the presence of an alkaline catalyst, comprising (i) providing a natural oil, (ii) providing a short chain alcohol, (iii) providing an alkaline catalyst, (iv) providing a mesh material, (v) combining the short chain alcohol with the alkaline catalyst into a composition (a), and (vi) combining the composition (a) with the natural oil in the presence of the mesh material;    (2) the biodiesel produced by the process;    (3) a fatty acid methyl ester produced by the above process; and    (4) a biodiesel batch reactor, comprising the mesh material within the interior of the batch reactor.
NOVELTY - The method involves determining long-term power management directives that include a charging threshold by an advisory layer (502) with model predictive control (MPC) using a processor. The optimal set points or reference trajectories are provided to reduce a cost of energy advisory layer. The real-time actions are determined based on the charging threshold to adaptively charge a battery from the power sources or to discharge the battery.    USE - Method for performing multi-objective energy management of micro-grids used for utility connection, micro-gas turbine and renewable generation such as fuel cell, wind turbine, and solar panel.    ADVANTAGE - The MPC objective function is updated for battery and grid power cost minimization over the optimization horizon and updates equality and inequality constraints of MPC optimization problem for optimization horizon. The balance is guaranteed between generation and consumption within the micro-grid at each time step while the optimal performance constraints provided are satisfied by MPC at advisory layer. The energy generations are dispatched in way, so that the operational cost is minimized. The balance is guaranteed between supply and demand at the presence of unpredictable variations of distributed generations (DG) and other physical limitations of a real micro grid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a multi-objective energy management system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the two-tiered power management system.    Advisory layer (502)    Real time layer (504)
NOVELTY - Pellet fuel comprises mixture of multiple combustible wastes having 40-80 meshes particle size as substance, fuel material and binder including industrial binder, vegetable binder or animal binder. The pellet fuel is obtained by supplying fuel material and 2-30 wt.% binding agent into a binder supply tank, mixing in a mixing vessel, extruding by an extruder to produce fuel material. The produced fuel material is molded in pellet fuel by a pellet molding apparatus, cut in rod-shaped by a cutter and solidified by cooling in different rod-shaped.    USE - Used as pellet fuel.    ADVANTAGE - The apparatus solves disposal problem of combustion waste and other industrial waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for pellet molding apparatus comprising a binder supply tank (2) provided with an agitator, a heating tank and a flow adjusting apparatus for supplying binder to bind with fuel material, and located on top of a base (1), a fuel material supplier (3) provided with an agitator, a heating tank and flow adjusting apparatus for supplying the fuel material with the multiple combustible wastes, disposed over the base, a mixing chamber (4) provided with an agitator, a heating tank and a flow adjusting apparatus for mixing the binder with the fuel material, disposed in the middle portion of the base, an extruder (5) equipped with a heating tank for extruding the fuel material, a pellet molding apparatus provided with a cooling means for forming extruded material in rods shaped, and a cutter for cutting the molded pellets into rod-shaped.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the pellet molding apparatus.    Base (1)    Binder supply tank (2)    Fuel material supplier (3)    Mixing chamber (4)    Extruder (5)
NOVELTY - Manufacture of synthesis fuel involves carrying out reforming reaction by reacting methane, water vapor and carbon dioxide in presence of nickel catalyst membrane, and performing Fischer-Tropsch reaction of obtained synthesis gas containing hydrogen and carbon monoxide. The molar ratio of total content of water vapor and carbon dioxide, and methane is 2-4.    USE - Manufacture of synthesis fuel (claimed).    ADVANTAGE - Coke deposition on the catalyst membrane due to the cracking reaction of methane is suppressed, such that the catalytic activity is maintained for long period of time. Unreacted synthesis gas is recycled after Fischer-Tropsch reaction, such that process energy efficiency and carbon utilization efficiency are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen and carbon monoxide-containing synthesis gas.
NOVELTY - Co-production of ammonia, urea and methanol from natural gas, comprises (a) producing a synthesis gas by simultaneously feeding natural gas to an autothermal reformer (ATR) and to a steam methane reformer (SMR), (b) feeding air to an air separation unit (ASU), (c) subjecting the synthesis gas from the SMR to a water gas shift, (d) removing the carbon dioxide from the synthesis gas, (e) combining the hydrogen-rich gas with the nitrogen, (f) optionally removing part of the carbon dioxide from the syngas, and (g) leading the syngas to the methanol synthesis unit.    USE - The method is useful for the co-production of ammonia, urea and methanol from natural gas (claimed).    ADVANTAGE - The method ensures efficient co-production of ammonia, urea and methanol from natural gas without excess use of carbon dioxide.    DETAILED DESCRIPTION - Co-production of ammonia, urea and methanol from natural gas, comprises (a) producing a synthesis gas by simultaneously feeding natural gas to an autothermal reformer (ATR) and to a steam methane reformer (SMR) running in parallel, (b) feeding air to an air separation unit (ASU), where the air is split into nitrogen and oxygen that is fed to the ATR, (c) subjecting the synthesis gas from the SMR to a water gas shift, (d) removing the carbon dioxide from the synthesis gas and leading it to urea synthesis in a urea synthesis unit, (e) combining the hydrogen-rich gas with the nitrogen, removing catalyst poisons and part of inters from the gases and leading the gas mixture to ammonia synthesis in an ammonia synthesis unit, (f) optionally removing part of the carbon dioxide from the syngas from the ATR and leading it to a urea synthesis unit, and (g) leading the syngas to the methanol synthesis unit, where synthesis gas is led either from the ATR outlet to the SMR outlet upstream from the shift stage or the other way.
NOVELTY - The apparatus has a first link plate connected with rotational axes with a rocking plate that is supported with a stoker board of even number sequences of stoker board groups (42). A second link plate is connected with the rotational axes with the rocking plate that is supported with the stoker board of odd number sequences of the board groups. First and second driving cylinders move the link plates along forward or backward direction. Coolant water supplied from a cooling unit (70) is formed in a hollow pipe through a circulation path while forming the rotational axes in the hollow pipe.    USE - Heating apparatus for use with a biomass carbonization furnace i.e. chamber, for carbonizing biomass feedstock i.e. biological-origin organic resource, such as chaff and wood chip to generate fertilizer i.e. carbon fertilizer, such as soil improvement substance for promoting growth of crops of grass and tree.    ADVANTAGE - The apparatus continuously performs carbonization process without completely combusting of biomass feedstock for generating the carbon, warm water or vapor by using heat-generation of a heater, so that the fertilizer such as the soil improvement substance can be generated from the biomass feedstock, thus ensuring global warming prevention in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a principal part of a heating apparatus provided with a carbonization furnace. '(Drawing includes non-English language text)'    Exhaust passage part (24)    Partition plate (26)    Communicating tube (28)    Stoker board groups (42)    Cooling unit (70)
NOVELTY - The combustor (14) has a first air flow path (421) for introducing air into a combustion chamber (401). The air introduced into the combustion chamber comes in contact with the heat emitter (481) of an ignition equipment (48), and collides with the combustion chamber inner wall face (402). An electronic controller is configured to control the heat emitter to heat the air colliding the combustion chamber inner wall face until the temperature of the combustion chamber wall surface exceeds the required temperature before the ignition of the air-fuel mixture.    USE - Combustor used in burning fuel and producing hot combustion gas for fuel cell system.    ADVANTAGE - Prevents incomplete combustion and emission of carbon monoxide due to the controlled operation of the heat emitter of the ignition equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional drawing of the combustor. (Drawing includes non-English language text).    Combustor (14)    Ignition equipment (48)    Combustion chamber (401)    Combustion chamber inner wall face (402)    First air flow path (421)    Heat emitter (481)
NOVELTY - The method involves performing electric current fluctuation process in which increase and decrease of electric current makes electric power generation portion supply and electric-power-generate reactive gas. The output of the electric power generation portion is measured during execution of electric current fluctuation process. Quality of electric power generation portion is determined based on change of output of electric power generation portion in execution of electric current. A fuel cell is comprised using the electric power generation portion.    USE - Manufacturing method of fuel cell used in electric power generation portion (claimed).    ADVANTAGE - The fuel cell can be manufactured efficiently. The precision of the evaluation test about the drain property of the fuel cell can be improved. Usability of the fuel cell can be improved. Simplification and manufacturing cost reduction of the fuel cell can be achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) evaluation method of electric power generation portion; and    (2) an evaluation apparatus of electric power generation portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell evaluation apparatus. (Drawing includes non-English language text)    Terminal (33)    Fuel cell evaluation apparatus (100)    Main control unit (110)    Fuel gas supply unit (120)    Voltage measurement unit (130)
NOVELTY - The device has an ultraviolet (UV) source for impact to electrolyte, placed in an electrolytic cell, and electrodes made in the form of arranged plates made from stainless steel with vertical and horizontal notches substituted on the surface and with opening for circulation of electrolyte and removal of gas. The openings in adjacent arranged plates are noncoaxial. A cavity of the case of an electrolyzer is connected by two channels with container for electrolyte. The outputs of channels arranged on opposite housing walls of electrolyzer and on contrary of each arranged plates.    USE - Electrolytic device for obtaining gaseous mixture of hydrogen and oxygen.
NOVELTY - The generator set comprises a machine that is easily operated and maintained with an effective processing system effectively and efficiently provides electricity. The temperature fluctuations and careful regulation of temperature is observed to prevent accidents.    USE - Multi-purpose biogas generator set.    ADVANTAGE - The technical problems that causes burn to people is prevented. The hazard to human health in transporting night soil and other wastes is reduced.
NOVELTY - The method involves injecting water steam jet stream of the high temperature generated with an electric arc-plasma jet in middle region of a reactor (10). The raw material pillar is heated in a circular cavity (11) which supplied the oxidizing agent. The portion of the organic component of the solid organic raw material within the circular cavity is gasified completely. The inside of the reactor is sucked in the other end side, and the fuel gas generated from the solid organic raw material is taken out at the temperature of 850 degrees C or more.    USE - Method for gasifying solid organic raw material such as various waste material, coal, timber, biomass, timber, and charcoal in gasifier (claimed). Can also be used as fuel for thermal power generation.    ADVANTAGE - The weight of the gasifier is reduced, thus the manufacturing cost, and running cost are suppressed. The synergy of the heat generated during combustion and the heating caused by the plasma makes the remaining organic component within the raw material to gasify, thus gasification is efficient. The gasification velocity is improved, and the power consumption of the electric arc-plasma jet is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasifier of solid organic raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gasifier.    Gasifier (1)    Reactor (10)    Circular cavity (11)    Residual-ashes discharging apparatus (50)    Electric motor (51)
NOVELTY - A nickel-phosphorus-alumina aerogel catalyst is obtained by performing gel reaction of nickel precursor, phosphorus precursor and alumina precursor, and dispersing the obtained gel in epoxide aqueous solution under supercritical carbon dioxide condition, and drying, and has internal porosity of 2-50 nm. The atomic ratio of nickel precursor and aluminum precursor is 0.01-1:0.01-1.    USE - Nickel-phosphorus-alumina aerogel catalyst is used for producing hydrogen gas by steam reforming reaction of liquefied natural gas.    ADVANTAGE - The nickel-phosphorus-alumina aerogel catalyst has excellent catalytic activity and adsorption capability with respect to reactant, and provides hydrogen gas with high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of nickel-phosphorus-alumina aerogel catalyst; and    (2) production of hydrogen gas.
NOVELTY - The method involves providing purifier with the waste oil heating kettle (10) for heating waste oil, while removing the gas pipe outside the gas emitted inside the waste oil heating kettle. A condenser (46) is provided to add condensation with respect to the gas taken out with the gas pipe (44). The fuel oil is purified by adjusting the relative position in the perpendicular direction of the waste oil heating kettle and the condenser is fractionated according to specific gravity.    USE - Method for purifying fuel oil derived from waste oil such as waste edible oil and tempura oil.    ADVANTAGE - The fuel oil derived from waste oil is fractionated by simple process, as the fuel oil is purified by adjusting the relative position in the perpendicular direction of the waste oil heating kettle and the condenser is fractionated according to specific gravity.    DETAILED DESCRIPTION - The extension in the perpendicular direction of the gas pipe is changed. The compatibility of gas pipe is differed with arbitrary pipes in perpendicular direction. An INDEPENDENT CLAIM is included for apparatus for purifying fuel oil derived from waste oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of waste oil heating kettle.    Waste oil heating kettle (10)    Waste oil supply pipe (32)    Gas pipe attaching port (42)    Gas pipe (44)    Condenser (46)
NOVELTY - The apparatus has combustor (2) which burns the hydrogen-containing-gas. The waste gas flow path (8) is formed into which the waste gas from the combustor flows. The branched path (11) is provided on primary waste gas flow path. The carbon monoxide (CO) detector (9) is provided in the branched path. The circuit breaker (10) interrupts the inflow of the waste gas to the branched path. The controller (12) blocks the circuit breaker in period, when waste gas flows into primary waste gas flow path.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The apparatus responds appropriately even during burning and discharging hydrogen containing-gas with combustor in CO detector.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Combustor (2)    Waste gas flow path (8)    CO detector (9)    Circuit breaker (10)    Branched path (11)    Controller (12)
NOVELTY - The improvement method involves removing a fine aggregate and a coarse aggregate with a vibrating strainer, and obtaining sludge water from ready-mixed-concrete sludge. The sludge water is filtered for obtaining solid content. The solid content is dried after filtering, and is made into a powder form. The solid content contains blast furnace slag. A 40 kg or more of solid content is mixed in conversion of a dry mass with respect to one cubic meter of soil.    USE - Soil improvement method using sludge powder.    ADVANTAGE - Utilizes ready-mixed concrete sludge that is effective in soil improvement. Greatly contributes not only to the effective usage of the sludge processed as industrial waste but to the effective usage of construction generated soil.    DESCRIPTION OF DRAWING(S) - The drawing shows the graphical view of the relationship of the uniaxial compressive strength and the cone index in the soil modified with different materials. (Drawing includes non-English language text).
NOVELTY - Production of hydrogen (16) involves providing reaction cell (30) containing tube (A) of hydrogen-permeable material and tube (B) of impermeable material, such that gap space is formed between tube (A) and tube (B), heating the gap space, and introducing mixture of hydrocarbon fuel and steam (22) into the gap space, such that mixture is thinned in the gap space causes steam and hydrocarbon fuel to absorb heat and react in water gas shift reaction to produce reaction gases (24) containing hydrogen gas. The gap space between tube (A) and tube (B) is 100-1000 mu m.    USE - Production of hydrogen used for proton exchange membrane fuel cell.    ADVANTAGE - The method efficiently provides hydrogen.    DETAILED DESCRIPTION - Production of hydrogen involves providing reaction cell containing concentrically positioned tube (A) of hydrogen-permeable material and tube (B) of impermeable material, such that gap space is formed between tube (A) and tube (B), heating the gap space, and introducing mixture of hydrocarbon fuel and steam into the gap space, such that mixture is thinned in the gap space causes steam and hydrocarbon fuel to efficiently absorb heat and react in water gas shift reaction to produce reaction gases containing hydrogen gas. At least some of the hydrogen gas permeates through the tube (A) and separates from remainder of the reaction gases. The gap space between tube (A) and tube (B) is 100-1000 mu m.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of hydrogen processor.    Hydrogen gas (16)    Mixture of hydrocarbon fuel and steam (22)    Reaction gas (24)    Exhaust gas (26)    Reaction cell (30)
NOVELTY - Fuel composition prepared from waste vegetable oil, comprises an emulsion of water and waste vegetable oil ethyl ester blended with diesel and an alcohol, where waste vegetable oil relates to cooking oil which has been used for frying an edible material, at least once.    USE - The fuel composition is useful as green alternative fuel for diesel engine.    ADVANTAGE - Alternative fuel is provided which is economic and is eco-friendly. Engine is also provided which is best suited for the fuel, where exhaust gases are recirculated to reduce nitrogen oxide (NOx) emissions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing fuel composition, from waste vegetable oil, which involves: (a) transesterification of waste vegetable oil with an alcohol to produce waste vegetable oil ethyl ester; (b) emulsifiying water and waste vegetable oil ethyl ester obtained in step (a); (d) blending emulsified water ethyl ester with diesel and alcohol; and    (2) a system for burning fuel composition comprising an internal combustion engine where exhaust gases are recirculated.
NOVELTY - The apparatus (100) has a modifier (1) that generates reformed gas from raw material containing hydrocarbon component and hydrogen. A combustor (2) burns the combustible gas containing a hydrocarbon component and heats modifier. An air supply device (3) supplies air to combustor. A combustible-gas supply device (4) supplies the combustible gas to combustor. A carbon monoxide detector (5) detects the carbon monoxide in combustion exhaust gas discharged from combustor. A controller (6) stops operation of combustor, when carbon monoxide is not detected by carbon monoxide detector.    USE - Hydrogen generating apparatus for electric power generation system.    ADVANTAGE - Since the abnormality in carbon monoxide detector is inspected, the hydrogen generating apparatus which can perform operation confirmation of carbon monoxide detector simply is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Combustor (2)    Air supply device (3)    Combustible-gas supply device (4)    Carbon monoxide detector (5)    Controller (6)    Hydrogen generating apparatus (100)
NOVELTY - The fuel cell system (200) has a circulation unit which forcedly circulates the gas containing hydrogen and water vapor between a hydrogen-producing unit and an electric power generation/electrolysis unit. A gas flow path control unit controls a gas flow path to suppress the circulation of the gas by the gas flow path, when operation of the fuel cell system switches from an electric power generation operation to a charging operation.    USE - Secondary battery type fuel cell system for use in electric power feeding system (claimed).    ADVANTAGE - The water vapor generated in the electric power generation/electrolysis unit at the time of the electric power generation operation of the secondary battery type fuel cell system is supplied to the electric power generation/electrolysis unit, without passing through the hydrogen-producing unit. The water vapor supplied to the electric power generation/electrolysis unit is made to increase by immediately after operation of the secondary battery type fuel cell system switches from electric power generation operation to charging operation, and responsiveness immediately after switching from electric power generation operation to charging operation is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electric power feeding system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the electric power feeding system. (Drawing includes non-English language text)    Fuel electrode (2B)    Heaters (3,4)    Containers (5,6)    Piping (7,10,11)    Fuel cell system (200)
NOVELTY - Anaerobic digesters controlling involves determining proportion of different waste mixture and hydraulic residence time of system by linear programming techniques that maximize an objective function and methane production. The diagnostic parameters are calculated, where alkalinity ratio is also determined. The control action determined linear constraint limits of the linear programming process.    USE - Method for controlling anaerobic digesters in treatment of different organic waste.    ADVANTAGE - The method improves anaerobic digestion yields, enhances performance in biogas digesters due to synergies between different substrates, and balances nutrients or moisture content in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a computer program product, which includes program instructions for causing a computer system for performing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the anaerobic digesters controlling method. (Drawing includes non-English language text).
NOVELTY - Bioorganic fertilizer comprises organic urea fertilizer, organic nitrogen-phosphorus-potassium (NPK) fertilizer, and bioorganic solution comprising Alcaligenes sp., Bacillus megaterium, Lactobacillus sp., Azospirillum sp., Azotobacter chroococcum, Penicillium sp., Trichoderma sp. and humic acid solution plant growth stimulant.    USE - Bioorganic fertilizer.    ADVANTAGE - The fertilizer improves physical, chemical and biological properties of soil. In the ground, organic fertilizer binds elemental nitrogen and is converted into humus or soil organic materials by organisms. The organic materials serve as primary grain binder and soil becomes secondary granules in the formation of stable aggregates, and the microorganisms improve soil structure and increase soil nutrients and fertility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of bioorganic solution by mixing microbial solution with mixture of humic acid and palm oil, coconut husk powder, molasses, urine, beef blood, beef offal, rice bran and water; and fermenting for greater than or equal to 2 years;    (2) preparation of organic urea fertilizer by crushing cow manure and phosphate/dolomite/zeolite into 2-5 mm particles, diluting bioorganic solution with water and spraying on crushed material, and treating so that nitrogen binding is increased to 24.98%; and    (3) preparation of organic NPK fertilizer by crushing cow manure, phosphate/dolomite/zeolith and rock phosphate into 2-5 mm particles, diluting bioorganic solution with water and spraying on crushed material, treating, and adding organic potassium.
NOVELTY - The modifier (130) has a first flow path (A) that is included in inner side of inner tube (210) in which gasifying gas (X1) is formed to gasify the gasification raw material by a gasifier. A second flow path is formed between the inner tube and outer tube (220) surrounding the outer side of inner tube, and provided downstream of the first flow path. A catalyst (230) which accelerates modification of tar in the gasifying gas is arranged in the second flow path. The gasifying gas which circulates first flow path is made to heat the catalyst through the side wall of inner tube.    USE - Modifier for modifying tar contained in gasifying gas generated by gasifying gasification raw material (all claimed) such as solid raw materials e.g. wood coal, petroleum coke, biomass and tire chip, and liquid raw materials e.g. black liquor, and used for electric power generation system, manufacture of hydrogen, manufacture of synthetic petroleum, manufacture of chemical fertilizer e.g. urea.    ADVANTAGE - The reduction of combustible gas is suppressed. The catalyst is pre-heated efficiently and the tar and dust which remain in the gasifying gas are removed effectively from the gasifying gas by a simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modifier. (Drawing includes non-English language text)    Modifier (130)    Inner tube (210)    Outer tube (220)    Catalyst (230)    First flow path (A)    Gasifying gas (X1)
NOVELTY - Molded charcoal without harmful elements comprises an active part, which is divided into an upper portion (20) including ignition part and igniting by creating harmless fuel ash, and a lower portion (30) inhales toxic gas (carbon monoxide) generated in the upper portion using an activation catalyst by ignition and combustion, and removing toxic gas from the lower portion. The molded charcoal (10) comprises 75-85 wt.% upper portion and 15-25 wt.% lower portion.    USE - The molded charcoal eliminates or reduces effect of toxic gases (carbon monoxide) generated during combustion, and has excellent calorific value, ignitability and storage stability compared to traditional ignition coal.    ADVANTAGE - Used as a molded charcoal without harmful elements.
NOVELTY - Extrusion molding machine conveying device comprises a crushing unit for crushing raw materials and is installed on a injection unit (12) of an extruder main body (10), and a compressing unit (30) for extruding solid fuel through an extrusion die by feeding compressed raw material crushed by the crushing unit into the extrusion die.    USE - Used as an extrusion molding machine conveying device.    ADVANTAGE - The device has improved productivity, increases the conveying efficiency of fuel and raw materials, does not convey raw materials with low specific gravity, produces compressed raw materials with high-density, and utilizes lightweight raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the extrusion molding machine conveying device.    Extruder main body (10)    Injection unit (12)    Transfer line (14)    Compressing unit (30)    Extruding feeding shaft (32)
NOVELTY - Oxidative reaction of herbal hydroxycinnamic acids in highly concentrated solution to an aqueous reaction solution for applying on fertilizer granules and hardening, comprises (i) preparing a highly concentrated weakly acidic to mildly alkaline reaction solutions from ferulic acid, containing their oxidation- and polymerization products, (ii) reacting the hydroxycinnamic acids for preparing reaction solutions using chemical or biochemical radical polymerization initiators, preferably ammonium persulfate, and (iii) hardening the reaction solution on the fertilizer granules by heating.    USE - The reaction solution is useful for coating the fertilizer granules (claimed).    ADVANTAGE - The method utilizes bio-based components, which are generated as waste materials in industrial processes.
NOVELTY - Oil-based solid lip cosmetics comprise 4-8 mass% polyethylene wax, 0.1-3 mass% multi wax, 10-50 mass% heavy liquid isoparaffin and/or polybutene and 10-40 mass% diisostearic acid polyglyceryl and/or triisostearic acid polyglyceryl in which cosmetics have needle insertion hardness of 20-80 g in hardness meter.    USE - Oil-based solid lip cosmetics (claimed).    ADVANTAGE - Perspiration prevention in high temperature is excellent.
NOVELTY - Cleaning shovel comprises a set, where the top surface of the set comprises a shovel body (1) and one end of shovel body is hinged on the machine body (7) of a lifting oil jar (3), where the lifting oil jar is hinged with a bracket (4). The bracket is connected with rockers (5, 6). The shovel body and bracket are hinged with a reset spring (2). The hinge shaft is located between the former rocker and latter rocker. The bracket is hinged with a hinge shaft. The lifting oil jar is connected with a bracket.    USE - Cleaning shovel used in polishing machine (claimed).    ADVANTAGE - The cleaning shovel solves problem of manual control and complex operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cleaning shovel.    Shovel body (1)    Reset spring (2)    Lifting oil jar (3)    Bracket (4)    Rockers (5,6)    Machine body (7)
NOVELTY - Treatment of low-carbon kitchen waste involves dehydrating kitchen waste, crushing, cooling crushed material, then mixing with 5-15% yeast, carrying out fermentation process under supply of air, further carrying out anaerobic fermentation process, collecting carbon dioxide gas, deodorizing, washing, drying, liquefying and compressed into liquefied carbon dioxide, collecting the suspension on the surface of the fermented mash, water-washing, drying, transesterifying, water-washing and drying to obtain fatty acid ethyl ester.    USE - Treatment of low-carbon kitchen waste (claimed).    ADVANTAGE - The method enables efficient treatment of low-carbon kitchen waste by environmentally-friendly process.    DETAILED DESCRIPTION - Treatment of low-carbon kitchen waste involves dehydrating kitchen waste, crushing, cooling crushed material, then mixing with 5-15% yeast, carrying out fermentation process at 28-32 degrees C for 3 hours at rate of 100-300 rpm under supply of air, further carrying out anaerobic fermentation process at 28-32 degrees C for 36-60 minutes at rate of 0-50 rpm, collecting carbon dioxide gas, deodorizing, washing, drying, liquefying and compressed into liquefied carbon dioxide, collecting the suspension on the surface of the fermented mash, water-washing, drying under reduced pressure, transesterifying, water-washing and drying under reduced pressure to obtain fatty acid ethyl ester, distilling 95% (vol%/vol.%) ethanol from fermented slag, drying and granulating.
NOVELTY - Preparing seedling matrix, involves (a) crushing mushroom waste, (b) controlling moisture content of the obtained product, (c) piling up the obtained product in greenhouse and ventilating the greenhouse, (d) fermenting compost at 60-65 degrees C for 5-10 days, and turning up the compost once or twice a week, (e) continuously evaporating water from the compost, (e) subsequently fermenting, and airing the compost for 3-5 days, and (f) adding vermiculite and sustained-release granules to the obtained product, and turning the product for 2-3 times.    USE - The method is useful for preparing seedling matrix (claimed).    ADVANTAGE - The method is cost-effective, rapid and environmentally-friendly. The prepared seedling matrix supplies essential nutrients need for seedling, improves survival rate of seedling, shortens breeding period of the seedling, makes seedling root to be strong, and promotes rapid growth of the seedling. The seedlings are resistance to soil-borne diseases and insects and pests.    DETAILED DESCRIPTION - Method for preparing seedling matrix, involves (a) crushing mushroom waste to obtain particles having size of 0.2 mm or less, (b) controlling moisture content of the obtained product, (c) piling up the obtained product in greenhouse (pile at a height of 1.5 m and width of 2-3 m) and ventilating the greenhouse, (d) fermenting compost at 60-65 degrees C for 5-10 days, and turning up the compost once or twice a week, (e) continuously evaporating water from the compost, (e) subsequently fermenting at 35-40 degrees C for 25-30 days, and airing the compost for 3-5 days, and (f) adding 20-30 wt.% vermiculite and 1-3 wt.% sustained-release granules to the obtained product, and turning the product for 2-3 times.
NOVELTY - Organic fuel product comprises raw organic material including straw that is ground, cleaned to remove seeds, hammered and heated to a temperature of at least 110 degrees Fahrenheit to form a processed material; and manure mixed with the processed material, the mixture of the processed material and manure being ground and dried to an amount that is less than ten percent of the original moisture content of the straw. The dried mixture is compacted and compressed into a predetermined shape fuel product by a hydraulic press.    USE - The organic fuel product is useful for producing fuel logs, balls, blocks, bricks, briquettes, blanks, and/or pellets.    ADVANTAGE - Ecologically friendly and organically composed fuel products and fire starters are provided. The fuel products and fire starters are made from readily available natural resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for creating an organic fuel product from raw organic material, which involves placing straw in a first grinder for grinding; cleaning the ground straw by removing seeds; hammering the straw in a hammering process; heating the straw to a temperature of at least 110 degrees Fahrenheit; providing the straw to a second grinder for mixing and grinding; adding manure to the second grinder for mixing and grinding with the straw; providing the mixed and ground straw and manure to a tumble dryer for drying the straw and manure mixture to an amount that is less than ten percent of the original moisture content of the straw; and providing the intermixed straw and manure from the tumble dryer to a hydraulic press for compacting and compressing the intermixed straw and manure thus creating an organic fuel product.
NOVELTY - Preparing arformoterol L-(+)- tartrate (Ia), comprises reacting crude arformoterol (I) with D-(-)-tartaric acid to form arformoterol D-(-)-tartrate (II), and reacting (II) with a base and L-(+)-tartaric acid.    USE - (II) is useful for preparing arformoterol L-(+)- tartrate (Ia) (claimed).    ADVANTAGE - The process ensures simple, reproducible and robust preparation of desired polymorphic Form B of (Ia) with optimum yield, a chemical purity of at least 99% and a chiral purity of at least 99% and without using chromatographic purification techniques in an eco-friendly and economical manner.    DETAILED DESCRIPTION - Preparing arformoterol L-(+)- tartrate of formula (Ia), comprises reacting crude arformoterol of formula (I) with D-(-)-tartaric acid to form arformoterol D-(-)-tartrate of formula (II), and reacting (II) with a base and L-(+)-tartaric acid. The level of N-(2-hydroxy-5-(2-(((1R)-2-(4-methoxyphenyl)-1-methyl-ethyl)amino)ethyl)phenyl)formamide of formula (A1) or 2-amino-4-((1R)-1-hydroxy-2-(((1R)-2-(4-methoxyphenyl)-1-methyl-ethyl)amino)ethyl)phenol of formula (B1) is less than 0.15 wt.% relative to the amount of (I) as determined by HPLC.
NOVELTY - Producing lignocellulosic biomass comprises forming a paste by mixing wood powder, peat, molasses and a diluting liquid, drying the paste at 80-150 degrees C, and carbonizing the dried paste at 200-300 degrees C by pyrolysis process.    USE - The method is useful for producing lignocellulosic biomass (claimed), which is useful as a bio-fuel.    ADVANTAGE - The method is capable of economically and energy-efficiently producing the lignocellulosic biomass with high quality, reduced moisture content and improved calorific value.
NOVELTY - LTA-type zeolite is prepared from sodium hydroxide and sodium metasilicate, and sodium ion of LTA-type zeolite is replaced by an antimicrobial metal ion. A portion of antimicrobial metal ions is replaced by calcium ion, to obtain antimicrobial deodorizer.    USE - Manufacture of antimicrobial deodorizer. Uses include but are not limited to resin, coating material, fiber, leather, buildings, furniture and cosmetics.    ADVANTAGE - The method efficiently provides environmentally-friendly antimicrobial deodorizer having excellent absorption capacity. The antimicrobial deodorizer does not elute in water.
NOVELTY - A printed material e.g. newspaper, leaflet, magazine or pamphlet is impregnated with water, and taken out. The water in the material is removed, beaten and the material is molded into spherical shape to obtain solid fuel with reduced weight. Shredded plastic products e.g. fiber, film sheet, container and paraffin are introduced into heat-resistant container and liquefied, and the liquefied product is molded into spherical shape and dried in sun. The weight-reduced solid substance is entwined in air enclosure to obtain solid fuel.    USE - Manufacture of solid fuel (claimed) used for combustion appliances e.g. small coal stoves.    ADVANTAGE - The method economically provides solid fuel using a raw material procured from local supply and local consumption e.g. household consumption. The solid fuel is can be easily and efficiently used by elderly people and in industries. The manufacturing method is environmentally-friendly.
NOVELTY - Extracting (M1) a carotenoid from oil obtained from/as a byproduct derived from starch-containing material for producing fermentation products comprises: contacting the oil and/or the oil-containing byproduct with a solid adsorption material; separating the solid adsorption material containing the carotenoid; and extracting the carotenoid from the solid adsorption material.    USE - The method is useful for extracting a carotenoid from oil obtained from/as a byproduct derived from starch-containing material for producing fermentation products, where the carotenoid is beta -carotene or lutein (claimed).    ADVANTAGE - The method provides carotenoid extracted oil which is of higher quality and pureness and provides a cheap, pure corn oil for animal nutrition and food, cosmetics and healthcare, and provides biodiesel with improved yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) manufacturing (M2) an animal feed additive, comprising a carotenoid bound to a solid adsorption material, where the carotenoid is derived from oil obtained from/as a byproduct derived from starch-containing material for producing fermentation products, comprising contacting the oil with a solid adsorption material and separating the solid adsorption material containing the carotenoid;    (2) an animal feed additive comprising a carotenoid derived from oil obtained from a byproduct derived from starch-containing material in a process for producing fermentation products;    (3) extracting a carotenoid from oil obtained from/as a byproduct derived from starch-containing material for producing fermentation products comprising extracting the carotenoid with a solid adsorption material; and    (4) use of bentonite containing a carotenoid derived from oil obtained from/as a byproduct derived from starch-containing material for producing fermentation products as an animal feed ingredients.
NOVELTY - The device has a catalyzed combustion device (14) to which a circulation line (L4) is interposed at time of starting of a fuel cell (13) such that catalyzed combustion of exhausted fuel gas (11A) is carried out. An air supply line (L5) supplies air (12) to the exhausted fuel gas of the circulation line. An oxygen analyzer (20) is branched from the circulation line in a part of catalyzed combustion gas (16), and measures oxygen concentration in the combustion gas. A control apparatus (31) adjusts supply amount of oxygen introduced into the combustion device according to oxygen concentration.    USE - Device for starting a fuel cell i.e. solid oxide fuel cell (SOFC), utilized for an electric power generation system.    ADVANTAGE - The system measures oxygen-containing degree in catalyzed combustion gas by an oxygen analyzer to perform flow volume adjustment of the introduction amount of oxygen such that the catalyzed combustion gas of appropriate oxygen concentration is introduced in the fuel cell in case of temperature rise at time of fuel cell starting, so that catalyst deterioration of a fuel cell interior in the case of temperature rise at time of starting can be prevented, thus maintaining soundness at time of driving of a fuel cell system.    DETAILED DESCRIPTION - The exhausted fuel gas is LNG. An INDEPENDENT CLAIM is also included for a method for starting a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a starting device for a fuel cell.'(Drawing includes non-English language text)'    Circulation line (L4)    Air supply line (L5)    Exhausted fuel gas (11A)    Air (12)    Fuel cell (13)    Catalyzed combustion device (14)    Catalyzed combustion gas (16)    Oxygen analyzer (20)    Control apparatus (31)
NOVELTY - The method involves obtaining an insert material (A) in a low temperature gasifier (1) by smoldering carbonization gas (B). The carbonization gas is converted into synthesis gas (D) in a high temperature gasifier (2). Downstream of the high temperature gasifier and partial stream (13) of the synthesis gas are derived from derived gaseous mixture (E) and returned into the high temperature gasifier and/or to an output (221) of the high temperature gasifier in quenched gas streams (141, 142), where one of the quenched gas streams is returned into the high temperature gasifier.    USE - Method for partial gasification of a fixed organic insert material e.g. charcoal and biomass.    ADVANTAGE - The method enables returning the downstream of the high temperature gasifier and the partial stream of the synthesis gas into the high temperature gasifier and/or to the output of the high temperature gasifier in the quenched gas streams, thus reducing temperature at an exit of the high temperature gasifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for performing partial gasification of a fixed organic insert material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for performing partial gasification of a fixed organic insert material.    Insert material (A)    Carbonization gas (B)    Synthesis gas (D)    Gaseous mixture (E)    Low temperature gasifier (1)    High temperature gasifier (2)    Partial stream of synthesis gas (13)    Quenched gas streams (141, 142)    Output of high temperature gasifier (221)
NOVELTY - Method for partial gasification of solid organic feedstock involves carrying out low temperature carbonization by smoldering the feedstock in low temperature gasifier (1), to obtain carbonization gas (B), and charging carbonization gas (B) comprising fraction of synthesis gas (D) and/or gas mixture (E) derived by pressurizing, in high-temperature gasifier (2), and carrying out partial oxidation and partial reduction of carbonization gas (B) to form synthesis gas (D).    USE - Method for partial gasification of solid organic feedstock (claimed).    ADVANTAGE - The method enables stable partial gasification of solid organic feedstock, in which back flow of gases is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (10).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for partial gasification of solid organic feedstock.    Low temperature gasifier (1)    High temperature gasifier (2)    System (10)    Quench unit (21)    Oxidation unit (22)
NOVELTY - Microorganism comprising a genetic modification that increases a growth rate or biofuel production rate of the modified microorganism in the presence of a feedstock inhibitor compound relative to the growth rate or biofuel production rate of an unmodified microorganism, is new.    USE - The microorganism is useful for producing a biofuel, which is ethanol (all claimed), propanol, butanol or other alcohols.    ADVANTAGE - The microorganism has the genetic modification, which: increases a growth rate or biofuel production rate of modified microorganism relative to the growth rate or biofuel production rate of the unmodified microorganism; increases an expression or activity of a histidine kinase or ZMO1162 relative to the expression or activity level in the unmodified microorganism; decreases the expression or activity of a functional sigma -54 modulation protein, and functional protein encoded by ZMO0038 relative to the expression or activity level in the unmodified microorganism; abolishes the function of a protein encoded by ZMO0038 (all claimed); provides an enhanced tolerance to the inhibitor compound; and provides the biofuel with improved yield and purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a biofuel, comprising: culturing the microorganism with a feedstock under conditions, so that the microorganism ferments the feedstock into a biofuel; and isolating the biofuel from the culture.
NOVELTY - Method of converting solid biomass material involves contacting a feed (102) comprising solid biomass material and petroleum-derived hydrocarbon composition containing 7C-asphaltene content of 1 wt.% or more based on the total weight of the petroleum-derived hydrocarbon composition, co-currently with a source of hydrogen in ebullating bed reactor(s) comprising a catalyst at 350-500 degrees C.    USE - Method of converting solid biomass material into liquid fuel composition for spark-ignition engine and auto-ignition engine (claimed).    ADVANTAGE - The method efficiently and economically converts solid biomass material into fuel composition with high energy content, with reduced emission of carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition, which comprises hydrocarbon compounds having boiling point of 370 degrees C or more, fraction (a) comprising 1-99 wt.% biomass-derived hydrocarbon compounds and a fraction (b) comprising 1-99 wt.% petroleum derived hydrocarbon compounds.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the method of converting solid biomass material.    Feed (102)    Chopper (104)    Wood chips (106)    Torrefaction unit (108)    Torrefied solid biomass material (110)
NOVELTY - Hydrogenation of oxygen-containing organic products, comprises bringing the oxygen-containing organic products into contact with a catalyst in the presence of hydrogen gas at 200-5000 degrees C and at a pressure of 10-1000 bar. The catalyst comprises at least one metal component comprising cobalt, nickel, molybdenum or tungsten, and at least one non-metallic supplement component that is electrically conducting. The catalyst includes a mixture of particles of the metal component and the non-metallic supplement component.    USE - The process is useful for hydrogenation of oxygen-containing organic products (claimed) and/or oil refinery products, for producing bio-fuels.    ADVANTAGE - The process: utilizes the catalyst having enhanced performance and high thermal stability and which reduces the consumption of hydrogen; and provides higher yields of highly pure hydrocarbons.
NOVELTY - Method of biodiesel production is realised by the re-etherification in mixing natural oil, alcohol and a catalyst and following separation of the target product. The method is characterised by the fact that at the first stage of the re-etherification iron sulphate (II) is applied as the catalyst, after which iron sulphate and precipitated glycerol are separated and the mixture of alcohol, oil and ethers of fatty acids are supplied to the second stage of the re-etherification, at which as the catalyst used is an enzyme - lipase, immobilised on the surface, after which glycerol and the enzyme catalyst are separated and the mixture of alcohol and biodiesel is directed to a stage of the target product separation.    USE - Chemistry.    ADVANTAGE - Method makes it possible to simplify the process of the re-etherification reaction and increase the completeness of the reaction process.6 cl, 1 tbl
NOVELTY - Applied is a mechanic mixture of a thermally regenerated sorbent - carbon dioxide absorbent, which represents potassium carbonate, fixed in pores of titanium dioxide, and has the following composition: wt %: K2CO3 - 1-40, TiO2 - the remaining part to 100, and a photocatalyst for the process of methanation or reduction of a composition separated in the process of the carbon dioxide regeneration: wt %: Pt?^0.1-5 wt %, CdS?^5-20 wt %, TiO2 - the remaining part to 100, the content of the photocatalyst in the mixture constitutes 10-50 wt %.    USE - Chemistry.    ADVANTAGE - Method represents an energy effective method of obtaining methane from air carbon oxide, applies alternative renewable energy for the fuel synthesis.5 cl, 4 ex, 1 dwg
NOVELTY - The system has a burner controller (64) for igniting gas i.e. propane gas, entering a heating chamber (60). Transfer units (50, 52, 54, 56) extend into the heating chamber. A biochar cooler (71) is connected to a biochar collection chamber (70). An outlet drive shaft assembly (31) conveys biochar through the collection chamber and the biochar cooler. Biomass drive assemblies convey biomass through the transfer units. A syngas port (65) is positioned on the transfer units. A syngas return line (66) fluidly connects the syngas port with the burner controller.    USE - Mobile horizontal gasifier system for facilitating gasification of organic material for syngas, biochar and excess heat production application or electricity, fuel and energy production application.    ADVANTAGE - The system facilitates gasification of organic material to produce syngas, biochar and excess heat without creation of a large amount of ash. The system facilitates quarter of length of the transfer units to separate a feeder from the heating chamber so as to prevent accidental burning of the biomass stored within the feeder and a hopper by the heating chamber. The system includes components to be positioned on a mobile trailer with a hitch to allow the system to be easily transferred from one location to another location.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of a mobile horizontal gasifier system.    Outlet drive shaft assemblies (31, 40, 45, 49)    Transfer units (50, 52, 54, 56)    Heating chamber (60)    Burner controller (64)    Syngas port (65)    Syngas return line (66)    Biochar collection chamber (70)    Biochar cooler (71)
NOVELTY - A benzyloxy-substituted silane (I) and halogenated silicon are reacted in presence of a transition metal or its compound as catalyst.    USE - Manufacture of siloxane used for motor vehicle material, building material, electronic material, pharmaceuticals, sealing material for LED and silane coupling agent for environmentally-friendly tire.    ADVANTAGE - The method efficiently and economically provides siloxane having controllable structure. Catalyst is removed by easy operation and is recyclable.    DETAILED DESCRIPTION - A benzyloxy-substituted silane of formula: R4-nSi(OCH2Ph)n (I) and halogenated silicon are reacted in presence of a transition metal or its compound as catalyst.    Ph=phenyl;    n=1-4;and    R=H, 1-8C alkyl, 1-8C alkoxy, 3-7C cycloalkyl, aryl, aralkyl, acyl, hydroxy, halo, carboxy, or acyloxy, where one or more R combines with each other to form cyclic structure.
NOVELTY - Method for processing organic sludge, involves irradiating organic sludge with microwave, digesting the irradiated sludge, and processing the digested product.    USE - The method is useful for processing organic sludge (claimed) which is useful for producing methane.
NOVELTY - The method involves moving biomass i.e. annual plant biomass, between pairs of support plates (20) as the biomass flows gradually and continuously downward in a reactor vessel (10) from an upper level of the biomass to a bottom outlet, where convergence of each pair of plates is along a single direction of convergence. Compaction of the biomass is gradually increased as the biomass flows down between each pair of support plates. Some of the compressive forces on the biomass are rapidly released as the biomass flows past lower edges on each pair of support plates.    USE - Method for processing biomass i.e. annual plant biomass, in a reactor vessel to dissolve carbohydrates or lignin or other components of the biomass to produce pulp for paper making and other wood-based products, fuels or chemicals.    ADVANTAGE - The method enables change in the direction of the single-dimension convergence between the pairs of plates, thus preventing an accumulation repeatedly in the same region, and hence preventing excessive compression of the biomass within the vessel. The reduction in torque allows for a smaller and less expensive gearing and motor to drive the stirring device and reduces the energy needed to drive the stirring device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a reactor vessel along a vertical axis, including pairs of single convergence plates mounted internally in the vessel.    Reactor vessel (10)    Upper inlet (12)    Vertical axis (13)    Liquid inlet (14)    Support plates (20)
NOVELTY - The method involves setting pore diameter of a crystalline zeolite smaller than effective diameter of molecule that comprises carbon compound larger than effective diameter of a water molecule, where ammonia or hydrogen sulfide is contained as an offensive odor component whose effective diameter is smaller than the pore diameter of the crystalline zeolite in the carbon compound. The carbon compound is made to contact the crystalline zeolite until setting offensive odor component as a parameter of the residual ratio of the water molecule and stop detection of smell of odor component.    USE - Method for removing water molecule from carbon compound e.g. carbon dioxide, ethylene, ethane, methanol, ethanol, propylene, butadiene, propane and cyclic hydrocarbon (all claimed), for coolant and compressor oil used for a cooling cycle apparatus.    ADVANTAGE - The method enables making the carbon compound to contact the crystalline zeolite until setting offensive odor component as the parameter of the residual ratio of the water molecule and stop detection of smell of offensive odor component, so that the presence of offensive odor component of ammonia or hydrogen sulfide can be detected by a trace. The method enables making effective diameter of ammonia or hydrogen sulfide to be same as diameter of the water molecule, so that an offensive odor component is removed by absorption by the crystalline zeolite to a same extent as the water molecule, thus eliminating the water molecule in the liquid carbon compound effectively even when detection of the offensive odor component is stopped.    DETAILED DESCRIPTION - The pore diameter is 0.3 nanometer (nm).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water molecule removal apparatus.    Adsorption tank (1)    Piping (2)    Switching valve (3)
NOVELTY - The ecological wood is produced from biomass straw fiber of young babassu palm tree.    USE - Ecological wood used for producing caloric energy.    ADVANTAGE - The ecological wood efficiently replaces common firewood, charcoal and fossil fuels, reduces carbon dioxide emissions, enhances additional revenue for projects with carbon credits commercialization, and promotes generation and distribution of income in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic photograph of the plant's original format.
NOVELTY - Soilless vegetable growing media preparation involves mixing straw, mushroom residue, waste biogas, vermiculite, grass material and other raw materials to obtain a mixture, and maintaining humidity of the obtained mixture. Fertilizer and trace element are added to the mixture, and then filled in a block.    USE - Method for preparing soilless vegetable growing media (claimed).    ADVANTAGE - The method enables preparing soilless vegetable growing media in a cost-effective manner, where the soilless vegetable growing media has wide market prospect in agricultural market.
NOVELTY - A support component is laminated on one surface side of a porous film to obtain laminate. One or more layer of polymer layer having reversibly reactive material and acid gases is laminated on the porous film side of the laminate. The support component is peeled from the laminate, to obtain gas separation film. The gas separation film selectively permeates at least acidic gas.    USE - Manufacture of gas separation film used in manufacture of hydrogen, urea, and natural gas.    ADVANTAGE - The method efficiently produces gas separation film having high mechanical strength, with reduced elongation of the porous film during high-temperature drying, and stable conveyance of the laminate. The gas separation film selectively permeates at least acidic gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of laminate.
NOVELTY - A hydrogen generating apparatus comprises modifier (1) which generates fuel gas which contains hydrogen by reforming reaction with source gas and water containing hydrocarbon component, water supply machine (7) which supplies water to modifier, material supply device (5) which supplies source gas to modifier, combustor (12) which burns gas of source gas and fuel gas and heats the modifier, air supply device (13) which supplies combustion air to combustor, gas detector which detects gas of carbon monoxide and oxygen, and controller (16) which controls water supply machine by combustor.    USE - A hydrogen generating apparatus used for fuel cell system (claimed) for household use.    ADVANTAGE - Lifetime deterioration and decline in energy efficiency are prevented.    DETAILED DESCRIPTION - A hydrogen generating apparatus comprises modifier (1) which generates fuel gas which contains hydrogen by reforming reaction with source gas and water containing hydrocarbon component, water supply machine (7) which supplies water to modifier, material supply device (5) which supplies source gas to modifier, combustor (12) which burns gas of source gas and fuel gas and heats the modifier, air supply device (13) which supplies combustion air to combustor, gas detector which detects gas of carbon monoxide in combustion exhaust gas discharged from combustor, and oxygen, and controller (16) which controls water supply machine by combustor based on detection result of gas detector in case combustion is performed. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text).    Modifier (1)    Material supply device (5)    Water supply machine (7)    Combustor (12)    Air supply device (13)    Controller (16)
NOVELTY - A catalyst solution containing iron liquor is added with respect to charcoal obtained by carbonizing a timber, heated, and gasified while introducing water vapor to charcoal to obtain hydrogen.    USE - Production of hydrogen (claimed).    ADVANTAGE - The method provides highly-efficient hydrogen having excellent catalytic activity. The component of iron contained in iron liquor does not generate aggregation, and exists stably on the surface of charcoal, without enlarging the particle size of catalyst component.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of charcoal for producing hydrogen; and    (2) charcoal, which is obtained by carbonizing timber and catalyst solution.
NOVELTY - Method (M1) for preparing manure, involves mixing peat and rice bran, and fermenting mixture to obtain the product.    USE - The method (M1) is useful for preparing manure. The method (M2) is useful for preparing land improvement material. The method (M3) is useful for deodorizing sludge (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing land improvement material, involves performing the above-mentioned method (M1); and    (2) method (M3) for deodorizing sludge, involves performing the above-mentioned method (M1) and mixing fermented product with sludge.
NOVELTY - Method (M1) for producing biofuel using genetically modified iron-oxidizing bacteria (IOB), involves providing IOB that have been genetically modified to enable them to generate particular biofuel, feeding first source of ferrous iron to the IOB, feeding water, carbon dioxide and oxygen to the IOB, producing at least the biofuel, ferric iron, and IOB biomass, and preventing formation of ferric precipitates.    USE - The method (M1) and system are useful for producing biofuel, ferric iron, and IOB biomass. The method (M2) is useful for producing chemical compound (all claimed).    ADVANTAGE - The method is cost-effective, and consumes minimal energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for producing biofuels using genetically modified iron-oxidizing bacteria; and    (2) method (M2) for producing chemical compound using the genetically modified iron-oxidizing bacteria.
NOVELTY - Pull mat comprises a layer of straight unidirectional threads oriented in the longitudinal direction of the pull mat, and at least one layer of open material. The layer consists of a multitude of straight individual threads, which are placed essentially parallel to each other in a single plane. The straight unidirectional threads are spaced apart from each other, preferably at regular distances. At least one layer of open material is a woven fabric, a laid scrim, a nonwoven fabric or a perforated film.    USE - The pull mat is useful in tunnel composting and in mushroom cultivation (all claimed).    ADVANTAGE - The economical pull mat has high tensile strength, air permeability and resistance against elongation.    DETAILED DESCRIPTION - Pull mat comprises a layer of straight unidirectional threads oriented in the longitudinal direction of the pull mat, and at least one layer of open material. The layer consists of a multitude of straight individual threads, which are placed essentially parallel to each other in a single plane. The straight unidirectional threads are spaced apart from each other, preferably at regular distances. At least one layer of open material is a woven fabric, a laid scrim, a nonwoven fabric or a perforated film. The pull mat has an air permeability of at least 1200 I/m2 second, preferably at least 3000 I/m2 second, as determined according to ISO 9237-1995 at a pressure difference of 100 Pa.
NOVELTY - Method for producing glucose, involves using bodily waste of living organism.    USE - The method is useful for producing glucose (claimed) which is useful as bioethanol.    ADVANTAGE - The method is cost-effective, suitable for industrialization, and highly stable, and produces glucose from bodily waste of living organism which is usually disposed as waste material. The method produces glucose without utilizing food resource or agricultural resource, and produces glucose steadily and independently without using plants, as compared to existing method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for glucose, which is produced by the above-mentioned method.
NOVELTY - Recovery of a reformed gas produced in a methanol plant during startup involves a) decreasing the temperature of the methanol plant reformed gas (G1) comprising not greater than 2.5 wt.% of water, 1-8 wt.% of methane, hydrogen, nitrogen, carbon dioxide, and carbon monoxide, to remove at least some of the water from the reformed gas; and b) using the water removed reformed gas as fuel in a steam reformer.    USE - For recovery of a reformed gas produced in a methanol plant during startup (claimed).    ADVANTAGE - The recovery of reformed gas increases the production and reduces the venting to have a positive impact on environment. The method reduces venting of reformed gas which reduces waste, enhances plant productivity by using the reformed gas as a fuel during plant startup, while concurrently reducing the carbon footprint of plant operation. The total amount of natural gas saved by use of reformed gas as fuel is 6132 MMNTU/25 hours.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for recovery of a reformed gas (G1) produced in a methanol plant during startup comprising a closed loop line from a reformed gas flare stack line to a fuel line for a steam reformer, where the closed loop line comprises a heat exchanger, and where the heat exchanger cools the reformed gas.
NOVELTY - Recycling gas to heat hydrodesulfurization section involves recycling natural gas during a reformer startup in a methanol plant, where the natural gas is recycled from a point before entry into a natural gas saturator, and where the natural gas is recycled until the natural gas is heated to a desired temperature.    USE - The methods are useful for recycling gas to heat hydrodesulfurization section; and for recycling natural gas during reformer startup in methanol plant (all claimed).    ADVANTAGE - The process efficiently recycles natural gas instead of venting the natural gas to the flare system. It involves recycling of natural gas until the hydrodesulfurization section reaches the required temperature, increases overall plant efficiency, enhances production, saves significant amounts of natural gas, and reduces the carbon footprint of the plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for recycling natural gas during a reformer startup in a methanol plant which involves: (a) suctioning natural gas by a suction drum; (b) boosting natural gas by a natural gas booster downstream of the suction drum; (c) heating a steam reformer to heat a reformer feed gas downstream of the natural gas booster; (d) heating a hydrogenerator downstream of the steam reformer; (e) heating a sulfur adsorber downstream of the hydrogenerator; (f) recycling natural gas by a recirculation line downstream of the sulfur adsorber and upstream of the reformer; (g) cooling the recycled natural gas by a heat exchanger downstream of the sulfur adsorber; and (h) suctioning the cooled recycled natural gas into the suction drum downstream of the heat exchanger; where the natural gas is recycled until the reformer feed gas reaches a desired temperature.
NOVELTY - An alkaline substance is added into radioactive sludge containing radioactive substance, and heating the radioactive sludge. The radioactive sludge is dissolved in water by carrying out alkaline hydrolysis of the radioactive sludge, in order to obtain solubilized sludge. The solubilized sludge is subjected to solid-and-liquid separation process, in order to obtain the undissolved sludge as solid, and the separated liquid containing the radioactive substance and water, as liquid. The radioactive substance is removed from the separated liquid.    USE - Removal of radioactive substance used to remove cesium in soil.    ADVANTAGE - The method enables removal of radioactive substance, without burning the radioactive sludge containing radioactive substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for radioactive-substance removal apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure of the radioactive substance removal apparatus. (Drawing includes non-English language text)    Aerobic-treatment portion (1)    Sludge-disposal portion (2)    Solubilization process portion (3)    Solid-liquid separation portion (4)    Removal portion (5)
NOVELTY - Manufacture of drying oil involves removing particulate precipitate from waste cooking oil, removing moisture from waste cooking oil, forming unsaturated polymer by reacting unsaturated acid and secondary alcohol at 100 degrees C for 5 hours, mixing unsaturated polymer with waste cooking oil in ratio of 7.5:2.5 at 160 degrees C for 4 hours, cooling to 100 degrees C for 3 hours, heating the reaction mixture to 200 degrees C at heating rate of 10 degrees C/hour, adding 0.4 wt.% cobalt and 0.2 wt.% manganese to reaction mixture, heating to 250 degrees C, cooling and drying.    USE - Manufacture of drying oil (claimed).
NOVELTY - Compressed natural gas (CNG) automobile gas sensor module comprises resin-type filter, and gas sensor module comprising gas sensor for measuring the concentration of at least one of gas chosen from combustible gas and carbon dioxide, where the filter reduces dust and dirt from air pollutants, and prevents pollution of gas sensor in the gas sensor module.    USE - CNG automobile gas sensor module.    ADVANTAGE - The CNG automobile gas sensor module has filter in the gas sensor module, which reduces dust and dirt from air pollutants, easily separates the contaminant, extends lifetime of the gas sensor module and significantly reduces maintenance cost.
NOVELTY - A biomass of tobacco plants and subcritical water is provided to a reactor at a primary temperature. The biomass of tobacco plants is hydrolyzed with the subcritical water at primary temperature. A liquid product and a solid product are recovered from the reactor. The liquid product contains water-soluble sugars. Thus, fractionation of carbohydrates and lipids or oils in the tobacco plants is enabled.    USE - Fractionation of carbohydrates e.g. sugars and lipids or oils e.g. nicotine (all claimed) used for production of bioethanol, bio-based products and liquid fuels.    ADVANTAGE - The method enables fractionation of carbohydrates and lipids or oils using compact satellite-type reactor which can be installed in a field or near to the tobacco biomass source, without using chemicals. Freshly-cut tobacco biomass can be used to prepare feedstock for hydrolysis. Sugars and oil present in tobacco biomass can be phase separated after the hydrolysis.
NOVELTY - The apparatus (101) has a central enclosure (100) that is closed at the top having a gasification zone (1). An annular space of gasification zone is arranged with an inlet (6) on the outer wall (5) to receive air from an external blower or fan. A fuel inlet (9) is arranged for supplying fuel to the enclosure till the upper limit of gasification zone. A grate (10) is fixed below the gasification zone to hold the fuel. The valves are arranged at the bottom of gas collection zone (3) for the exit of producer gas. An ash collector (11) is arranged for the collection of ash.    USE - Combined draft apparatus for gasification of fuel such as bio-fuel (claimed) e.g. firewood, coal, refused derived fuel, rubber waste, leather waste, coconut husk, coconut shell, coconut fronds, mango seed, cow dung and powdery bio-fuel or agro-wastes in balled, briquetted or pellet form.    ADVANTAGE - The novel co-current gasifier whose linear design allows for compact modular design in order to accommodate a wide variety of energy demands for the single size product unit is provided. The heat and power are produced at all levels of industries from flexible conditions. The apparatus can handle optimum size, extreme moisture and high bulk density feedstock in proposition with low bulk density feed materials such as sugarcane trash, bagasse, cow dung and other agro waste materials in balled or briquetted forms. Hence high gasification efficiency is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing producer gas by gasification of fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined draft apparatus for gasification of fuel.    Gasification zone (1)    Gas collection zone (3)    Outer wall (5)    Inlet of annular space (6)    Fuel inlet (9)    Grate (10)    Ash collector (11)    Central enclosure (100)    Combined draft apparatus (101)
NOVELTY - Zinc sulfate solution production involves analyzing content of elements zinc, iron and contaminants in waste flue dust to be processed. The required stoichiometric amount is calculated to dissolve the present waste zinc in sulfuric acid. A sulfuric acid solution is prepared based on the mentioned stoichiometry in an amount calculated on the basis of the amount of residue. The sulfuric acid solution and residue of steelworks' dust under stirring in a reactor.    USE - Method for producing a zinc sulfate solution used as fertilizer or used for preparing fresh sulfuric acid solution (all claimed).    ADVANTAGE - The method produces commercial quality zinc sulfate solution by using zinc obtained from steelworks' dust in a simple and eco-friendly manner without generating wastewater and additional waste.    DETAILED DESCRIPTION - Zinc sulfate solution production involves analyzing content of elements zinc, iron and contaminants in waste flue dust to be processed. The required stoichiometric amount is calculated to dissolve the present waste zinc in sulfuric acid. A sulfuric acid solution is prepared based on the mentioned stoichiometry in an amount calculated on the basis of the amount of residue. The sulfuric acid solution and residue of steelworks' dust under stirring in a reactor. The resulting mixture is stirred at 65 degrees C to obtain desired final solution with 12% zinc. The obtained mixture is filtered, where the filtrate including 12% zinc sulfate concentration is stored as final product. The obtained solution is stirred for 8-12 minutes, where the final solid residue is placed for secondary treatment or disposal according to the standard rules of the local environment.
NOVELTY - A rubber composition contains 100 pts. wt. polystyrene, 0.05-5 pts. wt. crosslinking agent (A), 1-100 pts. wt. crosslinking agent (B), 0.01-10 pts. wt. peptizer, 0.1-10 pts. wt. accelerator and 1-200 pts. wt. inorganic additive.    USE - Rubber composition for manufacturing fuel cell gasket (all claimed).    ADVANTAGE - The rubber composition provides fuel cell gasket having excellent heat resistance, strength, abrasion resistance, solvent resistance and rigidity. The gasket is manufactured economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel cell gasket.
NOVELTY - The gasket (13) is comprised in a square shape or a cyclic form. A surface (13a) is contacted with a frame of an anode side, and the surface (13b) is contacted with frame of a cathode side. A slit portion (14) is provided over a perimeter of the gasket, and is opened toward an inner side. An edge of a diaphragm (17) is accommodated in the slit portion. A filling portion (16) is provided in an outer side of the slit portion. The diaphragm is not accommodated in the filling portion.    USE - Gasket built in alkaline-water-electrolysis tank, for use in electrolytic cell for electrolyzing electrolyte solution and obtaining oxygen and hydrogen (all claimed).    ADVANTAGE - Since the edge of the diaphragm is accommodated in the slit portion, and the end surface of the edge of the diaphragm is covered, the leakage of the electrolyte solution and gas from the end surface of the diaphragm is prevented. Since the diaphragm accommodated in the slit portion in the position corresponding to the protrusion portion is pressed by the gasket when the protrusion portion is pressed locally, the diaphragm is held firmly in the gasket. Since the protective film is provided in one portion of one surface and another surface, the corrosion of the gasket by the electrolyte solution and gas is suppressed. Hence the improvement in maintainability of the gasket is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the gasket.    Gasket (13)    Surfaces (13a,13b)    Slit portion (14)    Filling portion (16)    Diaphragm (17)
NOVELTY - The method involves biologically treating waste water stored in storage tank, while using pump apparatus for supplying waste water to biological treatment tank from storage tank. The first driving state which stops pump apparatus and aeration apparatus that is aerated to biological treatment tank, and second driving state which operates pump apparatus and aeration apparatus are carried out in switching manner (S4). The operation time is set to biologically treat waste water by predetermined BOD/SS load when BOD/SS load of inflow waste water is lower than predetermined BOD/SS load.    USE - Sewage disposal plant-operation method.    ADVANTAGE - The waste water is biologically treated with sufficient energy efficiency even if BOD/SS load is lower than plan value. The microorganism flora of an activated sludge is induced to make a soil microbe superior for a short period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) the sewage disposal plant-operation control apparatus; and    (2) the sewage plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the control process of sewage disposal plant. (Drawing includes non-English language text)    Step for getting BOD of the amount of target sewage disposals (S1)    Step for computing BOD/SS load (S2)    Step for scheduling the operation time (S3)    Step for carrying out switching of driving states (S4)    Step for determining whether driving state is first driving state or second driving state (S5)
NOVELTY - Production of volatile short-chain fatty acid (VSCFA) of palm sludge oil (PSO) derived from palm oil mill effluent (POME) involves washing off sap of PSO using acid(s), decolorizing washed sap using bleaching lye(s) and distilling the sap under vacuum conditions to obtain volatile short-chain fatty acid.    USE - Production of volatile short-chain fatty acid used for production of volatile short-chain fatty acid ester. The palm sludge oil is used for producing biodiesel (all claimed).    ADVANTAGE - The biodiesel is economically produced during production of volatile short-chain fatty acid from palm sludge oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of VSCFA ester, which involves adding short-chain alcohol into VSCFA, adding an acid catalyst in alcohol-VSCFA mixture, refluxing the mixture at 60-80 degrees C, washing the mixture using solution (S1) which does not react, and distilling VSCFA ester. The solution (S1) is water; and    (2) process of converting refined PSO into biodiesel, which involves esterifying free fatty acid in PSO along with solid acid catalyst dissolved in alcohol, separating glycerol, contaminant and/or soap, neutralizing obtained esterified product by adding alkaline and solution (S2) which does not react, drying esterified product, transesterifying esterified PSO with alkaline catalyst and alcohol, and washing and drying obtained PSO ester. The solution (S2) is warm water.
NOVELTY - Granular fertilizer comprises a granular fertilizer core, a first coating layer made of a first coating composition and formed on a surface of the core, a second coating layer made of a second coating composition and formed on the first coating layer, and a third coating layer made of a third coating composition and formed on the second coating layer. The first and second coating compositions include an acrylic polymer. The third composition includes an acrylic polymer and a hydrophilic material.    USE - The granular fertilizer is useful for rice farming operations.    ADVANTAGE - The environmentally friendly granular fertilizer reduces river or groundwater contamination and sheath during farming the rice, and improves nutrient content and quality of the rice.    DETAILED DESCRIPTION - Granular fertilizer comprises a granular fertilizer core, a first coating layer made of a first coating composition and formed on a surface of the core, a second coating layer made of a second coating composition and formed on the first coating layer, and a third coating layer made of a third coating composition and formed on the second coating layer. The first and second coating compositions include an acrylic polymer. The third composition includes an acrylic polymer and a hydrophilic material. The second coating composition has a glass transition temperature that is higher than that of the first coating composition. An INDEPENDENT CLAIM is included for preparing granular fertilizer, comprising: forming the first coating layer on the surface of the core; forming the second coating layer on the first coating layer; forming the third coating layer on the first and second coating layers; and drying the first, second and third coating layers by heat treatment to obtain the granular fertilizer.
NOVELTY - The electrolyzer (1) has electrolysis board (5) that is provided with a pair of electrode plate (500) provided with an anode plate (501) and a cathode plate (502). A liquid absorption portion (4) is adhered to each surface of the anode plate and the cathode plate. An electrolytic cell (6) is provided to store to-be-electrolyzed liquid (13) absorbed by the liquid absorption portion.    USE - Portable electrolyzer for electrolyzing to-be-electrolyzed liquid of pure water for physics and chemistry experimental and clinical testing, etc., used in general household.    ADVANTAGE - Electrolyzer prevents malfunction, and efficient discharge of generated gas is ensured, and size reduction is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the electrolytic cell.    Portable electrolyzer (1)    Liquid absorption portion (4)    Electrolysis board (5)    Electrolytic cell (6)    To-be-electrolyzed liquid (13)    Electrode plate (500)    Anode plate (501)    Cathode plate (502)
NOVELTY - The organic refuse processor has a multiple screws which are positioned in parallel and rotated in direction opposite to a next portion. An insertion opening is located above the screw. A discharge port is located in end of the screw. A pair of inclined surface is provided in both-ends of the screw, and is inclined forward toward the screw. A blade is provided in surroundings of a screw shaft. A weight measurement unit is provided to measure weight of contents in a processing tank. The weight measurement unit is provided between the processing tank and a frame.    USE - Organic refuse processor for fermenting organic refuse.    ADVANTAGE - Since the pair of inclined surface is provided in both-ends of the screw, the fermentation of organic refuse is accelerated effectively in reliable manner. The wastefulness of energy which works the organic refuse processor is eliminated. The inside of the processing tank is maintained for activity of microorganisms. The product cost of the organic refuse processor is reduced.
NOVELTY - The reformer (2) has a cover (10,74) that is set up in an upper end portion of a sub tank (8). A collection tank (68) for solid constituent collection is connected to a rotating pipe (40). The rotating pipe is established in a table (6). An end box (44) and cover are set up in a line of rotating pipe. A back-end path is shut tightly. An exit (72) of the collection tank is connected to end box. The cover fixes rocker (12,76) after keeping airtight. The solid constituent movement route from sub tank to collection tank is maintained in vacuum condition.    USE - Reformer for biomass waste.    ADVANTAGE - The moving line of the solid constituent telling to the collection tank in the vacuum condition is prevented from being contacted with the outside air. Thus the high quality synthetic gas production is realized. The synthetic gas production efficiency is conspicuously improved with the manufacturing cost reduction of the facility according to the simplification of the structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reformer. (Drawing includes non-English language text)    Reformer (2)    Table (6)    Sub tank (8)    Covers (10,74)    Rockers (12,76)    Rotating pipe (40)    End box (44)    Collection tank (68)    Exit of collection tank (72)
NOVELTY - A pyrimidine derivative (VI), is new.    USE - New pyrimidine derivative is used for preparing ticagrelor (claimed).    ADVANTAGE - The ticagrelor is prepared with high productivity by simple and environmentally-friendly process using the pyrimidine derivative with reduced energy consumption.    DETAILED DESCRIPTION - A pyrimidine derivative of formula (VI), is new.    R=H or hydroxy protection group chosen from trimethylsilyl, triethylsilyl, triisopropylsilyl, tert-butyl dimethylsilyl, tert-butyl diphenylsilyl, methoxymethyl, tetrahydropyranyl or tetrahydrofuranyl.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of pyrimidine derivative (VI);    (2) N-(4,6-dichloro-2-(propylsulfanyl)pyrimidin-5-yl)-2,2,2-trifluoroacetamide; and    (3) preparation of ticagrelor, which involves preparing pyrimidine derivative (VI), and preparing ticagrelor by using pyrimidine derivative (VI).
NOVELTY - The wastewater treatment facility has a biofilm filtration aquarium (10) with a bio-filter that is provided for performing nitrification of processing water, such that the solid material and organic compound of foul water are removed. The denitrification and dephosphorization are successively performed in the biofilm filtration aquarium. A photosynthesis/nitrification basin (30) is provided for cultivating the microalgae so that the impaction is performed. A settling tank (40) is provided for separating sludge of processing water handled at photosynthesis/nitrification basin.    USE - Wastewater treatment facility.    ADVANTAGE - The disintegration of organic matter is removed and the denitrification of the organic material is facilitated. The processing efficiency of wastewater treatment facility is improved. The need for providing supplementary facilities according to the oxygenation and processing function is drastically reduced, so that the facility and maintenance cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the energy saving-type wastewater treatment facility. (Drawing includes non-English language text)    Biofilm filtration aquarium (10)    Anoxic filtration membrane unit (11)    Anaerobic tank (20)    Photosynthesis/nitrification basin (30)    Settling tank (40)
NOVELTY - The apparatus has photosynthesis unit (20) for culturing the microalgae, and nitrification basin (30) that is segmented by upper and lower sections by partition wall (31), so that microalgae is cultivated by nitrification and organic oxidation of processing water. A bio-filter is formed in bio-film filtration aquarium (10), so that solid material and organic compound of foul water are removed while maintaining the anoxic condition. A flow carrier (36) is filled in nitrification unit (35) formed at lower section, so that sludge of settling tank (40) is returned to photosynthesis unit.    USE - Waste water treatment apparatus using microalgae.    ADVANTAGE - The waste water treatment efficiency is improved by nitrification microorganism sticking process and heterophile bacterium growth while growing microorganism in generated oxygen in flow carrier. The oxygenation and processing function is drastically reduced and the maintenance cost is reduced. The inflow of suspended solids is cut off and the turbid matter is removed.    DETAILED DESCRIPTION - The average mixed liquor suspended solid (MLSS) of photosynthesis unit is maintained. The biofilm filtration aquarium comprises diffuser in the upper section for the oxidation of residual organic matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the waste water treatment facility. (Drawing includes non-English language text)    Bio-film filtration aquarium (10)    Photosynthesis unit (20)    Nitrification basin (30)    Partition wall (31)    Nitrification unit (35)    Flow carrier (36)    Settling tank (40)
NOVELTY - The apparatus (100) has multiple discharge holes that are formed in the outer periphery of discharge pipe (400) which is installed at the fermenter (200) of bottom surface of the fermentation space. A mixing unit (300) is installed in the fermenter and mixes the excrements to the fermentation space. A vertical tube (502) is provided in the upper direction of the manifold which is installed in the discharge pipe. A supply element (504) is provided for supplying oxygen to the horizontal tubes.    USE - Fermentation apparatus for liquid manure.    ADVANTAGE - The oxygen to the fluid excrements is easily supplied and is easily filled with the fermentation space and activates the microorganism for the aerobic fermentation within the excrements in a short time.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the fermentation apparatus for liquid manure.    Fermentation apparatus for liquid manure (100)    Fermenter (200)    Mixing unit (300)    Discharge pipe (400)    Vertical tube (502)    Supply element (504)
NOVELTY - Method for preparing protein feed, involves sonicating blood collected from slaughter house (pre-treatment), adding enzyme to the sonicated blood, carrying out solid-liquid separation, and drying the obtained product.    USE - The method is useful for preparing feed. The method is also useful for preparing liquid fertilizer (claimed).
NOVELTY - Method for performing synthesis silver nanoparticles using Barleria prionitis leaf extract (BPLE), involves providing 5 g B.prionitis leaf powder, immersing the B.prionitis leaf powder in 100 ml distilled water for 10 minutes, boiling for 10 minutes, centrifuging at 1000 revolutions/minute (rpm) for 15 minutes and filtering the prepared extract, performing bio-reduction of silver nitrate using the extract and monitoring the synthesis of silver nanoparticles by measuring UV-Vis spectra.    USE - The method is useful for performing synthesis silver nanoparticles using BPLE (claimed) which is used to determine antimicrobial and antibiofilm activity.    ADVANTAGE - The method is performed rapidly, cost-effectively and environmentally-friendly.
NOVELTY - Hydrogenation of imines involves contacting imine with hydrogen under pressure of 20-100 bar in the presence of a catalyst system comprising iridium-xyliphos ligands immobilized on alumina and a heteropolyacid.    USE - For hydrogenation of imines (e.g. (2-ethyl-6-methyl-phenyl)-(2-methoxy-1-methyl-eth-(Z)-ylidene)-amine) to obtain amines (e.g. (S)-N-(2-ethyl-6-methyl-phenyl)-N-(1-methoxymethyl)ethylamine) which are used for the preparation of 2-chloro-N-phenyl-acetamide compounds (claimed), particularly S-metolachlor that are useful as herbicide.    ADVANTAGE - The use of alumina and a heteropoly acid forms a covalent bond by anchoring to the catalyst thus immobilizing the catalyst. Such anchoring results in a high yield of the catalyst system and prevents leaching of the catalyst in the reaction solvent and thus rendering the overall process environment friendly, cost effective and economical. This helps in the improved recovery and recycling of the catalyst on repeated usage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) asymmetric hydrogenation (m2) of an imine of formula (II) involving contacting the imine (II) with hydrogen under pressure of 20-100 bar in the presence of a catalyst system comprising iridium-xyliphos ligands immobilized on alumina and a heteropolyacid to obtain an amine of formula (III);    (2) preparation (p2) of 2-chloro-N-phenyl-acetamide compounds of formula (I) involving either performing the method (m2) to obtain the amine (III), and reacting the amine (III) with chloroacetylchloride in the presence of a base in a non-polar solvent at 0-5 degrees C; or reacting aniline compound of formula (IV) with a ketone of formula R4-C(O)-R5 to obtain the compound (II), performing the method (m2) to obtain the amine (III) and reacting the amine (III) with chloroacetyl chloride in the presence of a base.    R1 to R4=H or 1-4C alkyl;    R5=H, 1-4C alkyl or CH2OCH3 (disclosed).
NOVELTY - A hydrogen source auxiliary system utilizes electrolytic water to produce hydrogen, and supplies the hydrogen to a device capable of using hydrogen source, so as to replace partial petrochemical energy with hydrogen, thus reducing the consumption of the petrochemical energy. In addition, between the device capable of using hydrogen source and a hydrogen discharging outlet is provided a check valve for preventing the hydrogen from combusting abnormally or blasting, improving the operational safety.
NOVELTY - This utility new type relates to a biomass activate one furnace, belonging to the biomass carbonizing activate device technology field. Technology solution is as follows: in a part set in an annular furnace body (6), a furnace body (11) of side wall is set with an annular side (7), the upper part of the centre and heat storage room and the annular side heat storage room in a heat storage room in annular ring is raw material bin (1), a space between the center and the heat storage room and the annular side heat storage room in a heat storage room in annular ring is burning room, heat storing room and an annular side heat storage room in the annular side wall upper part set with a middle smoke channel (2), and the side wall lower part set with steam pipeline (8), the bottom of the burning room set with spiral discharging device (5), a spiral discharging device (5) through exhaust valve (9), a smoke outlet (10). This utility new type carbonizing, gasifying, activate the process step is finished, high efficiency, short period, quality, continuous production, productivity is increased, reduce the production cost and save valid yield a using unit of energy.
NOVELTY - The device has a pneumatic mixing tank (5) connected with a hollow fiber membrane module (4) that is fixed with an air inlet tube (2). The air inlet tube is connected with an air compressor (1) and a vent valve (3). The pneumatic mixing tank is fixed with water inlet tubes (7, 8). An output water pump (10) is fixed with a water output tube valve (11). A filler (17) is formed with a sludge reaction area (16) and fixed with a perforated pipe (12). Spraying tubes (24, 25, 27) are fixed with the water output tube valve. A discharging tube (31) is fixed with a discharging valve (30).    USE - Bubble-free aeration pretreated composite biological deodorizing device.    ADVANTAGE - The device can reduce pollution and working area in an efficient manner, improves processing efficiency and removes bad deodorization effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bubble-free aeration pretreated composite biological deodorizing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a bubble-free aeration pretreated composite biological deodorizing device. '(Drawing includes non-English language text)'    Air compressor (1)    Air inlet tube (2)    Vent valve (3)    Hollow fiber membrane module (4)    Pneumatic mixing tank (5)    Water inlet tubes (7, 8)    Output water pump (10)    Water output tube valve (11)    Perforated pipe (12)    Sludge reaction area (16)    Filler (17)    Spraying tubes (24, 25, 27)    Discharging valve (30)    Discharging tube (31)
NOVELTY - Carbon dioxide generator comprises a vessel (4), where the vessel is filled with carbon dioxide (5). The vessel is set up with a temperature control unit (3). Carbon dioxide generator comprises a plant growth lamp and a shell, where the plant growth lamp comprises a light-emitting diode (LED) lamp body (1). The LED lamp body is set with a carbon dioxide generator (2). The LED lamp body and carbon dioxide are in the inner shell.    USE - Carbon dioxide generator.    ADVANTAGE - The carbon dioxide generator is energy-saving and eco-friendly, and reduces the energy consumption, manufacturing cost and material resources cost, and avoids continuously adding of fuel by manpower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a carbon dioxide generator.    LED lamp body (1)    Carbon dioxide generator (2)    Temperature control unit (3)    Vessel (4)    Carbon dioxide (5)
NOVELTY - Fertilizer composition comprises ethylene diamine o-hydroxyphenylacetic acid with iron, chelated zinc fertilizer, zinc and titanium salts of ethylenediaminetetraacetic acid, accelerating agent and microelement.    USE - Fertilizer composition used for soil planting of pear tree leaf (claimed).    ADVANTAGE - The fertilizer composition has surfactant that reduces surface tension, increases the spreadability and wettability of fertilizer composition. The fertilizer composition improves the nutrition of crops, yield and fruit quality.
NOVELTY - Biological fertilizer composition preparation involves mixing humus (70-75 wt.%), clover biogas liquid (10-20wt.%), plant extract (4-8wt.%) and additive (10-15wt.%), where plant extract is neem, vetch or unbracteolated spurge root. The obtained material is dried,and then performed for microbial fermentation. The obtained material is dried. The obtained material is mixed with hydrochloric acid solution, and then the obtained material is neutralized. The obtained material is filtered, evaporated, and then crystallized. The obtained crystals are dried to obtain the finished product.    USE - Method for preparing biological fertilizer composition, which is used for promoting Medicago sativa growth (claimed).    ADVANTAGE - The method enables to prepare biological fertilizer composition, which has special pesticide property and shows improved yield.
NOVELTY - Ammonia nitrogen is removed by preparing nutrient solution containing ammonium chloride, sodium bicarbonate, ferric chloride, magnesium chloride, phosphoric acid, and sodium oxalate, preparing culture liquid containing biological strain, culturing culture liquid at greater than or equal to 15 degrees C with pH of 7.5-8.5 and dissolved oxygen content of 2 mg/L for greater than or equal to 5 days to obtain sludge with biochemical oxygen demand (BOD) of less than or equal to 15 mg/L, and adding nitrified sludge to main sewage treatment system.    USE - Removal of ammonia nitrogen for sewage treatment plant (claimed).    ADVANTAGE - Removal of ammonia nitrogen reduces sewage treatment operation cost and enhances nitrification capacity of sewage treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the removal of ammonia nitrogen. (Drawing includes non-English language text).
NOVELTY - Fermentation device comprises a fermentation system, a monitoring system, a ventilation system, a heat preservation system and an insulation system. The fermentation system and monitoring system are connected. The fermentation system comprises a fermenting room (1), a sampling port (2), a discharge hole (3), an inner cylinder (4), an outer cylinder (5), an insulating layer (6), a flange seal heat preservation cover (7), a feeding port (8), perspective holes (9), a bracket (23) and a fixing nut (24). The inner cylinder is placed in the outer cylinder.    USE - Fermentation device used for composting manure and livestock excrement (claimed).    ADVANTAGE - The fermentation device increases rotten degree, quick-acting nutrient conversion rate and count, and shortens fermentation period.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for composting manure using a fermentation device, which involves:    (A) mixing livestock excrement, additives and strain, where the strain is selected from Bacillus subtilis, Streptomyces microflavus, Trichoderma longbrachiatum and Bacillus mucilaginosus; and    (B) fermenting the mixed material to obtain the desired product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation device.    Fermenting room (1)    Sampling port (2)    Discharge hole (3)    Inner cylinder (4)    Outer cylinder (5)    Insulating layer (6)    Flange seal heat preservation cover (7)    Feeding port (8)    Perspective holes (9)    Bracket (23)    Fixing nut (24)
NOVELTY - Aerobic fermentation device comprises a reaction chamber with a stirrer, a cooling water circulation, a condensation water collecting system, an air heating and ventilation system with function of deodorization, and a water bath heating and heat preservation system with remote monitoring of the intelligent control system. The fermentation device comprises a speed reducer (1), a rotating shaft (2), a stir paddle (3), a heat preservation interlayer (4), a water bath receptor (5), an air distributing tube (26), a cooling water tube (29) and a condensed water collecting tube (30).    USE - Aerobic fermentation device used for drying kitchen garbage (claimed).    ADVANTAGE - The aerobic fermentation device has reduced energy consumption, and has improved treatment effect with simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an aerobic fermentation device.    Speed reducer (1)    Rotating shaft (2)    Stir paddle (3)    Heat preservation interlayer (4)    Water bath receptor (5)    Air distributing tube (26)    Cooling water tube (29)    Condensed water collecting tube (30)
NOVELTY - Double lifting machine comprises a walking machine frame, a sliding rack and a lifting system, where the walking machine frame comprises a baffle (1), a horizontal machine frame (2), a vertical rack (4), a walking motor (9) and a walking wheel (10). The sliding rack and lifting system comprises a pump station (8), a screw mandrel (5), a lead screw motor (7), a worm (6) and a pulley (11). The machine lifting system comprises a motor (12), a lifting oil jar (13), a sliding frame (14), plates (16) and a reinforcing rib (17). The vertical rack and the horizontal machine frame are welded together.    USE - Double lifting machine.    ADVANTAGE - The double lifting machine is automatic, simple, cost-effective, and easy to operate. The double lifting machine has reduced malfunction rate with simple maintenance and low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a double lifting machine.    Baffle (1)    Horizontal machine frame (2)    Vertical rack (4)    Screw mandrel (5)    Worm (6)    Lead screw motor (7)    Pump station (8)    Walking motor (9)    Walking wheel (10)    Pulley (11)    Motor (12)    Lifting oil jar (13)    Sliding frame (14)    Plates (16)    Reinforcing rib (17)
NOVELTY - Corn straw waste degradation involves grinding corn straw, and mixing the obtained material with adjuvants. The straw degrading microbial strain is inoculated, where the moisture content is 60-80%. The inoculated material is processed at 20-30 degrees C.    USE - Method for degrading corn straw waste (claimed).    ADVANTAGE - The method promotes cellulase activity and xylanase enzyme activity, and increases degradion of corn straw.
NOVELTY - Organic fertilizer preparation involves removing shedding plants and weeds from plant. The obtained material is ground. The obtained plant part and chicken manure are mixed in the weight ratio of 1:1. The mixed material is added with mixed carbon and nitrogen in the ratio of 2-29:1. Water is added to the obtained material, where the water content is 58-62%. The obtained compost is fermented, and then stacked for 3 days, where the bottom diameter is 80-90 centimeter. The obtained material is fermented at 72-80 degrees C for 16-20 days, and then cooled naturally to ambient temperature.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to produce the organic fertilizer that has improved quality, content of potassium oxide and germination index.    DETAILED DESCRIPTION - Organic fertilizer preparation involves removing shedding plants and weeds from plant. The obtained material is ground. The obtained plant part and chicken manure are mixed in the weight ratio of 1:1. The mixed material is added with mixed carbon and nitrogen in the ratio of 2-29:1. Water is added to the obtained material, where the water content is 58-62%. The obtained compost is fermented, and then stacked for 3 days, where the bottom diameter is 80-90 centimeter. The obtained material is fermented at 72-80 degrees C for 16-20 days, and then cooled naturally to ambient temperature. The obtained compost is dried, and then crushed to obtain organic fertilizer.
NOVELTY - Composite microbial fertilizer composition comprises (in pts.wt.): urea (28.71), bran (12.84), chitosan (1.07), composite microbial inoculum (3.85), furfural residue (16.35), ammonium sulfate (15.48), potassium sulfate (12.54), mono-ammonium phosphate (16.23), rape seed (5.37), manure (8.46), humic acid (3.13), sesame rice bran (2.54), trace element (0.41) and microelement (6.81).    USE - Composite microbial fertilizer composition used fro preventing andtreating the diseases of corn (claimed).    ADVANTAGE - The composite microbial fertilizer composition shows improved fertilizer efficiency and yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing composite microbial inoculum, which involves inoculating Bacillus laterosporus, Actinomycetes and multi-adhesive bud spore in liquid culture medium, and then fermenting the obtained material in fermentation culture medium; and    (2) a method for preparing composite microbial fertilizer composition, which involves mixing raw materials uniformly to obtain fertilizer water solution, and then adding 3.85 parts of composite microbial inoculum to the obtained material; stacking and fermenting the obtained material at 37 degrees C for 2-3 days to obtain the finished product.
NOVELTY - Biological organic fertilizer preparation involves crushing wood waste and grass plant waste. The obtained material is dried naturally for 15-20 days. The obtained material is carbonized, and then crushed the obtained material. Microorganism is added to the obtained material, and then the obtained material is stirred uniformly with clean water to prepare stack body. The obtained material is dried at 60-70 degrees C. The obtained material is fermented for 15-20 days, and then the obtained material is dried. The obtained material is mixed with biological carbon to obtain the finished product.    USE - Method for preparing biological organic fertilizer from garden plant waste (claimed).    ADVANTAGE - The method enables to prepare biological organic fertilizer, which is rich in biological carbon.
NOVELTY - Preparing blueberry special liquid fertilizer comprises (i) preparing effective microorganism (EM) bacteria solution comprising EM complex flora, (ii) preparing trace element solution containing at least one trace element, or compound or composition of microelement, (iii) preparing plant organic nutrition solution comprising at least one vitamin, or amino acid, and (iv) preparing liquid fertilizer: mixing EM bacterial solution, trace element solution, and plant organic nutrition solution, stirring, vacuum filtering, and filtering to obtain the liquid fertilizer.    USE - The method is useful for preparing blueberry special liquid fertilizer (claimed).    ADVANTAGE - The fertilizer is convenient to use, has obvious effect, prevents disease, increases and enhances the stress resistance, and is suitable for spraying, irrigation and drip irrigation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for blueberry special liquid fertilizer, prepared according to the above mentioned method.
NOVELTY - Flower organic fertilizer comprises 15-25 wt.% vegetable oil cake, 8-15 wt.% dairy manure, 25-35 wt.% pine needle soil, 8-15 wt.% phosphate powder, 20-30 wt.% traditional Chinese medicine residue, and 4-6 wt.% biological bacteria. The preparation of flower organic fertilizer comprises mixing vegetable oil cake, dairy manure, pine needle soil and traditional Chinese medicine residue to obtain mixed raw material, then adding biological bacteria, mixing, maintaining moisture at 50-55%, and fermenting.    USE - Used as a flower organic fertilizer.    ADVANTAGE - The fertilizer shortens the growth period of a flower, produces sufficient nutrient and prevents insect pests.    DETAILED DESCRIPTION - Flower organic fertilizer comprises 15-25 wt.% vegetable oil cake, 8-15 wt.% dairy manure, 25-35 wt.% pine needle soil, 8-15 wt.% phosphate powder, 20-30 wt.% traditional Chinese medicine residue, and 4-6 wt.% biological bacteria. The preparation of flower organic fertilizer comprises mixing vegetable oil cake, dairy manure, pine needle soil and traditional Chinese medicine residue to obtain mixed raw material, then adding biological bacteria, mixing, maintaining moisture at 50-55%, fermenting for 10 days by turning, and passing into turn plate fermentation tower and fermenting for 12 days; carrying out aerobic fermentation of mixed fermented vegetable oil cake, dairy manure, pine needle soil and traditional Chinese medicine residue, maintaining moisture to 25%, so that no odor is released, and releasing from the fermentation tower; mixing the fermented mixture with phosphate powder; then crushing, screening, inspecting, granulating into powder.
NOVELTY - Organic fertilizer comprises 15-20 parts by weight (pts. wt.) vegetable oil cake, 35-45 pts. wt. quail manure, 8-12 pts. wt. dairy manure, 8-12 pts. wt. chicken manure, 8-12 pts. wt. calcium magnesium phosphate, 8-12 pts. wt. traditional Chinese medicine slag, and 2-4 pts. wt. biological bacteria.    USE - As organic fertilizer for sorghum (claimed).    ADVANTAGE - The organic fertilizer increases disaster of high disease resistance and immunity of sorghum, fertility is more durable, effective regulation of the body's ability to resist plant, increases production, and improves crop quality.    DETAILED DESCRIPTION - Organic fertilizer for sorghum comprises 15-20 parts by weight (pts. wt.) vegetable oil cake, 35-45 pts. wt. quail manure, 8-12 pts. wt. dairy manure, 8-12 pts. wt. chicken manure, 8-12 pts. wt. calcium magnesium phosphate, 8-12 pts. wt. traditional Chinese medicine slag, and 2-4 pts. wt. biological bacteria, and is prepared by mixing the vegetable oil cake, quail manure, dairy manure, chicken manure, calciummagnesia phosphate fertilizer, traditional Chinese medicine dregs raw materials according to corresponding ratio mix, mixing raw material in a corresponding proportion of adding biological strain, stirring uniformly, water holding at 50-55 degrees C, stacking to ferment for 10 days, entering into fermentation tower to ferment for 12 days, turning plate through aerobic fermentation ferment, mixing vegetable oil cake, quail manure, dairy manure, chicken manure, calcium-magnesia phosphate fertilizer, fermenting, traditional Chinese medicine dregs water content is 25%, which is obviously to feel without odor of a tower inner is put out from the fermentation, crushing, sieving, checking, at last, granulating or powder, sorghum special fertilizer to obtain Organic fertilizer.
NOVELTY - Synthesis of losartan biphenyl involves carrying out Friedel-Crafts acylation reaction using p-toluidine and benzoyl chloride as raw materials under Lewis acid catalyzed conditions, adding diazonium salt, benzene and precipitated sodium nitrite, carrying out ring-opening process under alkaline conditions, obtaining 2-(4-methylphenyl)benzoic acid as main product, and 5-methyl-2-phenylbenzoic acid as by-product, separating ring-opened product as salt, and converting carboxyl group into cyano group.    USE - Synthesis of losartan biphenyl (claimed).    ADVANTAGE - The method enables economical, safe, easy and environmentally-friendly synthesis of losartan biphenyl, and provides recyclable by-products.
NOVELTY - Hollow copper sulfide/polypyrrole nanocomposite with peroxide enzyme activity, is claimed.    USE - The nanocomposite is useful: for producing strong oxidizing hydroxyl free radical hydrogen peroxide, detecting glucose content in food and blood and oxidative degradation of organic pollutant in sewage; and in 3,3',5,5'-tetramethylbenzidine oxide to produce color development reaction, where the organic pollutant includes methylene blue, Rhodamine B, phenol, trichlorophenol, methyl orange, and polychlorinated biphenyl (all claimed).    ADVANTAGE - The nanocomposite has high catalytic efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the nanocomposite comprising polymerization of hollow copper sulfide nanogranule and polypyrrole nanoparticles in a polymeric surface oxide layer.
NOVELTY - The device comprises a tube, a chamber hole, a feeding cylinder having a cylinder body and cover, a gas hole provided on a top portion of the cylinder body, an air inlet tube, a bottom plate connected with the air inlet tube, a carbon tube, a water chamber, a gas chamber, a water inlet tube connected with a water outlet tube, an inner cylinder connected with a pyrolysis chamber, an oil tube, and a pumping tube connected with the water inlet tube. The cylinder body and the water chamber are connected with each other, where air holes are distributed on a top portion of the feeding cylinder.    USE - The device is useful for preparing biochar, bio-oil and biogas (claimed).    DETAILED DESCRIPTION - The device comprises a tube, a chamber hole, a feeding cylinder having a cylinder body and cover, a gas hole provided on a top portion of the cylinder body, an air inlet tube, a bottom plate connected with the air inlet tube, a carbon tube, a water chamber, a gas chamber, a water inlet tube connected with a water outlet tube, an inner cylinder connected with a pyrolysis chamber, an oil tube, and a pumping tube connected with the water inlet tube. The cylinder body and the water chamber are connected with each other, where air holes are distributed on a top portion of the feeding cylinder. The pyrolysis chamber and the inner cylinder form a cavity chamber.
NOVELTY - Fuel sludge composite molding is prepared by preprocessing sludge by dewatering to 50-65% water content, uniformly mixing shell powder and aluminum powder with mass ratio of 10:1-3, adding 1-2 wt.% biomass powder, mixing to obtain conditioning agent, chopping sludge, mixing sludge with conditioning agent with weight ratio of 1:2.5-4.5, uniformly mixing, pressing to granular molding material, drying to 15% water content, dipping in waste oil layer, and drying.    USE - Preparation of fuel sludge composite molding (claimed).    ADVANTAGE - Preparation is simple, uses easy to obtain raw materials, and has reduced cost. Composite is environment-friendly, simple, low cost, promotes complete combustion of carbon particles, and has improved fuel performance and calorific value, high combustion activity, and good mechanical properties.
NOVELTY - Mixed waste fuel rods are manufactured by establishing waste processing conveyor belt and smoke and dust removal system in which production of each waste fuel rod is carried out in machine conveyor, classifying waste based on volume and length as metallic or non-metallic, rolling, breaking, crushing, calcining at constant temperature, drying until temperature reaches 25 degrees C, mechanically molding into fuel rods to obtain partially calcined fuel rods, and transferring remaining fuel to heat drying furnace.    USE - Manufacture of mixed waste fuel rods (claimed).    ADVANTAGE - Process is suitable for automation, avoids human injury, and recycles heat produced during reaction which avoids use of external processing energy supply.
NOVELTY - Biodiesel production involves degumming high acid value animal and plant waste oil with a stirring in vacuum, and then 0.2-0.5 wt.% of phosphoric acid is added at 110-140?OC for 20-40 minutes. 0.2-0.5 wt.% of active carclazyte catalyst is added in the formed mixture with stirring for 15-30 minutes, where the resulting mixture is filtered. The filtered material is placed into inner esterification device provided with a condenser, in which 1.5-3.0 wt.% of ferric sulfate is also added.    USE - Method for producing biodiesel by using high acid value wastes of plants and animals (claimed).    ADVANTAGE - The method produces biodiesel in a simple and eco-friendly manner with high yield and without producing waste water.    DETAILED DESCRIPTION - Biodiesel production involves degumming high acid value animal and plant waste oil with a stirring in vacuum, and then 0.2-0.5 wt.% of phosphoric acid is added at 110-140 degrees C for 20-40 minutes. 0.2-0.5 wt.% of active carclazyte catalyst is added in the formed mixture with stirring for 15-30 minutes, where the resulting mixture is filtered. The filtered material is placed into inner esterification device provided with a condenser, in which 1.5-3.0 wt.% of ferric sulfate is also added. The esterification device is heated at 105-130 degrees C, in which methanol is injected through measuring pump to bottom of the esterification device. The reaction mixture is heated at 110-130 degrees C with stirring for half an hour, where the formed layers are separated. The upper layer is an ester oil, where the lower layer is impurity and catalyst layer. 0.5-1.2 wt.% of potassium hydroxide or sodium hydroxide is added for performing esterification in ester exchange device at 45-65 degrees C for 20-60 minutes to obtain the finished product.
NOVELTY - Polaribacter sp. DL8-7 strain (CGMCC NO: 9011), is new.    USE - The strain is useful for degrading petroleum hydrocarbons, preferably polycyclic aromatic compounds (diesel fuel and liquid alkane) (all claimed).    ADVANTAGE - The strain utilizes carbon source for growth and reproduction, and degrades oil-diesel fuel (1:1 volume ratio) up to 41.53%.
NOVELTY - The furnace has hearth (1) which is provided on inner side of furnace shell (2). The top to bottom portion of furnace is divided into feed section (11), drying section (12), pyrolysis unit (13), oxidation unit (14) and reduction unit (15). The inlet (161) of water steam generating unit (16) is connected with a water tube (162). The exit (163) of water steam generating unit is connected with oxidation unit through steam outlet tube (164). The vapor steam generator generates steam by inserting of the reduction unit to increase the rate of gas production and gas heating value.    USE - Biomass gasification furnace.    ADVANTAGE - The biomass gasification furnace is simple in structure, so that manufacturing cost is reduced. The furnace is environment-friendly. The biomass furnace is formed without increasing the consumption of raw material. The rate of gas production is increased and nitrogen content of the gas is reduced, so that calorific value of gas in the furnace is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass gasification furnace.    Hearth (1)    Furnace shell (2)    Feed section (11)    Drying section (12)    Pyrolysis unit (13)    Oxidation unit (14)    Reduction unit (15)    Water steam generating unit (16)    Inlet (161)    Water tube (162)    Exit (163)    Steam outlet tube (164)
NOVELTY - Sludge from sewage treatment plant is thermally dried, to obtain dry sludge. Methanol and solvent are added to dry sludge in presence of sulfuric acid catalyst, such that dry sludge undergoes in-situ transesterification. n-Hexane is added to obtained mixture, and supernatant is collected. The supernatant is cleaned using cleaning liquid, upper n-hexane phase is collected, n-hexane phase is passed through water scavenger-containing filter device, filtered liquid is evaporated to remove residual organic solvent, and obtained residue is collected, to obtain biodiesel oil product.    USE - Preparation of biodiesel oil (claimed).    ADVANTAGE - The biodiesel oil is efficiently prepared by economical method.    DETAILED DESCRIPTION - Sludge from sewage treatment plant is taken as raw material, and thermally dried, to obtain dry sludge. Methanol for in-situ transesterification and solvent are added to dry sludge in presence of sulfuric acid catalyst, such that dry sludge undergoes in-situ transesterification. n-Hexane as extracting agent is added to obtained mixture, supernatant is collected, and lower layer liquid is discarded. The supernatant is cleaned using cleaning liquid, upper n-hexane phase is collected, the n-hexane phase is passed through water scavenger-containing filter device, filtered liquid is collected and evaporated to remove residual organic solvent, and obtained residue is collected, to obtain biodiesel oil product.
NOVELTY - Honeycomb fuel is prepared by crushing crop and municipal organic waste, adding quicklime, stone coal material, crude salt, and activated water according to sulfur content of crop and municipal organic waste, and performing treatment.    USE - Preparation of honeycomb fuel for warming, cooking, and hot water.    ADVANTAGE - Honeycomb fuel is environment-friendly and odorless, can become auxiliary renewable energy source, and has no waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of honeycomb fuel.
NOVELTY - Bio-oil reactant is prepared by pretreating biomass raw material containing cellulose, hemicellulose, and lignin to infiltrate hemicellulose and cellulose with reaction solution, soaking treated biomass to hydrolyze hemicellulose, and adding alkaline substance to neutralize to pH of 6-8.    USE - Preparation of bio-oil reactant (claimed).    ADVANTAGE - Bio-oil reactant saves cost, simplifies process flow, improves bio-oil pyrolysis stability, restrains production of gas during reaction, and reduces formation of tar and coke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-oil which involves placing bio-oil reactant in high-temperature high-pressure reactor and reacting at 280-380 degrees C with pressure of 5-30 MPa for 5-120 minutes.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the preparation of bio-oil. (Drawing includes non-English language text).
NOVELTY - The method involves taking light component oil in water phase as raw material, fatty alcohol in water or acidic system, and nickel as catalyst at 150-260 degrees C. The reaction is performed in a high pressure reaction kettle, slurry bed or fixed bed reactor, where the resulting mixture is cooled to room temperature for collecting liquid and catalyst. The resulting mixture is separated.    USE - Method for improving quality of biomass pyrolysis oil light components in water phase (claimed).    ADVANTAGE - The method improves quality of biomass is a simple, cost-effective and eco-friendly manner under mild reaction conditions without using commercial hydrogen.
NOVELTY - A high-frequency vibration guide clinic biogas respirator, comprises: reaction container (1), respirator checking device (2) and a respirator, where the reaction container includes separate clapboard (3), marsh gas exit (4), inlet and outlet, liquid piston compressing device; temperature induction plug assembly body; and liquid level height ruler.    USE - As high-frequency vibration guide clinic biogas respirator (claimed) use in the production of marsh gas.    ADVANTAGE - The biogas respirator efficient in a production of marsh gas.    DETAILED DESCRIPTION - A high-frequency vibration guide clinic biogas respirator, comprises: reaction container (1) and respirator checking device (2), where a respirator is connected with the bottom of the reaction container, where the reaction container includes separate clapboard (3), marsh gas exit (4), inlet and outlet and liquid piston compressing device, where the marsh gas exit at the top of reaction container mounting, separate mounting plate in deviation of the reaction container lower part, inlet and outlet set on the side wall of reaction container, liquid piston compressing device is not sealed, where the liquid piston lower end passes through the separate plate, and the upper end passes through the top end of a reaction container, where the respirator checking device set with a temperature induction plug assembly body, where the temperature induction plug assembly body includes temperature induction plug, liquid level height ruler; where the liquid level height ruler one end passes through one end of a device of respirator, and a temperature table, and the other end connecting with the temperature induction plug.    DESCRIPTION OF DRAWING(S) - The figure shows a high-frequency vibration guide clinic biogas respirator.    Reaction container (1)    Respirator checking device (2)    Separate clapboard (3)    Marsh gas exit (4)    Marsh gas outlet (12)
NOVELTY - A intelligent marsh gas machine, comprises: reaction container (1) including a left feeding and discharging channel (2), a right feeding and discharging channel(3); and where the reaction container includes separate clapboard (5) and gas exit (6).    USE - As intelligent marsh gas machine for producing marsh gas (claimed).    ADVANTAGE - The intelligent marsh gas machine shows high efficiently in production of marsh gas.    DETAILED DESCRIPTION - A intelligent marsh gas machine, comprises: reaction container (1) including a left feeding and discharging channel (2), a right feeding and discharging channel(3); where the reaction container includes separate clapboard (5) and gas exit (6), where the exit mounted on top of the reaction vessel; where separation walls mounted in the lower side of the reaction vessel; the separate plate is clung to the lower raw material of high concentration, where the lower portion of the raw material concentration is low; where the reaction container continuously produces biogas when gas pressure is increased, and where the feeding automatic stop working, when the pressure is too large.    DESCRIPTION OF DRAWING(S) - The figure shows an intelligent marsh gas machine.    Reaction container (1)    left feeding and discharging channel (2)    Right feeding and discharging channel (3)    Separate clapboard (5)    Gas exit (6)
NOVELTY - Kitchen waste is processed by sending pretreated kitchen waste to acid production reactor, adding acclimatized anaerobic sludge, applying electric field, performing hydrolysis acidification reaction to obtain supernatant and biogas residue, collecting generated hydrogen, centrifuging supernatant, adjusting pH, sending to methane production reactor, forming electric field to increase methane production activity of methane production microorganism, reacting, collecting methane, and using produced electrical energy to form electric field in acid production reactor.    USE - Processing of kitchen waste (claimed).    ADVANTAGE - Processing of kitchen waste is fast and efficient and has high microbial activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combined microbial electrolytic cell and microbial cell coupled 2-phase anaerobic kitchen waste processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the processing of kitchen waste. (Drawing includes non-English language text).
NOVELTY - Method for biogas power generation using fermented mixture of pig manure and straw, involves collecting pig manure and storing the manure, grinding waste crop straw, pumping the pig manure into slurry pool, simultaneously adding crushed straw, then mixing commercially available agents, and uniformly stirring components, performing microbial anaerobic fermentation of mixed sludge, desulfurizing biogas gas, and dehydrating and storing the biogas gas, generating gas turbine power, and fermenting biogas residue and biogas slurry by-product.    USE - The method is useful for biogas power generation using fermented mixture of pig manure and straw which is used for regional power grid (all claimed) and producing biogas residue and biogas slurry as byproducts, which are useful for increasing yield of spring and summer season cotton, summer and autumn season rice, and winter and spring season wheat.    DETAILED DESCRIPTION - Method for biogas power generation using fermented mixture of pig manure and straw, involves (a) collecting pig manure using truck and storing the manure, (b) grinding waste crop straw, (c) pumping the pig manure into slurry pool using slurry pump, simultaneously adding crushed straw, then mixing commercially available agents (hydrogen producing bacteria and methane-producing bacteria), and uniformly stirring components using stirring device, (d) pumping sludge into anaerobic fermentation tank and performing microbial anaerobic fermentation of mixed sludge to produce biogas, (e) desulfurizing the biogas gas through dry desulfurizing tower and water separator, and dehydrating and storing the biogas gas in storage tank, (f) generating gas turbine power, and (g) fermenting biogas residue and biogas slurry by-product collected in the storage tank.
NOVELTY - An electrolyte comprises lithium salt, an organic solvent, 6-10 wt.% anti-overcharge additive, 1-2 wt.% functional additive and 6-8 wt.% film forming agent, where the lithium salt is 1.5-2 mol/l lithium hexafluorophosphate, 0.6-1.5 mol/l dilithium dodecafluorododecaborate, and 0.5-1.0 mol/l lithium bis(oxalate)borate.    USE - Electrolyte for protecting overcharge of lithium ion power battery.    ADVANTAGE - The electrolyte has increased safety performance.
NOVELTY - Processing sewage waste by earthworm cultivation base material involves mixing sludge, waste slag and biological bacteria uniformly, where the mass ratio of the sludge, waste slag, and biological bacteria is 200:100-200:1-3; adding the mixture of sludge, waste slag and biological bacteria into a fermenting tank, and fermenting for 40-60 hours; and decomposing the fermentation, by supplying oxygen mixture for 2-5 days, to obtain cultivated earthworm.    USE - For processing sewage waste by earthworm cultivation base material (claimed).    ADVANTAGE - The method uses sludge and factory waste slag as main raw materials, which are low cost; simple method; has short production period; and is very suitable for large scale cultivation earthworms, thus increases the yield of earthworms.
NOVELTY - Preparing micro-smoke mosquito-repellent incense using sawdust comprises (i) subjecting sawdust to anoxic high temperature dehydration carbonization, and crushing to obtain charcoal powder; (ii) taking 70 wt.% wood carbon powder, 29.4 wt.% dry clay, 0.02 wt.% dimefluthrin, 0.02 wt.% natural pyrethrin, 0.01 wt.% synergistic agent, and 0.01 wt.% essence; (iii) mixing the above mentioned components in water to obtain adhesive wet powder; (iv) molding the adhesive wet powder in a molding machine to obtain disk-type mosquito-repellent incense; and (v) drying the resulting mold.    USE - The method is useful for preparing micro-smoke mosquito-repellent incense (claimed).    ADVANTAGE - The mosquito-repellent incense: has good mosquito repelling effect; utilizes the main product having environmental protection effect.
NOVELTY - Processing natural antioxidant active components of resveratrol, comprises (i) preparing starch granules-containing large aperture by carrying out biological enzyme technology; (ii) filling resveratrol into the starch cavity of starch granules-containing large aperture in an easy manner; (iii) preparing sodium alginate microcapsules having smooth surface, circular or elliptical in shape, and good transmission property; and (iv) adding resveratrol into a transmission system having high loading amount, and slow releasing rate.    USE - The method is useful for processing natural antioxidant active components of resveratrol (claimed).    ADVANTAGE - The method is environmentally friendly, and produces product having small molecules as active components having high load carrying capacity, and slow releasing characteristics (all claimed).
NOVELTY - One biomass steam boiler, a combustion room with the pneuma furnace of a part set with a steam boiler, a combustion room side wall set with a smoke pneuma, outer combustion room side wall set with steam boiler is connected with the water tube, the outer wall of steam boiler, a cooker hearth side wall is formed between the flange and the return fire smoke channel. Making pneuma furnace with one time, making system and feeding system. The combustion room has a secondary oxygen supply device. This utility new type the steam pot and biological gasification furnace with biomass to a fuel a smart melting as a whole, set with pot body is connected with the connector of water outlet pipe and the furnace body can be through a connector of the water level observation that inner pot, and water can be added, the water tube of water can be conveniently inner pot discharging, simple and compact structure, convenient use, energy-saving effect is good.
NOVELTY - This new type utility claims one a paraquat water soluble granule spraying drying flow and device, wherein the device comprise feeding mechanism, an atomizing mechanism, air feeding mechanism, and drying mechanism, a fluidized drying cooling mechanism and exhaust mechanism. This utility new type provide the one a paraquat water soluble granule spraying flow drying granulating device, the device can be a paraquat water soluble granule of full-automatic, seal, dustless, clean and continuous production, which avoids dust leakage, it can reduce environmental pollution and prevent the suction caused by a directly, increase the production safety. Besides, the device can increase and the rate of finished products and enhance granulation strength.
NOVELTY - A biomass tar one this utility new type supply of a fluidized bed reactor, at least used for holding reaction material include a reactor shell, said inner reactor lower part fixing set with a distributor, a reactor upper part set for preventing the escape of a catalyste, said reactor shell set with a raw material entrance and product exit, a raw material entrance at least comprise biomass tar entrance, a biomass tar entrance set on the side wall of a reactor shell and a distributor of the above, this utility new type of fluidized bed reactor, through a distributor arranged above the biomass tar entrance, hydrogen distributor from entering into the lower part of impact and a circulation liquid is valid, and can ensure catalyste with biomass tar fully contact and mix reaction occurs promptly, so as to prevent the polymerization reaction of biomass tar to produce a coking phenomenon.
NOVELTY - Organic fertilizer comprises 40-80% fermented mushroom residue and 20-60% fermented adulterant, where the adulterant comprises crop straw, biogas residue or soybean curd residue.    USE - The organic fertilizer is useful in agricultural fertilization.    ADVANTAGE - The organic fertilizer protect soil environment and promotes plant growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer comprising harmless fermentation of the mushroom residue and the adulterant using a yeast for 15 days, followed by uniform stirring of 40-80% fermented mushroom residue and 20-60% fermented adulterant, then processing production using single double-cooling oven, granulating the product using rotary drum granulating machine, drying the produced fertilizer granules and finally carrying out cooling process to obtain organic fertilizer, and then packing the produced product.
NOVELTY - Organic fertilizer is produced by drying pig manure on ground, uniformly mixing e.g. straw with probiotics, adding mixture to dried pig manure, performing fermentation, mixing fermented product with feces and water and performing anaerobic fermentation, turning fermented product and adding water (suitable quantity), adding honeycomb and white gas to the fermented product, and continuously increasing environmental temperature, obtaining product without feces odor, and adding humic acid, ash and urea, and mixing and packing obtained product.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is cost-effective, environmentally-friendly, convenient to use, and prepared by less time consuming process.    DETAILED DESCRIPTION - Organic fertilizer is produced by (a) drying pig manure on ground, uniformly mixing straw, rice or corn with probiotics and adding water, adding mixture to dried pig manure, spraying water on the mixture, and performing fermentation process at 45 degrees C and humidity of 50%, (b) mixing fermented product with feces and water, turning mixture twice and performing anaerobic fermentation (during second day of fermentation process), (c) turning fermented product and adding water (suitable quantity) when the color of product is turned to white to cream color (during fifth day of fermentation process), (d) adding honeycomb and white gas to the fermented product, and continuously increasing environmental temperature (during ninth day of the fermentation process), and (e) obtaining product without feces odor after 12 days of fermentation process, and adding the obtained product to humic acid, ash and urea in a ratio of 50-59:10-15:7-11 and mixing and packing obtained product.
NOVELTY - A rice organic composite fertilizer comprises 35-50 wt.% quail manure, 8-15 wt.% calcium silicate powder, 8-15 wt.% calcium-magnesia phosphate fertilizer, 8-15 wt.% zeolite powder, 8-15 wt.% vinasse powder, 4-6 wt.% humic acid, 10-15 wt.% potassium chloride, and 1-3 wt.% biological bacteria.    USE - Rice organic composite fertilizer.    ADVANTAGE - The fertilizer increases yield and quality of rice, and it has high roughness.    DETAILED DESCRIPTION - A rice organic composite fertilizer comprises 35-50 wt.% quail manure, 8-15 wt.% calcium silicate powder, 8-15 wt.% calcium-magnesia phosphate fertilizer, 8-15 wt.% zeolite powder, 8-15 wt.% vinasse powder, 4-6 wt.% humic acid, 10-15 wt.% potassium chloride, and 1-3 wt.% biological bacteria. The fertilizer is prepared by mixing quail manure, calcium-magnesia phosphate fertilizer, vinasse powder and humic acid, adding biological bacteria, maintaining moisture content to 50-55%, stacking to ferment for 10 days, and adding into fermentation tower to ferment for 12 days; performing aerobic fermentation until moisture content is 25% and no more odor, and discharging fermentation material; and mixing with calcium silicate powder, zeolite powder and potassium chloride, crushing, sieving, inspecting, and granulating.
NOVELTY - The utility model claims a new hydrogen manufacture area, especially claims a remote anti-explosion coalification carbon dioxide circulation using hydrogen preparing device, comprising: CO2 tank, multi-plasma torch generator, sending intelligent coal, solar energy steam generator, steam tank, reaction chamber, steam generation unit, purifier, separator, solar energy electrolyzer, H2 tank, O2 tank, an online detector, a remote anti-explosion control system, CO2 tank, steam generation unit and multi-plasma torch generator connected, sending intelligent coal, steam tank and multi-plasma torch generator and reaction chamber connect. The utility model is new beneficial effect wherein: 1, this utility new type has simple structure, variable, 2, zero pollute discharge, CO2 circulation use, 3 and effective use, construction preparing hydrogen, oxygen, integrated chain, 4, this utility new type active device using solar can, relative traditional device can reduce consume, 5, anti-explosion remote control system to produce full process for strict monitoring and ensures safety of production line.
NOVELTY - This utility new type relates to one dedicated to a garbage treatment plant mix small integrated treatment tank of sewage, the treatment tank from left to right one time include, anoxic reaction area, an anaerobic reaction area, an aerobic area and sedimentation reflux reaction area, mixing area one side part is provided with a sewage inlet, a sludge reflux opening and a return opening up the precipitate of mix area under the sewage inlet, a first baffle plate set in the mix area and anoxic reaction area, the first baffle is provided with connected first port, set with a second baffle is set between the anaerobic reaction area and the aerobic reaction area, the second baffle is provided with second connected hole, a third baffle plate is set with sedimentation reflux area middle part, the third baffle is provided with third connected port, flow area upper part set with a water port at the bottom of sedimentation reflux area set with a return water pump, the return water pump through a pipeline sedimentation reflux inlet of a mix area, this utility new type with small floor area, using integrated design, simple structure, low construction and operation cost is low, the treatment effect is good.
NOVELTY - This utility new type relates to one a sewage processing device, especially a one combined ecological suspension bed. Include a bed, b purification layer, filling layer and plant purification layer and filler layer a. in a bed up, purification layer comprise plant planting layer and plant layer, plant planted in the planting layer upper layer. The structure set with a bed, and the plant purification layer, a filler layer set in a suspension bed up, at the same time with filler of purification, a biological purification process of plant, plant root lower is long, it can help to a filler, so as to increase the purification effect of whole body.
NOVELTY - This utility new type relates to a one by making use of straw quick fertilizer system, the system comprise a crusher, steam-type organic garbage disposer, acidification tank, an acid liquid separator, separator and fertilizer device, a steam exit-type organic garbage disposer inlet, steam-type organic garbage disposer exit a acidification tank inlet, acidifying tank exit a acid liquid separator inlet, liquid separator exit a filter separator inlet, separator exit connecting the fertilizer device, this utility new type for fermenting steam exploded wood fibre straw rear gas of residual solid matter and a recycling, the fertilizer efficiency is high and the safety is good, the yield is high, energy-saving and environment-friendly.
NOVELTY - This utility new type relates to a straw fertilizer one processing device, that is a serial one straw fertilizer speed fermentation tank, include a one or a multi-fermenting tank (1), wherein said speed fermentation tank (1) inner water tube and set with a winding (4), a fermenting tank (1) of inner water tube (4) form a closed loop, a multi-fermenting tank (1) and a water tube (4) are connected. The beneficial effect is as follows: fermenting tank inner temperature uniform, oxygen, and not need turning, fermenting heat would not loss, a fermenting tank heat, without supplemental initial heat, saves a lot of fuel, for a short, low fermentation cost, front rear to receive a continuous large scale fermentation fertilizer-making spring sowing, main production device of straw fertilizer.
NOVELTY - One a biomass fuel gasification ash water cooling spiral slag removing device, it comprise the ash collecting box, a slag collecting box by an upper cover plate, lower cover plate and side water cooling wall is surrounded by seal, upper part and lower part of said ash collecting box set with a cooling water inlet tube and cooling base water discharging tube base, a upper cover plate set with a biomass pneuma for furnace slag is connected with a slag liquid entrance, said upper cover plate is further set with a extending to a stirrer inner ash collecting box, a lower upper cover plate set with solid ash exit, said solid slag exit is set on the ash collecting box of spiral slag remover, a side water cooling wall by several arranged in parallel a cooling medium conveying tube and combination is formed by a flat steel is welded between the adjacent cooling medium conveying tube. The design not only can cool ash, but also can prevent dust and toxic substance in a flue gas directly entering into the atmospheric environment, a fully cooled slag material, operation cost is low, the energy utilization ratio is high, which meets the national energy conservation and emission reduction of.
NOVELTY - This utility new type relates to a one double-fluidized bed biomass gasification system indirectly, double-fluidized bed interaction a combustion and indirect gasification prepare high quality biomass synthetic pneuma, include fluidized bed combustor and the second level cyclone separator, a fluidized bed gasifier and second level cyclone separator, a combustor air adding system, a burner bed material feeding system, the gasifier steam adding system, the gasifier biomass feeding system, the gasifier and combustor bed material circulation system, a material, a combustor and gasifier pressure control system. This utility new type needle use inner and outer circulation which combine a double-fluidized bed gasifier, the indirect nitrogen pneuma and synthetic pneuma of separate in natural air, through reactor design of improved structure, different bed material mix use, increase of bed material circulation flow. pneuma and solid mix horizontal to increase gasification efficiency and synthetic pneuma heat value, low tar content, prepare high quality synthesis pneuma.
NOVELTY - This utility new type bottom claims one a biomass normal pressure gasification furnace liquid slag structure, include gasification furnace tube, pneuma for furnace body inner wall of the outer cylinder inner in turn set with a furnace wall insulating layer and furnace wall refractory wear-resisting layer, pneuma one furnace cylinder body set with a bearing furnace, furnace wall refractory wear-resisting layer and furnace bottom bearing form gasification furnace slag tank, a gasification furnace tube upper part set with a plasma torch nozzle, plasma torch nozzle in turn passes through the furnace wall insulating layer and furnace wall refractory wear-resisting layer is connected with the gasification furnace slag tank connected, bearing furnace bottom is high periphery and low middle of arched structure, the peripheral distribute with an inclined discharge channel, discharging channel in turn passes through the furnace wall refractory wear-resisting layer and furnace wall insulating layer and the slag, the slag in the gasification furnace set with a tube. This utility new type can be continuous deslagging, heat preservation effect is good, the continuous production time is long, high gasification efficiency, a greatly reduced production and operation cost, and it can be widely application biomass gasification technology field.
NOVELTY - This utility new type claims a biomass pneuma in one furnace water cooling type air, comprise a pipe set on the furnace wall brick up the outer wall of air supply tube along the axial direction symmetrical distribute on one strip-shaped baffle plate for the outer circumference of air supply tube are symmetrically set with one for semi-sleeve, two semicircular side of sleeve is connected with the outer side of a strip-shaped plate, a semicircular sleeve of a lower two end set with a upper sealing plate and lower sealing plate, so as to form two independent of a semicircular water cooling jacket on the periphery of air tube, wherein a semicircular water cooling jacket one the upper end set with a water inlet tube, and the other one a semicircular water cooling jacket set on the upper end, and a two semicircular water cooling jacket of lower end set with connected hole. This utility new type of beneficial effects comprise: 1. A valid cooling air, which avoids high temperature inner furnace smoke pneuma for air and furnace wall brick of ablation caused by 2. A valid avoids liquid slag block air, 3. Structure is simple and easy to be realized.
NOVELTY - This utility new type claims a biomass synthetic pneuma quench tower one ash bucket online clearing device, comprise dust hopper main body, wherein a dust hopper in the body cavity is set with blast pipe, a blast tube wall distribute with a downwind; top is set with first level gate plate door and second level gate plate door, a first level gate plate door and second level gate plate door a dust hopper main body set with a small bottom of the ash bin. The device structure is simple, and the stopping of the condition that a lower a working clearing, clearing process can be valid in a seal, which avoids synthesizing pneuma would not a outer leakage, at the same time, it would not make the oxygen in air is mixed in a synthetic pneuma.
NOVELTY - This utility new type claims a biomass synthetic pneuma one tar removal device, comprise vertically set with a seal tube, a seal tube top set with gas exit joint, a seal bottom of the cylinder body set with a slag discharging port joint, a seal tube lower part side wall set with a gas inlet joint and a gas inlet joint and the gas exit joint in turn set with first-stage filter device and second level filtering device. The utility model reduces biomass synthesis in valid pneuma of dust concentration and tar content, a simplified synthesis pneuma later period purification treatment process, and it can be widely application to biomass gasification field.
NOVELTY - One marsh gas membrane method of the new utility model claims marsh gas purifying technique area of purifying heating system, comprising heat recycling circulation pipeline, the heat of recycling circle pipeline equipped with hot water circulation pump, and compressor is set with water cool device in cooling system of compressor and used for heating gas and heat exchange device. The energy consume of this utility new model by using the compression and then generating marsh gas and heat recovery can then to marsh gas heating, so as to reducing gas membrane method purifying process, using energy use rate can increase, using the marsh gas membrane method purifying pre-process is more energy saving environmental protection.
NOVELTY - This utility new type relates to one based on a central biomass gasification system of crop straw include crusher, steam-type organic garbage disposer, acidification tank, an acid liquid separator and methane tank, biological desulphurization tower and a compressor, a steam exit-type organic garbage disposer inlet, steam-type organic garbage disposer exit a acidification tank inlet, acidifying tank exit a acid liquid separator inlet, liquid separator exit a methanation tank inlet and methane tank exit a biological desulfurizing tower inlet, the biological desulfurizing tower exit connecting the compressor, this utility new type preprocessing straw with a short, natural gas production, gas production amount, stable operation and low cost.
NOVELTY - This utility new type new energy relates to a preparation field, especially relates to a combined-type marsh gas biological fermentation one preparation system, include the biological marsh gas fermenting device, marsh gas storage room, safety discharge device, pneuma water separate device and marsh gas pipeline in turn through connecting a biogas purification desulphurization device, marsh gas pressurizing device and marsh gas cooker device, biogas biological fermentation device and a marsh gas storage room, safety discharge device and pneuma water separate through clamp device clamping fixed connecting, and the biogas biological fermentation device of the upper part opening and the bottom opening of the biogas storage room of the match. This utility new type on one hand reduces the occupied volume of biogas biological fermentation preparation system, which increases one time volume and reduces the transportation cost is high, on the other hand it simplifies the biogas biological fermentation device with the marsh gas storage room, safety discharge device, pneuma water separate device such as a separate mounting of mounting process, avoids the occurrence of leakage and increase the safety.
NOVELTY - This utility new type claims a one for installed on the vehicle in a mix power device, a vehicle category technology field, especially relates to a water electrolytic type one oil electric mix power device, less investment cost of the normal vehicle a fuel oil electric mix power new energy of a vehicle. C use a commercial power lithium battery group charging process, the energy of the lithium battery group through high efficiency water electrolysis device produce hydrogen oxygen gas, not only with not a large amount of storage, hydrogen oxygen gas through gas single entering into engine burning a water, time the lithium battery group electric quantity, the fuel switching switch through a fuel is switched to a state continuously. This utility new type avoids the user re-purchase of expensive oil electric mix power vehicle of huge cost and overcomes the pure electric vehicle mileage, a problem, which avoids the hydrogen bottle explosion danger of too large a volume, a valid reduces the fuel consumption, reduces the air pollution.
NOVELTY - This utility new type provide the one a synthetic ammonia waste heat recovery using system, wherein would produce tail pneuma and removing pneuma slag making time in the synthetic ammonia, include: for the decarburization tail pneuma a removing process of removing purification device, used for making the pneuma slag screening and purifying process of a filter purifying device, used for the said purification decarburization treatment device by a tail pneuma and removing said filter purifying device process of making the pneuma slag mix, to produce solid fluidized bed boiler of high temperature steam. This utility new type provide a system by using a gas-solid fluidized bed boiler burning technology, a synthetic ammonia produce of a waste, produce steam to generate electricity, a, heating use, time can be the synthetic ammonia produce a waste of a better recovery and comprehensive utilization of not only a waste and protect the environment.
NOVELTY - A one Straw gasification heating furnace, an ash bucket is set at the bottom of heating furnace, a combustion chamber located on the ash bucket, and set with through hole is connected with the ash bucket connected return combustion room is set on the back of the combustion room outer surface set with hearth water set, combustion room upper part set with through hole and the fire cage cover is connected between the lifting cylinder is set on the combustion chamber fire through hole with the cage fire cover, upper layer water set in mounting the lifting cylinder and a fire between fire smoke channel, a smoke water set connect with the hearth water set, the back combustion chamber set with a fire smoke channel, a smoke fire channel outer surface mounting with a smoke exhaust water set, upper end part set with water outlet port, in a plate inner fire smoke channel. This utility new type of advantage is that not only can burn straw pressing block, but also can burn coal, the fuel burns fully, a harmful gas is low, the combustion heat value high and wide use.
NOVELTY - Preparation of 6-aminopenicillanic acid comprises adding penicillin fermentation liquid in penicillin acylase and performing cracking reaction to obtain 6-aminopenicillanic acid, phenylacetic acid and penicillin mycelium mixture; microfiltering, ultrafiltering, removing penicillin mycelium and macromolecular substances, and concentrating by nanofiltration; mixing 6-aminopenicillanic acid and phenylacetic acid concentrate, decoloring, absorbing, and separating using resin to obtain 6-aminopenicillanic acid solution; and adjusting pH, crystallizing, filtering, washing, and drying.    USE - Method for preparing 6-aminopenicillanic acid (claimed).    ADVANTAGE - The method is suitable for industrial production, avoids the use of n-butanol, butyl acetate and other organic solvents, improves product yield, and reduces energy consumption. The 6-aminopenicillanic acid is environment-friendly.    DETAILED DESCRIPTION - Preparation of 6-aminopenicillanic acid comprises adding penicillin fermentation liquid in penicillin acylase and performing cracking reaction to obtain 6-aminopenicillanic acid, phenylacetic acid and penicillin mycelium mixture; microfiltering, ultrafiltering, removing penicillin mycelium and macromolecular substances, and concentrating by nanofiltration to obtain 6-aminopenicillanic acid and phenylacetic acid mixture; mixing 6-aminopenicillanic acid and phenylacetic acid concentrate, decoloring using decoloring agent, absorbing, and separating using resin to obtain 6-aminopenicillanic acid solution; and adjusting pH until isoelectric point, crystallizing, filtering, washing, and drying.
NOVELTY - Method of preparing acetyl glycyrrhetinic acid, involves extracting licorice using microwave, filtering the extract and obtaining licorice extract containing 9-65% glycyrrhizic acid, adding the catalyst and again subjecting the mixture to microwave reaction, where the catalyst is sulfuric acid, hydrochloric acid or phosphoric acid.    USE - The method is useful for preparing acetyl glycyrrhetinic acid (claimed).    ADVANTAGE - The method is rapid, cost-effective and environmentally-friendly, reduces consumption quantity of solvent, and increases conversion rate.
NOVELTY - The system has a compressor (2) that is set with entrance and exit. Two layers of hollow fiber films (4,5) and a carbon dioxide (CO2) recovery device (7) are set with the inlet. The inlet of the compressor is connected with a pipeline which is connected with hollow fiber film (4) of non-penetration gas exit. The inlet of CO2 recovery device is connected with a pipeline, and the tail end of the CO2 recovery device is connected with pneumatic exit. The hollow fiber film (5) is penetrated in the gas exit of compressor through pipeline.    USE - System for purifying carbon-dioxide in biogas.    ADVANTAGE - High operation convenience is achieved using the simple structured system for purifying carbon-dioxide in biogas. The automatic degree is high and improved safety and reliability is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for purifying carbon-dioxide in biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for purifying carbon-dioxide in biogas.    Marsh gas desulfurization dehydrating device (1)    Compressor (2)    Hollow fiber films (4,5)    Methane (6)    Recovery device (7)
NOVELTY - Preparation of 4,6-dichloro-5-nitro-2-propylthio-pyrimidine intermediate (I) comprises adding 2-nitro-malonic acid diethyl ester and thiourea in solvent, adding strong alkali, and synthesizing to obtain pyrimidine-containing intermediate (Ia); adding in solvent, adding strong alkali and halogenated propane, and reacting to obtain 4,6-dihydroxy-2-propylthio-pyrimidine intermediate (Ib); and adding in solvent, adding alkali and acylating agent, and reacting.    USE - Method for preparing 4,6-dichloro-5-nitro-2-propylthio-pyrimidine intermediate (I) (claimed).    ADVANTAGE - The method is easy to operate and suitable for large-scale industrial production, and has low environmental pollution.    DETAILED DESCRIPTION - Preparation of 4,6-dichloro-5-nitro-2-propylthio-pyrimidine intermediate of formula (I) comprises adding 2-nitro-malonic acid diethyl ester and thiourea in solvent, adding strong alkali, and synthesizing in the presence of strong alkali to obtain pyrimidine-containing intermediate of formula (Ia); adding in solvent, adding strong alkali and halogenated propane, and reacting to obtain 4,6-dihydroxy-2-propylthio-pyrimidine intermediate of formula (Ib); and adding in solvent, adding alkali and acylating agent, and reacting.
NOVELTY - Oxidative elimination of dihydrotestosterone finasteride iodide comprises using peroxyacetic acid as oxidant.    USE - Method for oxidative eliminating of dihydrotestosterone finasteride iodide used for preparing finasteride (claimed).    ADVANTAGE - The method uses cheap and easily obtained peroxyacetic acid as oxidizing agent, obtains high yield of finasteride reaching to 96% and high purity of finasteride reaching to more than 99.7%, is environment-friendly, simple, and stable, and has low cost.
NOVELTY - An edible mushroom cultivation method, involves obtaining edible mushroom cultivation medium, generating waste material for biogas, and producing biogas. The medium is placed on the compartment for mushroom cultivation, followed by introducing mushroom sporocarp in the medium and spraying generated biogas.    USE - Method for cultivating edible mushroom.    ADVANTAGE - The method enables cultivating edible mushroom with beneficial effects, in a cost effective manner.
NOVELTY - This utility new type relates to a composite fertilizer production line one, include stir tank, blanking bin, stir driving device, a stir, fertilizer conveying device, conveying device, stir driving device mounting the rotating shaft mounting with a stir blade, a blanking conveying device one end the blanking chamber, discharging chamber and stir tank a, fertilizer conveying device mounting the stir tank exit, wherein it further set with a control device, said stir tank is cylindrical structure, a stir tank is inclined set, a stir blade and the rotating angle of the shaft is 70 to 80 degrees, a control device with the stir driving device, conveying device, conveying device are a. This utility new type fertilizer conveying device above a mounting with a screen, a screen is located between the stir tank exit with the fertilizer conveying device. This utility new type has simple structure, energy-saving, good crushing effect, stir automatic degree high and so on.
NOVELTY - This utility new type relates to a high efficient controllable one biomass carbonized gasification device, belonging to the biomass carbonized gasification device technology field. Technology solution is as follows: the furnace body upper part is raw material bin (14), lower part of the furnace body is in pneuma chamber (15), set with a gas exit on the upper part of a pneuma for chamber (12), a combustible gas upper exit through a gas valve (9), a gas exit (8), the bottom of pneuma one chamber set with a gas lower exit (11), a lower gas lower exit through a gas valve (10), a gas exit, the lower pneuma one chamber set with a spiral discharging device (16), one chamber set with pneuma oxygen distribution device (5). This utility new type all smoke pneuma recovery is a combustion gas, carbonizing speed is fast and continuous production, high yield, a combustible gas through a exit and a gas lower exit of opening and closing, at the same time, match a discontinuous spiral discharging device, which can yield a yield and biomass carbon according to any a need of combustible gas, gasification of a biomass carbon at the same time can.
NOVELTY - This utility new type relates to a biomass gasification furnace environmentally-friendly one purification device. One a biomass vaporization furnace purification system, comprise biomass gasification furnace, the air outlet of the biomass gasification furnace in turn connected first-stage dust-removing pipeline with a vertical set of, cyclone dust collector, a tar purification device and a draught fan, a tar purification device comprise the sealed cleaning housing, a vertical set with the multi-channel stainless steel wire ball filter net layer inner shell of purification, a. cleaning the shell body bottom part and air inlet hole and outlet hole of pneuma. This utility new type for improved through a purification system of the device, and greatly enhance the purifying capacity of a filter so that the process in use can reduce the smoke dust, the green environmental protection of.
NOVELTY - A one oxygen-containing gas fuel manufacturing device, comprises one electrolytic unit, one air supply unit, mix one groove and one feedback control unit. The electrolytic unit the water electrolysis to produce hydrogen and oxygen to the mix groove, and the rear of the liquid catalyst in the mix groove mix produce a combustion gas output to one burner. The air supply unit into a rear compressing air to the groove in mix to accelerate a speed of combustible gas. The feedback control unit detecting the burner for a combustion gas consumption size of amount according to control the unit to change a produce a hydrogen amount and the oxygen amount. Therefore, a precise electrolytic unit produce a control oxygen amount and the hydrogen amount, the oxygen amount and a hydrogen amount is not enough or the multi-and increase safety of a use.
NOVELTY - Straws are dried, ground to length of 2 cm or less, and subjected to thermal pyrolyzis process using thermal pyrolyzis equipment including several screw feeders which are connected end to end and arranged from top to bottom in a reciprocating manner, electrical heating tubes laid on the surface of a pipeline of each screw feeder, and a pyrolyzis gas pipeline arranged at the upper portion of a tube cavity of each screw feeder. The generated pyrolyzis gas is condensed at temperature of 450-600 degrees C, oil is discharged and slag is simultaneously discharged.    USE - Method of extracting bio-oil from straws (claimed).    ADVANTAGE - The method efficiently and economically extracts bio-oil from straws with pressure-free process, by eliminating the potential safety hazards caused by pressure and simultaneously reducing the power consumption by pressure.
NOVELTY - The manufacturing method involves joining electrolytic membranes (300) by heating compression to form a film extension member (210). Each electrolytic membrane has base films (1,1s) that are joined in thickness direction by a connector (410). The connector is deformed in a clearance gap between electrolytic membranes, such that the cross-sectional shape of the connector is concave shape.    USE - Strip-shaped MEA manufacturing method for fuel cell.    ADVANTAGE - Yield is improved since the length of the half of connector is shorter than the length of the film extension member. Production defect is reduced by deforming the connector in the clearance gap.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a connector.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross sectional view of the film extension member.    Base films (1,1s)    Film extension member (210)    Electrolytic membranes (300)    Connector (410)
NOVELTY - A homogeneous single-phase catalyst comprises strontium, yttrium, titanium and ruthenium.    USE - Catalyst is used in manufacture of electrode for fuel cell for carbon dioxide reforming (all claimed) in production of synthesis gas.    ADVANTAGE - The catalyst has high catalytic activity and electroconductivity, and suppressed carbon deposition phenomenon.    DETAILED DESCRIPTION - A homogeneous single-phase catalyst has composition of formula: (Sr1-yY'yTi1-xRuxO3-d), where x is more than 0 to less than 1, y is more than 0 to less than 0.1 and d is 0 to more than 1. An INDEPENDENT CLAIM is included for dry-reforming method of carbon dioxide.
NOVELTY - The environment-friendly waste matter resourcing apparatus has a waste melter gasifier unit (110), where a waste melter gasifier and purifier produces the environment-friendly synthetic gas. A plasma pyrolysis melting furnace is provided for gasifying a melting furnace using a plasma torch and a burner. The steam and liquefied carbon dioxide are produced, where the synthetic gas is ejected in the plasma melting furnace. A carbon dioxide refinement is provided, where the heat exchange is cooled with a waste-heat recovery boiler device unit (120).    USE - Environment-friendly waste matter resourcing apparatus for use with the plasma pyrolysis gasifier of the waste.    ADVANTAGE - The waste melter gasifier unit is provided, where a waste melter gasifier and purifier produces the environment-friendly synthetic gas, and hence ensures collecting the carbon dioxide refined to the high purity in an effective manner and prevents the generation of the pollution in a reliable manner, and also preserves the source of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an environment-friendly waste matter resourcing apparatus. (Drawing includes non-English language text).    Waste melter gasifier unit (110)    Waste-heat recovery boiler device unit (120)    Synthetic gas refinement device (130)    Synthetic gas boiler device unit (140)    Cooling device unit (150)    Boiler water supply device unit (160)
NOVELTY - 40% Methane is treated with 60% peat at 300-400 degrees C in presence of a catalyst to form 2/3 of pulverized salt, sodium chloride, and 1/3 of pulverized iron, iron or iron oxide, under pressure of 1500-1800 psi to obtain kerosene.    USE - Conversion of peat into kerosene used as fuel for engines.    ADVANTAGE - The method efficiently and economically converts peat into high-quality kerosene.
NOVELTY - Manufacture of hybrid coal involves mixing timber powder and liquid biomass diluted solution to form liquid biomass paste, adhering the paste on surface of coal and drying.    USE - Manufacture of hybrid coal (claimed).    ADVANTAGE - The method enables efficient manufacture of hybrid coal with high density.
NOVELTY - Invention relates to production of fuel briquettes including grinding of wood wastes, their mixing, drying and pelletizing. Note here that briquette comprises an extra element composed of core of compacted asp saw dust with hole for drawbar.    USE - Process engineering.    ADVANTAGE - Higher calorific capacity, higher ecological and fire safety at application, transportation and storage.1 dwg
NOVELTY - A fuel component comprises 60-80 wt.% particulate derived from corn stover having particle size of 100-35000 mu m, 20-40 wt.% wood fiber having particle size of 100-30000 mu m and 1-10 wt.% sodium bicarbonate, and does not coal. The fuel component has dimension of 6 cm, volume of 10-100 cm3 and moisture content of less than 14%, and provides heat energy of 7000 BTU-lb-1.    USE - Fuel component is used for fuel source (claimed) used in power plant.    ADVANTAGE - The fuel source provided using the fuel component is economical, and has reduced impurities and emission of hydrochloric acid, sulfur dioxide and nitrogen oxide during combustion, low moisture content and high heating value.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel source, which comprises fuel component and fossil fuel; and    (2) method of reducing emission during combustion of fossil fuel, involves co-firing the fuel component with fossil fuel.
NOVELTY - The present invention discloses a method of a biodiesel production. The method comprises the steps of: adding a basic oxygen furnace slag as a catalyst into oils and alcohols to proceed a transesterification so as to obtain the biodiesel.
NOVELTY - The present invention relates to a roasting test method for biomass and burning rate evaluation method for biofuel after roasting. The roasting test method for biomass includes the following steps: (a) providing a biomass; (b) grinding the biomass; (c) placing the biomass after grinding into a rotary heating furnace; (d) roasting the biomass to make the biomass become biofuel; and, (e) analyzing the heating value increasing rate and coal combustion replacement rate for the biofuel.
NOVELTY - Aerobic fermentation device comprises a semi-cylindrical cavity (5), a speed reducer, a rotating shaft (2), a stirring paddle (3), stirring blade (4), a support shell and a control system, where the rotating shaft is arranged with the stirring paddle.    USE - Aerobic fermentation device for kitchen garbage (claimed).    ADVANTAGE - The aerobic fermentation device ensures simple structure, small occupied space and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an aerobic fermentation device.    Rotating shaft (2)    Stirring paddle (3)    Stirring blade (4)    Semi-cylindrical cavity (5)    Inner wall (6)
NOVELTY - Aerobic fermentation device comprises a reaction chamber, a water circulation system, a condensation water collecting system, an air heating system, a ventilation system and water heating bath that is connected to a heat preservation system. The reaction chamber is mounted with a switch. A temperature sensor is installed with the water heating bath.    USE - Aerobic fermentation device for kitchen garbage (claimed).    ADVANTAGE - The aerobic fermentation device ensures simple structure, high space utilization rate and low operation energy consumption.
NOVELTY - A hydrogen generator (1) comprises modifier (1a) which produces fuel gas containing hydrogen by reforming reaction of source gas, combustor (1b) which burns source gas or fuel gas and heats modifier, off combustion gas path (12) which discharges off combustion gas emitted in combustor, gas sensor (17) which detects specific gas by burning specific gas which is positioned on off combustion gas path and is contained in off combustion gas, and buffer tank (14) which is positioned in upstream of gas sensor and stores off combustion gas.    USE - A hydrogen generator for fuel cell system (claimed).    ADVANTAGE - Oxygen deficiency of off combustion gas of combustor, carbon monoxide concentration detection failure of gas sensor, and deterioration of detection accuracy of sensor can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generator. (Drawing includes non-English language text).    Hydrogen generator (1)    Modifier (1a)    Combustor (1b)    Off combustion gas path (12)    Buffer tank (14)    Gas sensor (17)
NOVELTY - A high-strength blast furnace coke is manufactured by drying coal blend (A), obtaining char (B) by extracting chemical material from oil component obtained by dry-distilling biomass in which dreg contains 10-100 mass% residual oil components (C), and mixing char with coal blend.    USE - Manufacture of high strength coke for blast furnaces (claimed).    ADVANTAGE - Highly strong blast furnace coke with required particle size can be manufactured with high reactivity with gas, biomass can be recycled as resources, generation amount of carbon dioxide can be reduced, and installation cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawings show schematic diagrams of the conventional manufacturing process cokes and the manufacturing process of cokes.    Drying machine (1)    Coke oven (2)    Coal blend (A)    Biomass char (B)    Residual oil component (C)
NOVELTY - Exothermic wood pellets are obtained by impregnating/coating a composition comprising 75-85 wt.% glycerin, 10-20 wt.% alcohol, 2-3 wt.% fatty acid, 2-3 wt.% dispersing agent and oil obtained as by-product during hydrolysis of glycerin, fatty acid and glycerol, in wood pellets, and has calorific value of 7000 kcal/kg.    USE - Exothermic wood pellets (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of exothermic wood pellets.
NOVELTY - Producing bio-oil, comprises: (a) preparing a biomass feedstock; (b) performing pyrolysis of the feedstock in a reactor at a temperature of 250-420 degrees C; and (c) condensing the pyrolyzed feedstock with gas and then extracting.    USE - The method is useful for producing bio-oil including methyl tert-butyl ether, isopentyl acetate, 2-propylpentanoic acid and 1,2-dodecanediol, where the bio-oil is petrol or phytochemicals (all claimed).    ADVANTAGE - The method is capable of producing the bio-oil with high yield.
NOVELTY - Crystalline form of 1-( beta -D-glucopyranosyl)-4-methyl-3-(5-(4-fluorophenyl)-2-thienylmethyl)benzene is new.    USE - (I) is useful for treating diabetes mellitus, diabetic retinopathy, diabetic neuropathy, diabetic nephropathy, delayed wound healing, insulin resistance, hyperglycemia, hyperinsulinemia, elevated blood levels of fatty acids, elevated blood levels of glycerol, hyperlipidemia, obesity, hypertriglyceridemia, Syndrome X, diabetic complications, atherosclerosis and/or hypertension (claimed). No biological data given.    ADVANTAGE - (I) can be safely and economically prepared without using organic solvents in an environmentally friendly manner. The hydrates of (I) have good handling properties such as good isolation, drying, flow and compaction properties.    DETAILED DESCRIPTION - Crystalline form of 1-( beta -D-glucopyranosyl)-4-methyl-3-(5-(4-fluorophenyl)-2-thienylmethyl)benzene of formula (I) is new. INDEPENDENT CLAIMS are included for:    (1) the preparation of (I); and    (2) a combination comprising (I) and metformin.
NOVELTY - A deinking sludge is combusted in a combustion zone (3) to generate solid combustion product. Portion(s) of the solid combustion product is transferred from the combustion zone to a gasification zone. Carbonaceous material is gasified in the gasification zone (6), to generate fuel gas.    USE - Method for generating fuel gas is used for treating waste products generated during recycling of waste paper.    ADVANTAGE - The method thermochemically converts waste products generated during recycling of waste paper into generated fuel gas having high hydrogen content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (1) for generating fuel gas, which consists of combustion zone for combusting deinking sludge to generate solid combustion product, gasification zone for gasifying carbonaceous material to generate fuel gas, and transfer system (A) (8, 19, 10, 13) for transferring portion(s) of the solid combustion product from the combustion zone to the gasification zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for generating fuel gas.    System (1)    Combustor (2)    Combustion zone (3)    Gasifier (5)    Gasification zone (6)    Gasification fluidizing gas inlet (7)    Transfer system (8,10,13,17,19)
NOVELTY - The chemical sensor has a metal oxide sensing layer (11) arranged between two electrodes (26-1,26-2). The electrodes are arranged above and below the layer of metal oxide. The electrode arrangement is patterned to form a grid, fingers or a meandering line electrode. The pattern has a characteristic length in the order of the penetration depth of an analyte, preferably in 1 mu -50 mu . The electrode (26-1) is porous.    USE - Integrated metal oxide chemical sensor for a portable electronic device (claimed). Uses include but are not limited to a smart phone, a handheld computer, a laptop, an electronic reader, a tablet computer, a game controller, a pointing device, a photo or a video camera, or a computer peripheral.    ADVANTAGE - Reduces the distance between the electrodes and hence the thickness of the metal oxide layer to less than 10 mu or more preferably, to a range between 2 mu and 200 nanometer while retaining a large active area or volume within the metal oxide layer. The characteristic length is typically a lateral dimension of the area between two adjacent parts of the top electrode, thus ensuring that the gas molecules can migrate to the active sensor volume between the electrodes even when entering the surface of the metal oxide at a location midway between the two adjacent parts. Hydrogen gas is effectively suppressed, increasing the selectivity to less reactive gases such as e.g. methane. The structure of the upper electrode increases the selectivity of the sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a metal oxide gas sensor.    Metal oxide layer (11)    Complementary metal oxide semiconductor layer (13)    Heater (15)    Electrodes (26-1,26-2)
NOVELTY - A fuel, platform chemical or solvent from a fatty acid resource producing method involves heating the fatty acid resource in the presence of alkenes.    USE - Method for producing fuel, platform chemical or solvent, or producing a branched alkane and/or branched alkene from a fatty acid resource, biomass feedstock, and heavy oil    ADVANTAGE - The method enables producing higher grade fuel than the traditional biodiesels with higher yields of desirable products than pyrolysis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel or solvent produced by the method.
NOVELTY - The manufacturing method involves injection molding a frame gasket on a frame such that a first airtight portion of the frame gasket substantially covers a surface of the frame to maintain the shape of the frame gasket and a second airtight portion of the frame gasket projects upward and downward from both ends of the first airtight portion, the injection molding being performed independently from the formation of the gasket. The first airtight portion of the frame gasket is brought into contact with a second side of the separator (10) with the gasket formed on the first side.    USE - Manufacturing method for fuel cell separator with gasket.    ADVANTAGE - When the area of the edge of the separator is increased to reduce the deformation of the separator, which is caused by the pressure difference between the gasket materials being flowed through both sides of the separator, the power density of the fuel cell stack may be reduced, thus, burrs project from both sides of the second airtight portion, and thus the removal of the burrs can be automated using a burr removal tool or die cutter. The second airtight portion seals the recess formed between the edges of the separators such that the condensed water formed in the recess is prevented from being moved to the other unit cells, and thus it is possible to prevent the occurrence of short circuit and corrosion, which are caused when the condensed water formed in the recess is exposed to the outside, and improve the durability of the separator.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the method for manufacturing a separator with a gasket injection-molded on one side of the separator.    Separator (10)    First mold (11)    Upper mold (12)    Upper gasket molding groove (12a)    Lower mold (13)    Separator receiving groove (13a)    Gas side gasket (14)
NOVELTY - A method comprising: (a) providing a recombinant yeast host cell that expresses an engineered biosynthetic isobutanol pathway; (b) growing the recombinant yeast host cells in fermentation medium comprising suitable carbon substrates from renewable feedstocks; (c) extracting the bioproduced isobutanol from the fermentation medium with an isobutanol-selective liquid solvent, thus forming an isobutanol-containing organic phase; and (d) separating the bioproduced isobutanol from the isobutanol-selective liquid solvent to produce recovered isobutanol.    USE - The method is useful for producing isobutanol, and a fuel or fuel additive (claimed).    ADVANTAGE - The method is environment-friendly, cost-effective and produces isobutanol as a single product.    DETAILED DESCRIPTION - A method comprising: (a) providing a recombinant yeast host cell that expresses an engineered biosynthetic isobutanol pathway, where the engineered biosynthetic isobutanol pathway is encoded by heterologous genes, and where the engineered biosynthetic isobutanol pathway comprises an acetolactate synthase enzyme, a ketol-acid reductoisomerase enzyme, a dihydroxy-acid dehydratase enzyme, a branched chain keto acid decarboxylase enzyme, and an alcohol dehydrogenase enzyme, each of which are encoded by heterologous genes that lack a mitochondrial targeting sequence; (b) growing the recombinant yeast host cells in fermentation medium comprising suitable carbon substrates from renewable feedstocks, where isobutanol is bioproduced and where the cells grow during fermentation; (c) extracting the bioproduced isobutanol from the fermentation medium with an isobutanol-selective liquid solvent, thus forming an isobutanol-containing organic phase; and (d) separating the bioproduced isobutanol from the isobutanol-selective liquid solvent to produce recovered isobutanol; (e) blending the bioproduced isobutanol with a fossil fuel to make a fuel or fuel additive.
NOVELTY - Hexose sugar (22) is used to produce alkali metal levulinate, alkali metal valerate, alkali metal 5-hydroxy pentanoate, or alkali metal 5-alkoxy pentanoate. An anolyte comprising the obtained compound is prepared and the alkali metal levulinate, alkali metal valerate, alkali metal 5-hydroxy pentanoate, or alkali metal 5-alkoxy pentanoate is decarboxylated (70) to form radicals which are reacted to form hydrocarbon fuel compound.    USE - Manufacture of hydrocarbon fuel compound used as gasoline additive (claimed) and diesel fuel used for diesel engines.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining conversion process of biomass into hydrocarbon fuels.    Biomass (14)    Carbohydrates (18)    Hexose sugars (22)    Electrochemical decarboxylation (70)    Carbon dioxide (80)
NOVELTY - Upgrading (M) a hydrocarbon stream, comprises: providing the hydrocarbon stream comprising a deoxygenated pyrolysis product, where the hydrocarbon stream comprises a residual oxygen-containing compound content; and contacting the hydrocarbon stream with a solvent composition that has a greater affinity for oxygen-containing compounds over hydrocarbons.    USE - The method is useful for upgrading a hydrocarbon stream (claimed) which is useful as combustion fuel to generate electricity.    ADVANTAGE - The method reduces the residual oxygen-containing compound content of the hydrocarbon stream.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) upgrading (M1) a hydrocarbon stream, comprising: pyrolyzing a biomass feed to produce a pyrolysis product stream; contacting the pyrolysis product stream or its derivative with a solvent composition that has a greater affinity for oxygen-containing compounds over hydrocarbons; and separating an oxygenate-rich solvent composition from an upgraded hydrocarbon stream after contacting the hydrocarbon stream with the solvent composition; and    (2) an apparatus (10) for upgrading a hydrocarbon stream (20), comprising: a pyrolysis unit (12) for pyrolyzing a biomass feed (18) to produce a pyrolysis product stream; optionally, a deoxygenating unit for receiving the pyrolysis product stream and for deoxygenating the pyrolysis product stream; and an extraction unit (14), downstream of the optional deoxygenating unit, for receiving the hydrocarbon stream comprising a deoxygenated pyrolysis product and for extracting residual oxygen-containing compounds from the hydrocarbon stream.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of an for upgrading a hydrocarbon stream.    Apparatus (10)    Pyrolysis unit (12)    Extraction unit (14)    Biomass feed (18)    Hydrocarbon stream (20)
NOVELTY - Biodiesel biodegradable additive production involves mixing bio-oil, biodiesel and isopropyl acetate, and decanting polar phase comprising biodiesel, where the isopropyl acetate is separated from the formed phase.    USE - Method for producing biodiesel biodegradable additive for use as an biodiesel antioxidant (all claimed).    ADVANTAGE - The method produces biodiesel biodegradable additive that provides better oxidation stability, allows use of the most valuable fractions of bio-oil, and is stable and soluble in biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting improvement in oxidation stability in respect to the stability of biodiesel without additive. (Drawing includes non-English language text).
NOVELTY - The system includes stainless steel or other metals negative electrode and aluminum positive electrode for developing an electrolysis process, and a mixture of electrolyte and desalinated seawater. The electrolyte and desalinated seawater are mixed with sodium chloride, nitric acid, sodium hypochlorite or sodium hydroxide in similar equivalent. The hydrogen vapors are produced at cathode in electrolysis process, are collected by a compressor. The oxygen vapors are produced at anode in electrolysis process, are collected by another compressor.    USE - System for producing hydrogen, oxygen and electricity for use in automotive, railway, yachting, aviation and various other industries.    ADVANTAGE - The system produces hydrogen, oxygen and electricity in a simple and cost-effective manner by using renewable energy (solar and wind) and a mixture of desalinated seawater and various chemical components.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the electrolysis process. (Drawing includes non-English language text).
NOVELTY - A catalyst ink comprises catalyst-carrying carbon, first ionomer having first molecular weight, second ionomer having second molecular weight that greater than the first molecular weight, first solvent having first solubility parameter, and second solvent having second solubility parameter that greater than the first solubility parameter, where the catalyst ink is provided for forming catalyst layer of a membrane electrode assembly which has a microporous layer containing catalyst layer containing an electrolytic membrane, and a catalyst-carrying carbon and an ionomer, and carbon and a binder.    USE - Catalyst ink for forming catalyst layer of membrane electrode assembly that is utilized for manufacturing fuel cell (claimed).    ADVANTAGE - The ink suppresses oxidation of the carbon of a catalyst layer.    DETAILED DESCRIPTION - A catalyst ink comprises catalyst-carrying carbon, first ionomer having first molecular weight, second ionomer having second molecular weight that greater than the first molecular weight, first solvent having first solubility parameter, and second solvent having second solubility parameter that greater than the first solubility parameter, where the mass ratio of the first solvent and the second solvent is equal to ratio of the peak frequency of the molecular weight of the first ionomer in a distribution graph of the molecular weight of an ionomer, and the peak frequency of the molecular weight of the second ionomer, the catalyst ink is provided for forming catalyst layer of a membrane electrode assembly which has a microporous layer containing catalyst layer containing an electrolytic membrane, and a catalyst-carrying carbon and an ionomer, and carbon and a binder. An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell.
NOVELTY - Adjustment of slag property of biofuel in gasification process involves adding ashes of slag additive with flow temperature of 100K or more, preferably 100-150K which is below operating temperature of the melting chamber. The dynamic viscosity of slag additive in molten state at operating temperature of melting chamber is 25 Pa.second or more.    USE - Adjustment of slag property of biofuel e.g. coal, in gasification process used for producing synthesis gas.    ADVANTAGE - The method is economical, and provides high quality biofuel, by effectively separating the ash particles formed during the gasification process.
NOVELTY - The biomass gasifier (1) allows passage of the cyclone (6) for separating and removing the ashes contained in gas generated with reaction tube (22), while the scrubber (8) is provided for residue water vapor removal and for storing on a retention-of-gas tank (5). A piping (9) is provided between cyclone and reaction tube, such that the cyclone is covered with heat insulating material (16).    USE - Biomass gasifier for gasifying biomass of wood chip and paper garbage and generating clean high calorie gas used as fuel of gas engine for electric power generation.    ADVANTAGE - As the obstruction of collection unit of the ashes at cyclone lower portion is prevented, the ashes are collected stably and reliably, so that the production efficiency of generated gas is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass gasifier. (Drawing includes non-English language text)    Biomass gasifier (1)    Gasifier reaction installation (2)    Hot gas furnace (3)    Biomass supply apparatus (4)    Retention-of-gas tank (5)    Cyclone (6)    Gas cooler (7)    Scrubber (8)    Pipes (9,10)    Reaction tube (22)    Collection box (62)
NOVELTY - Preparation (M1) of teriflunomide (I) involves condensation of cyanoacetic acid (II) with 4-trifluoromethyl aniline (III) in presence of chlorinating agent to give 2-cyano-N-(4-(trifluromethyl)phenyl) acetamide (IV); followed by acetylation with an acetylating agent in presence of base (B1) and solvents (S1).    USE - For preparing teriflunomide (claimed) which is used for treating rheumatoid arthritis, autoimmune disease and multiple sclerosis.    ADVANTAGE - The present method is simple, cost effective, ecologically friendly, reproducible, useful on a commercial scale, and robust, to produce teriflunomide with high chemical purity; and avoids use of hazardous reagents like sodium hydride, high temperature and expensive coupling agent. The present method provides improved processes which not only reduces the number of steps, but also provides a safe and easy to operate at large scale.    DETAILED DESCRIPTION - Preparation (M1) of teriflunomide of formula (I) involves condensation of cyanoacetic acid of formula (II) with 4-trifluoromethyl aniline of formula (III) in presence of chlorinating agent to give 2-cyano-N-(4-(trifluromethyl)phenyl) acetamide of formula (IV); acetylation (IV) with an acetylating agent in presence of base (B1) and solvents (S1). An INDEPENDENT CLAIM is included for purification (M2) of teriflunomide involving providing a solution of teriflunomide in base (B2) and solvent (S2); separating aqueous and organic layers; acidifying aqueous layer with acid to obtain teiflunomide; optionally recrystallizing teriflunomide to afford pure teriflunomide.
NOVELTY - A synthesis gas is received at reactor tube having carbon nanotube from gasification/reforming step of liquid fuel production process. The carbon monoxide of synthesis gas is reacted with surface of carbon nanotube where oxygen functional groups act as catalyst, to remove oxygen from carbon monoxide using hydrogen in synthesis gas. Hydrogen is added to carbon, to form carbene moieties and water. Carbene is polymerized, to form longer hydrocarbon chains. Thus, conversion of carbonaceous materials to liquid fuels is enabled.    USE - Conversion of carbonaceous materials e.g. coal, biomass and natural gas to liquid fuels e.g. gasoline, diesel, jet fuel and kerosene.    ADVANTAGE - The method enables conversion of carbonaceous materials to liquid fuels with excellent conversion efficiency.    DETAILED DESCRIPTION - A synthesis gas is received at reactor tube having carbon nanotube from gasification/reforming step of liquid fuel production process. The carbon nanotube is produced by air-assisted chemical vapor deposition and has attached oxygen functional groups. The carbon monoxide of synthesis gas is reacted with surface of carbon nanotube where oxygen functional groups act as catalyst, to remove oxygen from carbon monoxide using hydrogen in synthesis gas. Hydrogen is added to carbon, to form carbene moieties and water. Carbene is polymerized, to form longer hydrocarbon chains. Thus, conversion of carbonaceous materials to liquid fuels is enabled. An INDEPENDENT CLAIM is included for system, which comprises a reactor tube having downstream which provides synthesis gas to the reactor from a gasification/reforming system block of a liquid fuel production system, a flow of synthesis gas in the reactor tube, carbene moieties and water formed in the reactor, and polymerized carbene.
NOVELTY - An irradiated Chlamydomonas reinhardtii strain M4013 (KCTC 18236P) having high lipid content, is new.    USE - The C.reinhardtii strain M4013 is useful for producing biodiesel (claimed).    ADVANTAGE - The irradiated C.reinhardtii strain has high lipid content (up to 30%) when compared to C.reinhardtii strains that are not irradiated.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) preparation method of the above-mentioned C.reinhardtii strain M4013; and (2) production method of biodiesel, involves (a) subjecting the above-mentioned C.reinhardtii strain M4013 to transesterification, or (b) obtaining lipid from the above-mentioned C.reinhardtii strain M4013 and subjecting the lipid to the transesterification.
NOVELTY - Production of reactive intermediates from biomass, comprises treating a biomass with a composition comprising a co-solvent mixture of aqueous tetrahydrofuran (THF) and an acid catalyst under conditions to produce a solid glucan-rich material, monomeric sugars, furfural, 5-hydroxymethylfurfural (5-HMF) and lignin products.    USE - The method is useful for the production of reactive intermediates (such as solid glucan-rich material, monomeric sugars, furfural, 5-HMF, lignin products and levulinic acid) from biomass (claimed), preferably lignocellulosic biomass including agricultural residues, wood, forestry wastes, sludge from paper manufacture and municipal and industrial solid wastes, where reactive intermediates are useful as platform chemicals for biological conversions and as drop in reagents for liquid transportation fuels such as ethanol, gasoline, jet and diesel range aromatic and hydrocarbon fuels.    ADVANTAGE - The method ensures stable, effective and large scale production of reactive intermediates from biomass with high yield and purity (greater than 99%) and improved selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method-I for the combined fractionation and catalytic conversion of biomass to produce reactive intermediates from biomass, comprising treating a biomass with a co-solvent mixture comprising THF, water and an acid catalyst under conditions to produce furfural, 5-HMF, levulinic acid, glucan-rich material and lignin;    (2) a system for the combined fractionation and catalytic conversion of biomass to produce reactive intermediates from biomass; and    (3) a composition comprising a biomass and a THF aqueous co-solvent.
NOVELTY - The method comprises (a) carrying out plasma treatment for mixed gas of methane, inert gases and water vapor, (b) performing carbon-hydrogen (C-H) bond decomposition for the plasma processed mixed gas in the presence of a catalyst, and (c) recovering the inert gas from the obtained reaction product through a separation film. The step (c) is performed after removing the water from the reaction product. The method further comprises removing nitrogen in the mixed gas prior to step (a), and controlling the gauge pressure of the separation film to 0-1 bar during the step (c).    USE - The method is useful for producing hydrogen and/or hydrocarbon having more than 2 carbon atoms (claimed).    ADVANTAGE - The method is capable of producing the hydrogen and/or hydrocarbon in an economical manner.    DETAILED DESCRIPTION - The method comprises (a) carrying out plasma treatment for mixed gas of methane, inert gases and water vapor, (b) performing carbon-hydrogen (C-H) bond decomposition for the plasma processed mixed gas in the presence of a catalyst, and (c) recovering the inert gas from the obtained reaction product through a separation film. The step (c) is performed after removing the water from the reaction product. The method further comprises removing nitrogen in the mixed gas prior to step (a), and controlling the gauge pressure of the separation film to 0-1 bar during the step (c). The steps are performed in a plasma reactor. The steps (a) and (b) are carried out in the presence of a catalyst. The reaction product of the step (b) comprises hydrogen, and hydrocarbons and their precursors. The reaction product further includes methane gas, which is circulated back to the plasma reactor. The ratio of inert gas/methane is 1:9. An INDEPENDENT CLAIM is included for an apparatus for producing hydrogen and/or hydrocarbon.
NOVELTY - The device has a first fermentation cylinder (3) whose upper end portion is set with a feed port. A second material circulation channel (15) is set with a storage bin door (17). One end of the hollow shaft is connected with speed reducer (7) and servo motor (6), and other end is connected with temperature and humidity regulating device (2) and air blower (1). The hollow shaft is set with a vent hole (22) and is welded with a spiral stir blade (12) whose one end is welded with a baffle plate (13).    USE - Alternating current servo controlled spiral enforced circulating type dual-drum organic fertilizer fermenting device.    ADVANTAGE - The organic fertilizer fermenting device accelerates the fermenting speed and increases the fermentation quality so as to perform uniform fermentation of the organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of organic fertilizer fermenting device.    Air blower (1)    Temperature and humidity regulating device (2)    First fermentation cylinder (3)    Servo motor (6)    Speed reducer (7)    Spiral stir blade (12)    Baffle plate (13)    Second material circulation channel (15)    Storage bin door (17)    Vent hole (22)
NOVELTY - The system has a conveying unit (1), a feeding device (2), a crushing device (5) and a ventilation device. The conveying unit is set with multiple groups consisting of a number of conveyors layered from low to high forming a three-dimensional installation. Each of the conveying unit group is equipped with a number of stations connected to a linear conveyor. Each group of the conveying unit is set with a crushing device. A material molding device (3) is mounted on the top portion of feed conveyor provided above the feeding device.    USE - Three-dimensional environment-friendly fermentation system.    ADVANTAGE - The fermentation efficiency of the three-dimensional environment-friendly fermentation system is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of environment-friendly fermentation system.    Conveying unit (1)    Feeding device (2)    Material molding device (3)    Material pre-crushing device (4)    Crushing device (5)
NOVELTY - The water treatment apparatus (500) has an aerobic tank (5) into which the effluent from an anaerobic tank (4) flows in. A water-quality-measurement unit (16) is provided to measure a parameter of nitrate nitrogen concentration of an influent and an effluent of anaerobic tank. The nitrate nitrogen concentration of the influent and effluent of anaerobic tank is computed from the water-quality-measurement unit. An air volume control unit (19) is provided to control the aeration air volume of nitrification tank (3) using the computed nitrate nitrogen concentration.    USE - Water treatment apparatus for removing nitrogen and phosphorus with activated sludge.    ADVANTAGE - The water treatment apparatus can obtain stable nitrogen using the denitrifying phosphorus accumulation microbe (DPAO). The phosphorus elimination is performed efficiently. The water treatment apparatus is provided for making the activity of DPAO and the treated water quality maintenance in anaerobic-anoxia-aerobic method more compatible. The nitrogen removal performance and the phosphorus elimination performance are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water treatment apparatus. (Drawing includes non-English language text)    Nitrification tank (3)    Anaerobic tank (4)    Aerobic tank (5)    Water-quality-measurement unit (16)    Air volume control unit (19)    Water treatment apparatus (500)
NOVELTY - A rutin quercetin is prepared by eliminating degraded enzyme of collected flower bud in steam at 100-120 degrees C for 10-15 minutes, taking out bud and steam drying, crushing, performing diacolation, percolating solution of filter slag, obtaining crude extract, adding flocculation agent to crude extract at ratio of 1-5 g:100 L, lightly stirring flocculation agent to uniformly distribute to crude extract, standing for 20-40 minutes, separating and removing precipitate and impurity, adding antioxidant, complexing agent, and mixed acid solution, hydrolyzing, cooling, precipitating, and separating.    USE - Preparation of rutin quercetin (claimed).    ADVANTAGE - Preparation process shortens process flow, reduces production cost and pollution, saves energy, and increases conversion rate of raw materials.    DETAILED DESCRIPTION - A rutin quercetin is prepared by eliminating degraded enzyme of collected flower bud in steam at 100-120 degrees C for 10-15 minutes, taking out bud and steam drying, crushing, performing diacolation, percolating solution of filter slag, obtaining crude extract, adding flocculation agent to crude extract at ratio of 1-5 g:100 L, lightly stirring flocculation agent to uniformly distribute to crude extract, standing for 20-40 minutes, separating and removing precipitate and impurity, adding antioxidant into solution, adding complexing agent, controlling pH to 3-5 by adding mixed acid solution, obtaining acid liquid, hydrolyzing acid liquid at 150-200 degrees C and 0.05-0.75 MPa for 0.5-2.5 hours, obtaining mixed liquid, cooling to 20-30 degrees C, precipitating quercetin, and separating in which ratio of mixed liquid and water is 1 L:20-30 L.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of rutin quercetin. (Drawing includes non-English language text).
NOVELTY - A teprenone is prepared by mixing geranyllinalool, 5-acetyl-2,2-dimethyl-(1,3)dioxane-4,6-dione, and aluminum isopropoxide with molar ratio of 1:1.2-1.5:0.02-0.1, dissolving in p-xylene solvent, warming at 150-160 degrees C, refluxing for 6-10 hours, cooling, removing solvent, washing, extracting, combining organic layer, drying to obtain crude product, performing molecular distillation, removing impurity, performing vacuum distillation, and removing impurity.    USE - Preparation of teprenone (claimed).    ADVANTAGE - Preparation process is simple, easy to control, and reduces reaction by-product. Product is safe and has high conversion rate, high purity, and stable quality.
NOVELTY - Active sludge preparation involves taking plant ash (100g), and using concentrated sulfuric acid (20ml) for maintaining pH of the plant ash less than or equal to 6. Straw (250g) is crushed, and then added to the sludge (1kg) to obtain a mixture.    USE - Method for preparing active sludge for use as fertilizer for agricultural (claimed).    ADVANTAGE - The method enables preparing active sludge in an eco-friendly manner.
NOVELTY - A biological organic fertilizer comprises 45-55 wt.% cow dung, 25-35 wt.% corn straw, 5-15 wt.% sesame straw, 2-8 wt.% cowpea straw, 2-8 wt.% wheat bran, and 0.01-0.1 wt.% biological bacteria. The biological bacteria comprise cell membrane bacteria and biological membrane bacteria at mass ratio of 2:1. The cow dung is fresh cow dung with 50-60 wt.% water content. The cowpea, sesame straw and corn straw are dried and crushed into 1-3 cm filaments.    USE - Biological organic fertilizer used for early spring greenhouse (claimed) in maintaining normal growth of crops.    ADVANTAGE - The fertilizer is easy to use, has good formulation, and can be stored for more than 2-3 years. The method is easy and simple with rapid fermentation at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological organic fertilizer comprising composting for 28-32 hours, mixing water, brown sugar and biological agents at mass ratio of 100:5:1, stirring to dissolve brown sugar, standing for 22-26 hours, mixing with wheat bran, covering with film, standing for 5-7 hours, turning layers of cow dung, cowpea, sesame straw and corn straw at 10-15 cm, wheat bran and biological agent at 0.5-1 cm thick and compost layer at 0.8-1.2 cm thickness, covering with film, fermenting for 3-5 days, piling at 1.3-1.7 m wide and 1.8-2 2 m long, adding 2-3 vent holes per m2, fermenting for 10-15 days until odorless, shredding, and granulating to obtain product with moisture content of 20-30%.
NOVELTY - Manufacturing soilless culture substrate involves mixing raw material in certain amount to obtain a mixture, maintaining water content of the mixture to 20-30% for 7-8 days, and then adding urea, ammonium phosphate and potassium sulfate to the mixture. The mixture is fermented to obtin the desired product.    USE - Method for manufacturing soilless culture substrate (claimed).    ADVANTAGE - The method enables manufacturing soilless culture substrate with high fertility in an eco-friendly manner.
NOVELTY - Manufacture of flower substrate comprises mixing biogas residue, grass material, straw and lime to obtain compost matrix, adding water, keeping moisture to 50%, composting, regularly turning while controlling moisture and temperature, adding fertilizer additive, mixing, aging, sampling, powdering or granulating, and packaging.    USE - Method for manufacture of flower substrate (claimed).    ADVANTAGE - The method is easy and environment-friendly, and it has wide raw material source and short fermentation time.
NOVELTY - Fertilizer comprises (in pts.wt.): peanut oil (20-35), cottonseed cake (25-32), bean cake (8-15), micro-fertilizer (2-4), colza cake (35-50), effective microorganisms (0.5-2) and food debris (20-30).    USE - Fertilizer for plant (claimed).    ADVANTAGE - The fertilizer ensures reduced pollution and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing fertilizer, which involves:    (A) crushing and mixing corn straw, peanut oil, bean cake, cotton seed cake and colza cake and effective microorganisms to obtain a mixture; and    (B) fermenting the mixture at 25-35 degrees C for 10-15 days.
NOVELTY - Preparation of composite microorganism fertilizer comprises crushing ammonium sulfate, adding bioorganic fertilizer, mixing, sieving through 18-mesh sieve to obtain 10% total nutrient-containing fertilizer, granulating through disk pelletizer, and composting to not greater than 50 degrees C until moisture content is 20% or less.    USE - Method for preparation of composite microorganism fertilizer used for promoting growth and increasing yield of eggplants and tomatoes (all claimed).    ADVANTAGE - The fertilizer is convenient to use, and it has long lasting effect and synergistic function in promoting growth of crops, and low cost.
NOVELTY - Strawberry culture substrate preparation comprises mixing rice bran, sawdust, pig fermentation bed waste, dairy manure and coir, and crushing; stacking crushed powder, controlling water content at 30-35%, and fermenting at 60-70 degrees C while regularly turning; adding fertilizer to fermentation product; and inspecting quality, reprocessing unqualified product, and pressing qualified product into 30 cmx 30 cm blocks.    USE - Method for preparing culture substrate used for soilless cultivation of strawberries (claimed).    ADVANTAGE - The method is fast and no pollution. The culture substrate is convenient to use and has wide material source, stable quality and low cost.
NOVELTY - Environment-friendly light nutritional substrate comprises 45-55 wt.% sawdust, 9-14 wt.% coconut husk, 4-9 wt.% reed residue, 4-9 wt.% bagasse, 4-9 wt.% corn cob grain, 9-14 wt.% rice hulls, 3-7 wt.% peanut shells, 3-7 wt.% traditional Chinese medicine dregs, 4-9 wt.% perlite, 4-9 wt.% fly ash, 0.1-0.5 wt.% potassium dihydrogen phosphate, 0.1-0.5 wt.% urea and 0.1-0.3 wt.% fermentation bacteria.    USE - Environment-friendly light nutritional substrate used for soilless cultivation (claimed).    ADVANTAGE - The product is rich in nutrients and has long fertilizer effect and good moisture retention and air permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environment-friendly light nutritional substrate comprising mixing peanut shells, sawdust, coconut husk, reed residue, bagasse, corn cob grain, rice hulls, traditional Chinese medicine dregs, perlite and fly ash, carrying out UV disinfection, mixing to obtain base material, dissolving potassium dihydrogen phosphate and urea in water, adding base material, placing in fermenting tank, coating with film base material, mixing, adding fermentation bacteria, fermenting in pressure reactor and drying.
NOVELTY - A multi-component slurry comprises 4-38 mass% sludge, 35-66 mass% carbon-containing substance, 18-38 mass% water, 0.2-1.6 mass% auxiliary agent and 0.02-0.1 mass% additive. The additive is chosen from 10-40 mass% sodium polyacrylate with average molecular weight of 2000-5000 Da, 25-70 mass% sulfonated melamine formaldehyde resin and 5-35 mass% sodium hexametaphosphate. The auxiliary agent is chosen from 60-80 mass% sulfonated castor oil and 20-40 mass% nonylphenol polyoxyethylene ether.    USE - Multi-component slurry.    ADVANTAGE - The multi-component slurry is harmless, and has concentration of not less than 62%, viscosity of less than 1200 mPa. seconds, good fluidity and no hard precipitation production for 40 days, and meets requirements for producing synthetic gas, reduces sludge treatment cost, reduces recycling sludge treatment and reduces consumption amount of carbon-containing substance to achieve rational use of resources in production of synthetic gas.    DETAILED DESCRIPTION - A multi-component slurry comprises 4-38 mass% sludge, 35-66 mass% carbon-containing substance, 18-38 mass% water, 0.2-1.6 mass% auxiliary agent and 0.02-0.1 mass% additive. The additive is chosen from 10-40 mass% sodium polyacrylate with average molecular weight of 2000-5000 Da, 25-70 mass% sulfonated melamine formaldehyde resin and 5-35 mass% sodium hexametaphosphate. The auxiliary agent is chosen from 60-80 mass% sulfonated castor oil and 20-40 mass% nonylphenol polyoxyethylene ether. The distribution granularity of 100% of the slurry is less than 14 meshes, 98-100% of the slurry is less than 20 meshes, 90-98% of the slurry is less than 40 meshes, 50-60% of the slurry is less than 120 meshes, 40-45% of the slurry is less than 200 meshes, and 25-35% of the slurry is less than 325 meshes.
NOVELTY - Manufacture of bark compact biofuel involves collecting rough bark, screening to diameter of 0.8-20 cm, pulverizing the bark to particle size of less than 0.8 cm, drying the crushed bark particles at 150-170 degrees C using air-dryer such that the moisture content is less than 16%, performing desulfurization process, transporting the dried particles using belt conveyors to an extruder, extruding the bark particles at 180-200 degrees C and packaging.    USE - Manufacture of bark compact biofuel used for coal-fired boiler.    ADVANTAGE - The method enables efficient and economical manufacture of bark compact biofuel with high quality, excellent productivity, density of more than 1.1 ton/m3, heat value of more than 4500 kcal/kg, moisture content of 10% or less, sulfur content of less than 0.15%, burning rate 95% or more and thermal efficiency of 85% or more.
NOVELTY - A Winogradskyella sp. strain DL5-3 with preservation number CGMCC No. 9012 for petroleum degradation is new.    USE - Winogradskyella sp. strain DL5-3 with preservation number CGMCC No. 9012 for petroleum degradation, oil-containing wastewater, and biological strengthening treatment and repair of bodies of water and soil having petroleum pollution (all claimed).    ADVANTAGE - The strain efficiently degrades petroleum hydrocarbon and strengthens treatment and repair of body of water and soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of strain for petroleum hydrocarbon contaminant degradation in which petroleum pollutant exists when low hydrocarbon component is present.
NOVELTY - Method for producing biodiesel using Haematococcus pluvialis microalgae, involves culturing algae in photobioreactor until logarithmic growth phase is reached, performing rapid propagation of motile algal cells, obtaining biomass, where the natural astaxanthin and bio-energy grease are rapidly accumulated in high amount, and centrifuging biomass to obtain accumulated product.    USE - The method is useful for producing biodiesel using H.pluvialis microalgae (claimed).
NOVELTY - This utility new type relates to a one by magnetotactic bacteria absorbing heavy metal of a device, the device by mixed liquid pour, ultrasonic pour, three filter part is composed of a pour liquid mixing set with a liquid sample inlet, stir device, waste liquid inlet and magnetic field generator, magnetotactic bacteria culture liquid with strain absorbing fixing treatment of a waste liquid mix rear stir absorbing, magnetic field generator by the rear a heavy metal of, adding a little clean water eluting adsorbed cells entering into ultrasonic pour, pour ultrasonic set with ultrasonic probe, after bacteria removing liquid entering into ultrasonic pour opening for a body proceed ultrasonic crushing, ultrasonic crushing processing absorbing bacteria liquid of a heavy metal entering into filter, breaking cells trapped in the filter bag of filter, high concentration of heavy metal waste liquid by a valve. This utility new type is suitable for various industrial waste in water of a heavy metal recovery, small floor area, a capacity is strong, and it has strong application prospect.
NOVELTY - This new utility model claims have one mode type of livestock and poultry cultivation waste water harmless resource processing system, from waste collection device collecting metering after, by vacuum suction filtration automatic water outlet integrated device for solid liquid separation, malodorous gas and back through the vacuum pump enter into tail gas and purification device discharge. Built-in solid waste salt dissolving tank through solid liquid separator and separating out the transport device after discharging, enter into dry fermentation device by dry fermentation, biogas generated by collecting after purification as light fuel, generated as organic fertilizer using biogas residue. After solid liquid separating the liquid with the dry fermentation product of liquid to enter into flow Anaerobic fermenter, marsh gas generated by fermentation and Anaerobic dry fermentation when producing the marsh gas collecting to, after purification as light energy, Anaerobic fermentation produced biogas slurry enter into horizontal undercurrent artificial wetland and vertical flow artificial wetland for treatment, at last back by chlorine dioxide sterilizing system for processing, conversion is in water as livestock and poultry house ring washing water circulation use. One big the system solves the problem of livestock and poultry cultivation waste water treatment and, in protecting environment and at the same time, realize the recycling using waste.
NOVELTY - This utility new type relates to a one liquid organic fertilizer production device, belonging to the field of environmental device field. The structure is: a stirrer, a sterilizing natural ferment storage tank, a normal temperature water tank, a first filter, a secondary fermentation tank, a second filter, a micro-generating bacteria feeding fermenting tank and a finished product tank connected in turn, the stirrer, sterilizing fermenting naturally storage tank and secondary fermentation tank are respectively connected with an air supply device through the pipeline, wherein said stirrer, the normal temperature water tank, the first filter and the micro-generating bacteria feeding fermenting tank are respectively connected with water supply device through the pipeline. The advantages are: simple structure, convenient use, low cost and good effect. The device can be made according to the custom needs, in the later building, only need simply adding the device to finish the professional system of the output. It not only meets the requirement of environmental protection department, and processes the waste in real time, but also improves the environmental sanitation, changes waste into treasure and increases benefit for enterprise.
NOVELTY - A device comprises electrolytic groove (1), anode pole (2), cathode pole (3), supplying water box (17), and solvent supply tank (19). The device further comprises gas-water separator, pressurizing pump, one-way valve, gas storage room, first gas channel, and second air passage.    USE - Device used for generating hydrogen-oxygen gas (claimed).    ADVANTAGE - The device does not need fuel oil or gas, solves problem such as energy shortage, and has no tail gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of device.    Electrolytic groove (1)    Anode pole (2)    Cathode pole (3)    Supplying water box (17)    Solvent supply tank (19)
NOVELTY - This utility new type claims a furnace of a rotate one removal of biomass gasification furnace, comprise a furnace body, a furnace body set with inner burning biomass granule of furnace cavity, furnace cavity lower part is set with ash discharging space set with a furnace gate at the end opening lower furnace cavity, the furnace gate by several furnace parallel combination is formed along the axial direction arrangement with a flat head teeth and sharp teeth, a flat head teeth and sharp teeth spaced arrangement of a furnace, each furnace around its own axis of a synchronous rotate, making time rotate to flat head teeth relative the to reduce a gap between the furnace bar supporting a biomass to a inner furnace cavity, ash discharging time rotate furnace, a joint rear tip teeth of the furnace ash crushing and discharging to discharge inner space, after recovering to the flat head teeth. This utility new type of biomass gasification furnace can smoothly discharge and slag, increase the pneuma production efficiency, reduces the energy waste, one is a significant innovation in preparing fermentable reducing sugar from biomass pneuma.
NOVELTY - This utility new type claims a furnace of a rotate one removal of biomass gasification furnace, comprise upper furnace body and lower furnace body, a furnace body set with inner furnace cavity, furnace chamber and the lower furnace burning biomass granule of connected, set with a furnace gate, furnace grid by multiple parallel combination is formed by furnace end opening at the lower furnace cavity, the furnace gate is set on the lower body upper along axial direction arrangement with a flat head teeth and sharp teeth, a flat head teeth and sharp teeth spaced arrangement of a furnace, each furnace around its own axis of a synchronous rotate, making time rotate to flat head teeth relative the to reduce a gap between the furnace bar supporting a biomass to a inner furnace cavity, ash discharging time rotate furnace, pointed teeth the furnace ash crushing and discharging to lower inner furnace body, rear discharge is finished to a flat head of the teeth. This utility new type of biomass gasification furnace can smoothly discharge and slag, increase the pneuma production efficiency, reduces the energy waste, one is a significant innovation in preparing fermentable reducing sugar from biomass pneuma.
NOVELTY - A three-dimensional (3D) particle preparation method involves immersing graphite in deionized water for 30-60 minutes, and subjecting the graphite to ultrasonic cleaning at 20-40 degrees C and dispersing in ethanol. The dispersion is dried in an oven and added with 60 wt.%. The product is heated in water bath at 60-80 degrees C, while adding ethanol dropwise. The product is stirred with PTFE particles and extruded into particle having size of 2-3 mm followed by drying product at 80 degrees C and removing ethanol residue.    USE - Method for preparing 3D particle of graphite-PTFE cathode for synthesis of hydrogen peroxide in a microbial fuel cell.    ADVANTAGE - The method enables preparing the 3D particle of graphite-PTFE cathode with high mass transfer efficiency and increased yield of hydrogen peroxide.
NOVELTY - Planting of cucumber comprises selecting seedling, selecting soil, preparing plating field, planting seedling, covering with film, carrying out planting management, and harvesting. The planting field is prepared by digging planting field in row position, spreading fermented straw on ditch, homogenously dispersing straw beneficial microflora, scattering straw vaccine, shoveling with soil, watering, fermenting for 2-3 days, leveling to keep 15 cm straw on soil, and punching on hole of soil layer.    USE - Method for planting cucumber (claimed).    ADVANTAGE - The method reduces fertilizer dosage and planting cost and increases quality and yield of cucumber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fermented straw comprising mixing 2-3 wt.% composite strain, 48-67 wt.% wheat bran straw, and 30-50 wt.% cake fertilizer, adding water, holding humidity to 60-70%, standing for 1 day, where mass ratio of composite strain to straw is 1-3:1000, mixing, crushing straw, holding material humidity to 60-70%, stacking at not greater than 2 m high, and fermenting for 5-7 days, where composite strain comprises 8 pts. wt. fibrous slime molds, 4 pts. wt. fibrous Bacillus, 3 pts. wt. high temperature fibrous Aeromonas, 3 pts. wt. fibrous Vibrio, and 36 pts. wt. aerobic yeast.
NOVELTY - A molding apparatus comprises molding part (10) which compresses and molds particle raw material (x), heating part (20) which heat-processes compression-molded raw material by heat-tracing unit (21), cooling unit (30) which cools raw material heat-processed in heating part, communication part (40) provided so that center part of molding part and heating part may be connected, and internal heating unit (41) to heat raw material in heating part from inner side to communication part.    USE - A molding apparatus for production of biomass coke.    ADVANTAGE - Dispersion of particle raw material in molding apparatus can be prevented, and particle raw material can be appropriately molded, cooled, and heated over a short period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of the molding apparatus.    Molding part (10)    Heating part (20)    Heat-tracing unit (21)    Cooling unit (30)    Communication part (40)    Internal heating unit (41)    Raw material (x)
NOVELTY - Producing watermelon using soilless cultivation medium comprises (i) mixing corn stalks, clinker, mushrooms waste and biogas, crushing, (ii) stacking the pulverized powder, adding urea, and fermenting until the moisture content reaches 50%, and regularly monitoring the moisture content in the compost; (iii) adding fertilizer and sterilizing agent into the fermentation product, and ripening for a month; (iv) inspecting the quality of ripe hyphae, crushing and sieving or pressing into a loose matrix blocks, and using the substandard product as raw materials for re-processing.    USE - The method is useful for producing watermelon using soilless cultivation medium (claimed).    ADVANTAGE - The method uses rich raw material source. The matrix has stable quality, is suitable for growing, convenient for transplantation, pollution-free, economical, and fast production rate.
NOVELTY - A hydrogen production system comprises hopper (2), pressure-proof reactor (1) and purification device (3) which are sequentially connected; pressure pump (10) and regulator valve (9) connected in parallel with the hopper; and precipitate separation and solution recovery device (6) including filter screen and circulation pump. The pressure-proof reactor and precipitate separation and solution recovery device form a circulation loop.    USE - System used for hydrogen production by hydrolysis of magnesium or aluminum salt solution in the presence of nano metal powder (claimed).    ADVANTAGE - The system improves water utilization rate, thus, increasing hydrogen content of system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen production device.    Pressure-proof reactor (1)    Hopper (2)    Purification device (3)    Precipitate separation and solution recovery device (6)    Regulator valve (9)    Pressure pump (10)
NOVELTY - Production of organic fertilizer comprises mixing sheep, cattle, pig, chicken, duck and goose dung, adding crop straw, mixing, spraying, fermenting for 3 months, crushing, sieving, mixing, granulating and packaging.    USE - Method for producing organic fertilizer (claimed).
NOVELTY - Preparation of disease-resistant corn special fertilizer includes mixing raw materials including rapeseed and wheat bran with water in fermentation tank, adding Bacillus subtilis, pre-fermenting, covering tank with yellow soil, and fermenting to obtain fermented material; melting urea, adding ferrous sulfate, monoammonium phosphate, diammonium phosphate, boric acid, potassium chloride, zinc sulfate, potassium magnesium fertilizer and ammonium molybdate, and mixing fermented material; and adding with medical stone, charcoal, oil shale ash and attapulgite powder, crushing, and sieving.    USE - Method for preparation of disease-resistant corn special fertilizer (claimed).    ADVANTAGE - The fertilizer increases lodging capacity of corn, improves soil physicochemical property and fertility, and satisfies nutrition element needed for corn's growing period.    DETAILED DESCRIPTION - Preparation of disease-resistant corn special fertilizer comprises (A) adding rapeseed, wheat bran, ash, animal manure and pond mud into fermentation tank, mixing with water until water content of mixture is 24-27%, adding Bacillus subtilis, pre-fermenting for 5-8 days to obtain pre-fermented material, covering tank with 13-15 wt.% yellow soil, and fermenting for 15-20 days to obtain fermented material; (B) melting 20-40 pts. wt. urea, adding 1.5-3 pts. wt. ferrous sulfate, 1-3 pts. wt. monoammonium phosphate, 2-4 pts. wt. diammonium phosphate, 1-2 pts. wt. boric acid, 0.5-1.3 pts. wt. potassium chloride, 1.5-2.5 pts. wt. zinc sulfate, 1.2-1.7 pts. wt. potassium magnesium fertilizer and 0.25-0.5 pts. wt. ammonium molybdate, mixing, cooling, placing into mixer, and adding 30-50 pts. wt. fermented material to obtain first mixture; and (C) mixing 35-45 pts. wt. first mixture with 4-6 pts. wt. medical stone, 2-5 pts. wt. charcoal, 1-3 pts. wt. oil shale ash and 1-3 pts. wt. attapulgite powder, crushing, and sieving through 100-200 mesh sieve.
NOVELTY - A biofertilizer comprises 600-800 pts. wt. sodium humate, 200-400 pts. wt. amino acid raw powder, 5-10 pts. wt. Bacillus subtilis, and 1-5 pts. wt. sodium silicate.    USE - Biofertilizer used for controlling water moss (claimed).    ADVANTAGE - The biofertilizer kills moss, decomposes organic material, cultivates beneficial algae, has low cost, and is environment-friendly, pollution-free, biodegradable and simple to prepare and use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofertilizer preparation by uniformly premixing sodium silicate and B. subtilis; and sequentially adding sodium humate, amino acid raw powder and premixed material to a reactor, uniformly stirring for 20-30 minutes, crushing, passing through 100-mesh sieve, and packaging.
NOVELTY - An environment-friendly biomass wood pellet fuel contains pine sawdust and hard sawdust.    USE - An environment-friendly wood biomass pellet fuel (claimed).    ADVANTAGE - The biomass wood pellet fuel is energy-saving and environment-friendly, and has improved heat of combustion, combustion rate, and thermal efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environment-friendly biomass wood pellet fuel which involves crushing raw materials, mixing according to proportion, drying, and extruding to obtain pellets.
NOVELTY - The biomass wood pellet production equipment includes a sawdust crusher (2), a drier (3), and an extrusion molding, where material room is designed between the dryer and extrusion molding for transforming wooden raw material. A dust remover is designed with the material room.    USE - Biomass wood pellet production equipment.    ADVANTAGE - The biomass wood pellet production equipment produces the biomass wood pellet with high combustion rate and heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass wood pellet production equipment.    Shaker (1)    Sawdust crusher (2)    Drier (3)    Ton material (4)    Extruded pellet mill (5)
NOVELTY - This utility new type provide the one from biogas in a removing of constant-temperature absorbing device, include absorption tower, a regeneration tower, an absorption tower lower part a conveying gas of fan, the bottom of the top of regeneration tower, a regeneration tower bottom set with an electric heater, and pump through a tower top part of the regeneration tower is also a decarburization solution storage tank through a valve group, a return pump, and it further comprise air blower, a pneuma pneuma heat exchanger and the spiral electric heater, a regenerating tower bottom of a stay lower area part. The device a no vapour constant temperature of decarburization solution absorption and regeneration, the cost is low, operation cost is low, a high utilization rate of the absorption purifying marsh gas of application;
NOVELTY - Preparation of activated carbon propane adsorbent involves: leaching coconut shell active carbon to concentration of 5-22 mol/l of hydrofluoric acid solution, putting in a hydrothermal reaction kettle at 120-180 degrees C with hydrothermal process for 17 days, washing, drying, obtain activated carbon propane adsorbent.    USE - For preparation of activated carbon propane adsorbent which is used in hydrocarbon purification treatment applications (all claimed).    ADVANTAGE - The purification material with low concentration for HC (hydrocarbon) purification efficiency is high, with low cost, with simple preparation technology. The method provides condition of 20 ppm propane concentration, with 50000 ml/g/hour airspeed, the material of the highest propane at normal temperature and normal pressure, purification efficiency of more than 99%, and absorbing capacity reach to 2 ml C3H8/g AC.
NOVELTY - Titanium alkoxide and hydrochloride salt of molybdenum in a molar ratio of 7:3 are mixed to obtain mixture (a). Stearic acid is added and mixed. Obtained mixture is dissolved in n-propanol, stirred, heated at 90-260 degrees C for 0.2-3 hours, calcined at 500-800 degrees C for 1-10 hours in a hot crucible, cooled, and ground to 80-100 mesh, to obtain mesoporous solid acid catalyst. The molar ratio of mixture (a) and stearic acid is 1:4-1:6.    USE - Preparation of mesoporous titanium-molybdenum solid acid catalyst used in esterification reaction during production of biodiesel fuel (claimed).    ADVANTAGE - The method enables preparation of mesoporous titanium-molybdenum solid acid catalyst having high catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of mesoporous solid acid catalyst in esterification reaction during production of biodiesel fuel.
NOVELTY - Bacillus megaterium ZH5 strain is deposited in China microorganism strain preservation management committee under accession number (CGMCC NO.8802), and is new.    USE - Bacillus megaterium ZH5 strain used for promoting growth of peanut plant in the red soil region (claimed) and used in fertilizer.    ADVANTAGE - The Bacillus megaterium ZH5 strain can sustain in highly acidic, alkaline and high phosphorus content environment. Bacillus megaterium ZH5 strain enables to promote peanut growth by increasing the quality of red soil by enhancing the utilization rate of fertilizer by red soil.
NOVELTY - The reaction tank comprises a semi-spiral-shaped main body divided into six layers. An inner part of the reaction tank is set with fillers. A lower part of the reaction tank is set with a water inlet. An upper part of the reaction tank is set with a water outlet and a baffle. The filler is biological filler and is distributed in the reaction tank. One end of the baffle is fixed on an inner wall of the reaction tank.    USE - The reaction tank is useful for treating sewage (claimed).    ADVANTAGE - The reaction tank is simple in structure, and rapidly treats the sewage with increased efficiency.
NOVELTY - Preparation of ammoniacal nitrogen canal matrix used for agricultural non-point source pollution control, involves mixing treated sand and 20-30 wt.% meadow brown soil, mixing into activated sludge, adding coal slag, and inoculating mixture with Paracoccus denitrificans culture broth.    USE - Method for preparing ammoniacal nitrogen canal matrix used for agricultural non-point source pollution control.    ADVANTAGE - The canal matrix has good absorption property, and promotes complete purification and complete degradation of ammoniacal nitrogen.
NOVELTY - Organic composite matrix comprises waste vegetable and dairy manure in weight ratio of 3:2.    USE - Organic composite matrix.    ADVANTAGE - The organic composite matrix is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite matrix, which involves:    (A) mixing grain, dairy manure, vinasse and beer (derived from by-product of white wine) to obtain a mixture;    (B) crushing the mixture, and then removing impurities from the crushed material;    (C) adding urea to the mixture, and the adding quicklime for regulating pH value to 5.5-8.0;    (D) adding fermenting agent to the mixture, and then processing the mixture at 60-65 degrees C; and    (E) adding nitrogen, phosphorus pentoxide and potassium oxide to the mixture to obtain the desired product.
NOVELTY - Synthesis of 2-tert-butyl-p-cresol involves alkylating cresol using alkylating agent under atmospheric pressure conditions in presence of modified Y zeolite-NaY zeolite catalyst formed by performing ion-exchange process of ammonium chloride, manganese nitrate, lanthanum nitrate or cerium nitrate.    USE - Synthesis of 2-tert-butyl-p-cresol (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables efficient synthesis of 2-tert-butyl-p-cresol with high conversion ratio, and excellent selectivity, by simple method.
NOVELTY - Preparation of thiobarbituric acid derivative (I) comprises reacting thiourea and malonic acid derivative (II) in organic solvent, adding aluminum isopropoxide and reacting.    USE - Method for preparing thiobarbituric acid derivative (claimed).    ADVANTAGE - The method is easy, environment-friendly and high=yield.    DETAILED DESCRIPTION - Preparation of thiobarbituric acid derivative of formula (I) comprises reacting thiourea and malonic acid derivative of formula (II) in organic solvent, adding aluminum isopropoxide and reacting.    R1=H, methyl, ethyl or nitro; and    R2,R3=ethyl or methyl.    An INDEPENDENT CLAIM is included for the production device comprising reaction kettle (1), filter groove (2), acidification tank (3), vacuum dryer (4), organic solvent recovery tank (5), waste liquid pool (6) and pipeline (7).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of production device.    Reaction kettle (1)    Filter groove (2)    Acidification tank (3)    Vacuum dryer (4)    Organic solvent recovery tank (5)    Waste liquid pool (6)    Pipeline (7)
NOVELTY - 4-aminomorpholine from 4-nitrosomorpholine is synthesized by adding 4-nitrosomorpholine into closed neck bottle, using carbon dioxide aeration device with gas flowmeter, adding water and ammonium chloride, stirring and starting system through carbon dioxide gas, aerating at 30-50 degrees C, adding palladium/carbon reducing agent, adding zinc powder while maintaining temperature to 30-50 degrees C, continuously reacting, performing gas chromatography (GC) detection, stopping ventilation, filtering and washing, combining filtered liquid into distillation bottle, and decompressing and distilling.    USE - Synthesis of 4-aminomorpholine from 4-nitrosomorpholine for 1-amino piperazine (claimed).    ADVANTAGE - Synthesis process is environment-friendly, increases security, avoids organic reagent, and reduces production cost, and product has high yield.    DETAILED DESCRIPTION - 4-aminomorpholine from 4-nitrosomorpholine is synthesized by adding 4-nitrosomorpholine into closed neck bottle, using carbon dioxide aeration device with gas flowmeter, adding water and ammonium chloride, stirring and starting system through carbon dioxide gas, aerating at 30-50 degrees C, adding palladium (Pd)/carbon (C) reducing agent to system, adding zinc (Zn) powder to system while maintaining temperature to 30-50 degrees C, continuously reacting, performing gas chromatography (GC) detection of 4-nitrosomorpholine, stopping ventilation, filtering Pd/C and Zn slag with water and washing solid slag once, combining filtered liquid into distillation bottle, decompressing 1st water evaporating in reaction system, and decompressing and distilling collection at 64-72 degrees C/15mmHg fraction in which product is white solid and normal chromatographic content is 97-99%.
NOVELTY - Sodium aspoxicillin is prepared by performing carboxyl group monomethyl esterification on D-aspartic acid in thionyl chloride and methanol mixed solution to obtain D-aspartic acid methyl ester hydrochloride, performing methyl amination reaction in methylamine aqueous solution, reacting with ethyltrifluoroacetate in methanol/triethylamine mixed solution, reacting with carbonyldiimidazole (CDI) to obtain active mixed anhydride, performing condensation reaction with amoxicillin triethylamine salt to obtain reaction solution, and adding methanol.    USE - Preparation of sodium aspoxicillin (claimed).    ADVANTAGE - Preparation of sodium aspoxicillin is simple, stable, low-cost, environment-friendly, and easy to control, has high product purity and yield, mild reaction condition, and large safety coefficient, and uses low-cost raw materials.    DETAILED DESCRIPTION - Sodium aspoxicillin of formula (I) is prepared by performing carboxyl group monomethyl esterification on D-aspartic acid in thionyl chloride and methanol mixed solution to obtain D-aspartic acid methyl ester hydrochloride of formula (II), performing methyl amination reaction in methylamine aqueous solution to obtain compound of formula (III), reacting with ethyltrifluoroacetate in methanol/triethylamine mixed solution to protect primary amine of compound of formula (III) with trifluoroacetyl group and form compound of formula (IV), reacting with carbonyldiimidazole (CDI) of formula (IVa) to obtain active mixed anhydride of formula (V), performing condensation reaction with amoxicillin triethylamine salt of formula (Va) to obtain reaction solution containing compound of formula (VI), adding methanol and sodium carbonate aqueous solution, stirring and reacting to remove trifluoroaceyl protecting group and generate sodium aspoxicillin, and recrystallizing with water and acetone.
NOVELTY - A clarithromycin intermediate is prepared by using methylation reaction of (2',4'-0-bis trimethylsilyl)-erythrocin A-9(0-(1-ethoxy-1-methylethyl))oxime as raw material, toluene, n-hexane, and dimethyl sulfoxide as solvents, methyl bromide, methyl iodide, and toluene sulfonic acid methyl ester as methylating agents, and potassium hydroxide as catalyst.    USE - Preparation of clarithromycin intermediate (claimed).    ADVANTAGE - The preparation has high reaction conversion rate, reduced cost, continuous recovery, simple and stable operation, low energy consumption, and less pollution.
NOVELTY - Method using ultrasonic and acid combination circulation to extract protein and humus in dehydrated residual sludge comprises dehydrating residual sludge of town sewage treatment plant in acidic condition, ultrasonic crushing; putting cell dissolved liquid in room temperature for low settling; and centrifuging, separating white colloid substance in supernatant, drying to obtain protein, filtering the supernatant through 23-pore ceramic film filter, filtering out semi-solid substance humus.    USE - Method using ultrasonic and acid combination circulation to extract protein and humus in dehydrated residual sludge.    ADVANTAGE - The method can completely extract protein and humus, and can improve biochemical degradability to 75.7% from 40.2%.    DETAILED DESCRIPTION - Method using ultrasonic and acid combination circulation to extract dehydrated residual sludge protein and humus comprises:    (A) dehydrating residual sludge of town sewage treatment plant in acidic condition, in which sludge concentration is 2 mol/L, regulating pH to 3 using sulfuric acid, ultrasonic crushing for 10-30 minutes at frequency of 20 KHz and power density of 1-2 W/mL, sieving through 100 meshes, removing solid substance and cell dissolved liquid;    (B) putting the cell dissolved liquid in room temperature for low settling for 30-60 minutes; and    (C) centrifuging at 4-30 degrees C and 4000-8000 revolutions/minute for 5-30 minutes, separating white colloid substance in supernatant, drying at 50-60 degrees C for 48 hours to obtain protein, filtering the supernatant through 23-pore porous ceramic film filter, filtering out semi-solid substance humus, and returning filter liquid to step one.
NOVELTY - The device has a shell (1) equipped with a jacket structure and fixed with a gasification reaction room (3). A top part of the shell is equipped with a feeding port (4). A lower end of the gasification reaction room is fixed with a separating plate (5). The shell is equipped with an ash outlet (6). The gasification reaction room is arranged between an air inlet pipeline (7) and an air outlet pipeline (8). A control cabinet (16) is fixed at one side of the shell and mounted on a tool box (17). The air inlet pipeline is fixed between a tar filter device (9) and a dehumidifying device (10).    USE - Gasification reaction room integrated straw-type gasification device.    ADVANTAGE - The device has reasonable design, simple structure, automatic control operation and prolonged service life, and is convenient to operate, energy-saving and environment-friendly, and saves regeneration resource of a heating source and solves the problem of cooking, heating, planting and farm fields.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a gasification reaction room integrated straw-type gasification device.    Shell (1)    Gasification reaction room (3)    Feeding port (4)    Separating plate (5)    Ash outlet (6)    Air inlet pipeline (7)    Air outlet pipeline (8)    Tar filter device (9)    Dehumidifying device (10)    Control cabinet (16)    Tool box (17)
NOVELTY - A Trichoderma koningiopsis Zjc-1 strain (CGMCC 8948), is new.    USE - The T.koningiopsis Zjc-1 strain is useful for degrading rice straw (claimed) and processing agricultural waste into organic fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) T.koningiopsis Zjc-1 inoculum comprising less than or equal to 106 colony forming unit (cfu)/ml; and (2) method for preparing the inoculum involves inoculating the strain in a culture medium containing rice straw powder, culturing the strain at 20-25 degrees C for 6-8 days under static condition, adding sterile water to the culture, filtering culture, to obtain spore suspension and adjusting concentration of spores in the spore suspension to less than or equal to 106 cfu/ml.
NOVELTY - Removing ammoniacal nitrogen in sewage and organic waste products comprises treating and centrifuging the sewage and organic waste products; preparing a suspension; and adding sodium alginate and Prochlorococcus.    USE - The method is used for removing ammoniacal nitrogen in sewage and organic waste products (claimed).    ADVANTAGE - The method for removing ammoniacal nitrogen is rapid and has high efficiency.
NOVELTY - A DNA molecule encoding D-p-hydroxyphenylglycine protein, the protein selected from (i) a protein comprising a defined sequence of 484 or 312 amino acids (SEQ ID NO. 1 or 3), given in the specification, and (ii) a protein comprising an amino acid sequence of SEQ ID NO. 1 or 3 having one or more amino acid residue substitution and/or deletion and/or addition, is new.    USE - The DNA molecule is useful for producing hydantoin.    ADVANTAGE - The DNA molecule is useful for producing hydantoin, where the production method is simple and environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a recombinant vector comprising DNA molecule above; and (2) a recombinant Escherichia coli strain comprising the vector of (1).
NOVELTY - This utility new type relates to one conversion section a saturation tower section water energy saving device, include a plurality of pipeline spraying device inner saturation of tower, a spraying section... inner the saturated tower, one end to any one of a pipeline to corresponding section of the spraying device, and the other end connecting to one water heater. When the synthetic ammonia reducing production time, semi-water coal gas is reduced, according to the size of a water coal, semi-opened part pipeline of valve to make the spraying area of inner saturation tower a multiple part, so as to ensure good atomization effect spray device with a spray head.
NOVELTY - This utility new type provide a one microorganism sewage treatment unit, and comprise microorganism sewage treatment system at least one of a the microbial sewage treatment unit, the microbial sewage treatment unit include plant or floating plant floating leaved plant, connecting network and at least one a microbial growth area, the connecting hung floating plant floating leaved plant plant or microbial growth area located on the plant or floating plant, floating leaved plant is hung connected network system, microbial growth area containing a microorganism of active sludge. This utility new type sewage processing advantages of the aquatic plant and microorganism are combine together, it can process each a sewage, efficient, low cost, and it has wide application prospect.
NOVELTY - This utility new type claims a one step water ecological purification system, include concrete, a concrete bed body from upper to lower comprise three area a, a is floating bed area, microorganism area and sink bed area, a floating bed area set with air tube, said air tube upper end set with air vent and windmill, a windmill fixing set with the air vent of the lower part close to the vent hole, a vent tube lower end port and set with stirrer, a stirrer set in the fixing port, a vent tube lower end is inserted to the microorganism area, a concrete bed body of the left and right two side set with a water inlet and a water outlet, a water inlet and a water outlet set with a detachably a filter network. This utility new type of stepped water ecological purification system purification speed is fast, purification effect, easy maintenance and management, and the cost is low.
NOVELTY - This new type utility claims one a sludge low temperature carbonization system, include the sludge storage tank, a heat exchanger, a carbonization reaction tower, a burner, a centrifugal separate machine and a carbonized product storage tank, wherein, said sludge storage tank and the heat exchanger set with a high pressure slurry pump, the discharge port feeding port is connected with a heat exchanger of a carbonization reaction tower a, discharge hole of carbonization reaction tower in turn a heat exchanger and centrifugal separate machine, the top part discharge tube of carbonization reaction tower through pipeline connecting with the burner. This utility new type carbon chemical reaction for a low sludge low temperature state in the absence of oxygen, the organic component in the oxygen free condition low cracking from solid carbon dioxide in separate, produce a combustion gas volatility organic matter, improving dehydration property, no burning, a sludge carbon, carbide as new resource recycling.
NOVELTY - This utility new type claims a town domestic garbage of one processing device, include high temperature curing reaction groove, an aerobic reaction pool and anaerobic acidification reactor, high temperature curing reaction groove, an aerobic reaction pool and anaerobic acidification reactor are set on the ground following, and in turn to a high to low by a step-shaped channel, a, acidification and three for a technique process of a sequential operation. This utility new type the aerobic biological treatment and anaerobic biological treatment method to organically combine, and degradation of the organic substance is divided into, and acidifying the fermentation a three order of technique process, to accelerate the degradation speed, so as to for a harmless and recycling treatment of domestic garbage.
NOVELTY - Blast. This utility new type claims a static aerobic fermentation of one compost groove, fermenting groove comprise the fermentation groove is of one rectangular fermenting tank, a fermenting tank mounting with the match use of aeration system, the aeration system comprise a sieve plate set with the fermentation tank, the fermentation tank mounting and connecting a vent pipeline of the sieve plate, a blower device, the sieve plate comprise padding layer and stainless steel screen layer. The a compost groove structure simple structure, convenient operation, and in the compost process for a stack effect is good, it is not easy to produce stench and other dangerous gas, high safety.
NOVELTY - This utility new type relates to a one organic solid waste aerobic compost experiment device, include reactor, stir device, an electric control device and a device, reactor by tank body and tank cover, the bottom of the tank body from the 1/5 height of tank body set with shaped; the reactor is divided into upper and lower two layer, the upper layer is the side wall of reaction room compost, compost reaction room a set with sampling hole and a temperature probe, the lower layer is gas distribution room, the bottom of the tank body set with liquid outlet and the air inlet, the air inlet pipeline and the air blower through connecting, a pipeline set with heating plate, tank cover by a semi-round cover is spliced by two observation window is set with a tank cover, a gas port and discharge port, a stir device comprise motor, stir shaft and stir paddle, electric appliance control device connecting with the motor and a heating plate pneuma communication, a device connecting with a gas detection inlet and temperature probe. This utility new type operation is convenient, function is complete, experiment effect is good, convenient for a teaching and scientific research.
NOVELTY - An efficient energy-saving counter-current contact-type persulfate electrolysis device comprises groove shell (7), graphite cathode frame (1), graphite cathode block (3), anode material entrance (15), and cathode material entrance (16). The device further includes hydrogen discharge port, cathode material exit, cover plate, graphite cathode component, cathode copper row, anode copper row, concave liquid collector, anode jack, anode feeding tube through-hole, anode discharge tube through-hole, material liquid distribution box, base plate, and lower membrane tube through-hole.    USE - Efficient energy-saving counter-current contact-type persulfate electrolysis device.    ADVANTAGE - The device ensures conduction and difference between equilibrium concentration of ion to reduce back mixing and ensures electrolysis maximum efficiency.    DETAILED DESCRIPTION - An efficient energy-saving counter-current contact-type persulfate electrolysis device comprises groove shell (7), graphite cathode frame (1), graphite cathode block (3), anode material entrance (15), and cathode material entrance (16). The device further comprises hydrogen discharge port, cathode material exit, cover plate, graphite cathode component, cathode copper row, anode copper row, concave liquid collector, anode jack, anode feeding tube through-hole, anode discharge tube through-hole, material liquid distribution box, base plate, lower membrane tube through-hole, and lower anode feeding tube through-hole.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of efficient energy-saving counter-current contact-type persulfate electrolysis device.    Graphite cathode frame (1)    Graphite cathode block (3)    Groove shell (7)    Anode material entrance (15)    Cathode material entrance (16)
NOVELTY - This utility new type claims a one for conversion of straw decomposing comprehensive utilization device, comprise straw crusher, cracking furnace, a cyclone separator, a condenser, a gas purification device and fractionating tower, straw crusher through inlet end of conveying pipeline with the cracking furnace is connected with exit end of cracking furnace through inlet end of pipeline is connected with the cyclone separator are connected, bottom end of cracking furnace set with a carbon exit, exit end of cyclone separator through inlet end of pipeline connected with the condenser, exit end of condenser is connected with the air inlet of gas purification device is connected, the air outlet is connected with the inlet end of the fractionating tower of gas purification device is connected. This utility new type the straw processing conversion is the biomass gas, carbon, tar and so on completely collect product, conversion efficiency and purification completely, no second pollution, and avoids the serious waste of energy.
NOVELTY - This utility new type relates to one a biomass pyrolysis reaction device, comprise feeding device, reactor and condensing device, a feeding device comprise storage bin, the bottom storage bin set with a discharging port, and the reactor, direct current speed regulating motor and set on the rotate shaft of the bottom of a storage bin, a reactor comprise reaction chamber, reaction chamber at the bottom set with a guide plate, a guide plate set with a wall inner ceramic ball or metal steel ball bed layer, the reaction chamber has a property of carrier set with stir device and reaction chamber set with a electric heating device, lower part of reaction chamber with a carbon bin, upper part of reaction chamber set with air outlet through pipeline with the condensing device a, condensing device comprise first-stage cooling tank, second level condenser and vacuum cold trap. This utility new type has a transfer rate high, the product is not easy to generate a secondary cracking, which can ensure the stable material.
NOVELTY - This utility new type claims a furnace of a rotate one removal of biomass gasification furnace, comprise upper furnace body and lower furnace body, a furnace body set with inner furnace cavity, furnace chamber and the lower furnace burning biomass granule of connected, set with a furnace gate, furnace grid by multiple parallel combination is formed by furnace end opening at the lower furnace cavity along the axial direction arrangement with a flat head teeth and sharp teeth of a furnace, the two interval arrangement, each furnace around its own axis of a synchronous rotate, making time rotate to flat head teeth relative the to reduce a gap between the furnace bar supporting a biomass to a inner furnace cavity, ash discharging time rotate furnace, pointed teeth the furnace ash crushing and discharging to lower inner furnace body, rear discharge is finished to a flat head of tooth row. furnace gate mounting in a move of a pedestal, and the pedestal out a lower furnace body. This utility new type of biomass gasification furnace can smoothly discharge and slag, increase the pneuma production efficiency, reduces the energy waste, one is a significant innovation in preparing fermentable reducing sugar from biomass pneuma.
NOVELTY - This utility new type relates to a one honeycomb sludge molding machine, wherein, comprise electrical machine, machine frame, big roller surface, smooth small roller, a sludge baffle, sludge molding plate, smooth the big idler wheel and small idler wheel face side by side on a machine frame upper, face of the big idler wheel rotating shaft is connected with motor rotating shaft connecting, smooth big rotating shaft of a roller further with a driving gear, the driving gear is a one a driven gear face a small roller, and to face the small roller to rotate, smooth small roller side set with sludge baffle, sludge molding plate set on the face big idler wheel and small idler wheel face, a said sludge molding plate set with a protruding column. This utility new type has simple structure, is convenient to prepare honeycomb sludge, and drying sludge, can shorten the drying time, convenient for subsequent combustion of beneficial effects.
NOVELTY - This new utility model relates to one of marsh gas power distributed energy system, wherein the marsh gas pool comprises generating device, an air storage tank, a daily life for gas device, micro-engine, and direct marsh gas boiler, the biogas pool generating device and air storage tank connected with the air storage tank air outlet respectively with the gas device, micro-engine, and direct connect methane boiler and daily life, connected with the micro-gas turbine for power generation, connecting the direct and marsh gas boiler for user supply cold heat. The beneficial effect: the system using fuel gas as core, realize cool heat connect power supply system, can at the same time high temperature tail gas for the micro-combustion engine, direct, marsh gas boiler equal device for recycling, as heating heat source and maintain temperature in marsh gas pool, can realize direct and satisfy user multi-requirement of the energy step using technology model, increase of comprehensive energy use rate of the traditional energy system, can effective relieving convention energy consume and environment pollute caused by the problem, for optimizing energy structure open of one strip and new way.
NOVELTY - This utility new type category domestic garbage treatment field, especially solar energy domestic garbage low temperature dry distillation energy control system. Each function component solar energy domestic garbage low temperature dry distillation energy control system, include: solar energy system (01), transmission system (02), energy match-store system (03) and a monitoring system (04), the solar energy system (01), using real time tracking sunshine shaft, lens group focusing type solar energy cantilever tower recovering refrigerant such as integrated technology, which not only greatly improve the photovoltaic power generating efficiency, further the refrigerant coexist a heat obtaining heat energy, of a transmission system (02), connected solar energy system (01) is connected with the energy match-store system (03) of; the operation monitoring system (04), monitoring the system operation state, energy match-store system (03) solar energy household garbage carbonization engineering a intelligent distribution electric energy and heat energy, to make it stable. Collect inexhaustible, not using the solar clean energy of a domestic garbage " three-chemical " a, a predicate the nation is a breakthrough innovative technology.
NOVELTY - This new type utility claims one composite microorganism fertilizer production a special cooling device, it mainly comprise a cylinder body, a driving motor, a stirring claw, a blast pipe and blower, said cylinder body is hollow-shaped of two end opening, a supporting wheel for distribute in rows, the rows distribute in pairs of wheels located on cylinder body of the bottom of the driving motor and any transmission connecting wheel, a stirring claw fixed mounting on the inner side wall of cylinder body up, the stirring claw is uniform distribute a row on the inner side wall of the cylinder body, one end said blast tube of blower is connected with the other end of the air supply tube of the inner cylinder body, this utility new type has the advantages: structure is simple, using continuous rolling of cylinder body for composite microorganism fertilizer a valid fast cooling, at the same time, from the discharge hole one side a cylindrical inner body continuously into the cooler, a cooling efficiency is greatly increase, in the cooling process, the inner cylinder body continuously stirring lower the effect of stirring claw, the fertilizer cooling fast and uniform, valid to ensure the quality of the product.
NOVELTY - Domestic waste harmless processing system comprises waste sorting mechanism, anaerobic and aerobic bioorganic fertilizer production mechanism (14), waste incinerator (10) and flue gas purifying mechanism (11) integrally connected by a conveyor belt.    USE - Domestic waste harmless processing system used for small and medium sized towns and cities.    ADVANTAGE - The processing system can be automatically operated, thus, saving labor and time. Organic waste is used for bioorganic fertilizer production, and plastic film can be recycled. The flue gas purification mechanism prevents dioxin formation, making the system environment-friendly and producing no secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of domestic waste processing system.    Waste collecting tank (1)    Coarse crushing machine (3)    Magnetic separator (5)    Cylinder sieve (7)    Waste incinerator (10)    Flue gas purifying mechanism (11)    Anaerobic and aerobic bioorganic fertilizer production mechanism (14)
NOVELTY - An efficient sewage fermentation stirring tank comprises tank body (3), stir device (2), breathing port (1), sewage inlet (5), and circulation inlet (7). The tank further comprises, heat transfer medium inlet, temperature measuring device, pH regulating device, pH detection port, sewage exit, sewage circulation exit, transfer heat medium exit, sewage circulation inlet, and circulation pump exit.    USE - Efficient sewage fermentation stirring tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of efficient sewage fermentation stirring tank.    Breathing port (1)    Stir device (2)    Tank body (3)    Sewage inlet (5)    Circulation inlet (7)
NOVELTY - Combined treatment of vinasse and distillery wastewater comprises stirring wastewater; filtering to get leaching liquid and slag, introducing leaching liquid to storage tank, and regulating pH value; carrying out anaerobic biological treatment; pumping effluent into mixing pool to generate biogas for recycling; absorbing residual dregs in ammonia stripping tower for production of organic fertilizer; and filtering slag in second step in plate frame filter press, where residue is used for production of organic fertilizer, and introducing filtrate to mixing pool.    USE - Method for combined treating of vinasse and distillery wastewater (claimed).    ADVANTAGE - The method has zero-waste discharge, effectively handles solid vinasse, reduces pollution, and saves energy.    DETAILED DESCRIPTION - Combined treatment of vinasse and distillery wastewater comprises:    (A) stirring wastewater for 3-5 days at 40-50 degrees C;    (B) filtering to get leaching liquid and slag, introducing leaching liquid to storage tank, and regulating pH value to 6.8-7.2;    (C) carrying out anaerobic biological treatment when ammonia-nitrogen concentration is less than 800 mg/L or carrying out stripping off of ammonia when ammonia-nitrogen concentration is higher than 800 mg/L and carrying out anaerobic biological treatment for 1-2 days;    (D) pumping effluent into mixing pool to generate biogas for recycling;    (E) absorbing residual dregs in ammonia stripping tower for production of organic fertilizer; and    (F) filtering slag in second step in plate frame filter press, where residue is used for producing organic fertilizer, and introducing filtrate to mixing pool.
NOVELTY - Dewatering sludge comprises adding biochemical residual sludge and sewage according to a volume ratio of 2:1-1:2 into a reactor and then stirring at speed of 60-80 revolutions per minute and temperature of 20-30 degrees C for 5-7 days, carrying out hydrolysis acidification to pH value of 3-4, regulating pH value to 6.8-7.2 using sodium carbonate, sodium hydroxide or sodium hydrogen carbonate, performing fermentation process with an anaerobic fermentation tank, controlling the temperature to 33-37 degrees C and then fermenting for 5-8 days.    USE - The method is useful for dewatering sludge (claimed).    ADVANTAGE - The method is capable of dewatering sludge with increased processing efficiency and shortened reaction period, and without pollution.
NOVELTY - Household garbage/livestock manure anaerobic and aerobic biological organic fertilizer preparation device comprises belt pulley (1), crushing machine (2), solid-liquid separating drum (3), aerobic reaction cylinder (4) and anaerobic reaction cylinder (5).    USE - Household garbage/livestock manure anaerobic and aerobic biological organic fertilizer preparation device.    ADVANTAGE - The device is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of household garbage/livestock manure anaerobic and aerobic biological organic fertilizer preparation device.    Belt pulley (1)    Crushing machine (2)    Solid-liquid separating drum (3)    Aerobic reaction cylinder (4)    Anaerobic reaction cylinder (5)
NOVELTY - Organic fertilizer comprises 160-240 pts. wt. manure, 60-140 pts. wt. leftovers, 60-140 pts. wt. rice bran, 60-140 pts. wt. straw, 60-140 pts. wt. brandy, 60-140 pts. wt. mushroom bed, 60-140 pts. wt. rice husk, 30-70 pts. wt. bean dregs, 30-70 pts. wt. soybean meal, 30-70 pts. wt. wheat bran, 30-70 pts. wt. plant leaf, 2-8 pts. wt. earthworm, 0.5-1.5 pts. wt. Bacillus natto, 0.05-0.5 pt. wt. photosynthetic bacteria, 0.05-0.3 pt. wt. nitrobacteria and 0.05-0.3 pt. wt. nitrite bacteria.    USE - Organic fertilizer used for promoting plant growth, promoting soil granulation, increasing ventilation capacity, improving water retention and improving drainage ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of organic fertilizer comprising taking manure, plant leaf and leftovers, adding photosynthetic bacteria, nitrobacteria and nitrite bacteria, fermenting, adding rice husk, wheat bran and bean dregs, mixing, adding mushrooms, fermenting, adjusting pH to 5.5-6.5, stacking, adding straw, soybean meal and Bacillus natto, fermenting, adding earthworms and breeding.
NOVELTY - Production of organic-inorganic compound fertilizer comprises mixing sheep, cattle, pig, chicken, duck and goose manure, adding crop straw, controlling moisture at 50-65%, spraying, fermenting for 3 months, adding ammonium sulfate and phosphorus-potassium rich fertilizer, milling, mixing, crushing, granulating, drying, cooling, sieving and packaging.    USE - Method for producing organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The production method is environment-friendly, has good waste utilization and does not produce pollution.
NOVELTY - A wood crushing system comprises shaker (1) with screen (11), collection bin which is located below screen, sawdust hopper (12) which is directly connected to conveyor belt of sawdust mill (2), discharge port which is provided in sawdust mill, and online control system which monitors amount of big wood raw materials to be fed in mill through conveyor belt.    USE - A wood crushing system for biomass wood raw material (claimed).    ADVANTAGE - The system reduces sawdust mill feed rate, improves quality of crushed sawdust, enhances production efficiency, and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wood crushing system.    Shaker (1)    Sawdust mill (2)    Drum-type dryer (3)    Screen (11)    Sawdust hopper (12)
NOVELTY - This utility new type relates to one used for a marsh gas compressing water scrubbing purification tower comprise a tower body, said tower body is a vertical structure, the tower body comprise filler section on the upper part and a water storage section is located below a top a filling section set with gas exit, the lower gas exit set with one layer or multi layer silk screen foam destroyer, a filling section upper part set with liquid inlet, a filler section lower part set with gas inlet, liquid inlet is located on a silk screen foam destroyer, the tower body between the liquid inlet and the gas inlet set with first-stage or multi-stage material distributor, the lower part set with a material distributor and the matched use of filler, the filler is set on the filler support through a wall of the inner tower body fix the water storage section lower part set with liquid exit, the side wall water storage section set with far transmission liquid level meter. The tower operation stable, reliable and increase the working efficiency of corrosion resistant property and absorption tower of a product pneuma quality reach the national natural gas a one level standard.
NOVELTY - This utility new type relates to a biomass granule machine of one discharging and cooling and dust-removing device, a cooling dust-removing device of the main discharge hole, used for connecting exhaust fan is provided with a suction opening on the upper part of cooling dust-removing device, a fan connected with a de-dusting cloth bag. Cooling dust-removing device of the host is equipped with a discharge port, by a cooling wind, and the exhaust effect, simplifies the system structure of a whole production line to make the granule in a cooling, increase the hardness, a good for preventing a crack, increase rate of a molding.
NOVELTY - Preparation of biomaterial involves washing shrimp enzymatic extraction residue using water, drying, immersing washed shrimp enzyme extraction residue in sodium hydroxide solution, drying, washing using water, adding dilute hydrochloric acid to adjust washed residue to neutral, performing solid-liquid separation, drying obtained residue, crushing the residue into 100-200-mesh powder, adding powder into sodium alginate solution, mixing, granulating, adding calcium chloride to obtained shrimp powder particles, curing, and drying.    USE - Preparation of high-absorption property biomaterial used for purifying sewage (claimed) and industrial wastewater containing organic substance and heavy metal ion.    ADVANTAGE - The method enables preparation of biomaterial with high adsorption property.    DETAILED DESCRIPTION - Preparation of biomaterial involves washing shrimp enzymatic extraction residue 3-5 times using water, drying, immersing washed shrimp enzyme extraction residue in 20-30% sodium hydroxide solution for 2-4 hours, drying, washing using water, adding dilute hydrochloric acid to adjust washed residue to neutral, performing solid-liquid separation, drying obtained residue at 80-105 degrees C, crushing the residue into 100-200-mesh powder in ultrafine crusher, adding 10-30% powder into 0.5-3% sodium alginate solution, mixing uniformly, granulating, adding 3-5% calcium chloride to obtained shrimp powder particles, curing for 8-12 hours, and drying. The mass ratio of washed shrimp enzyme extraction residue and sodium hydroxide solution is 1:5. An INDEPENDENT CLAIM is included for usage of biomaterial, which involves adding biomaterial to sewage, and performing adsorption treatment for 6 hours. The mass ratio of biomaterial and sewage is 1:10.
NOVELTY - Removing water from a biofuel consisting of biofuel intermediate or a biofuel feedstock, comprises mixing the biofuel with a demulsifier. The demulsifier comprises a product formed from oxyalkylating a resin prepared from a formulation comprising a phenol and a compound consisting of an aldehyde, a diamine and/or a polyamine. The biofuel has less than 50 vol.% of straight vegetable oil or straight waste vegetable oil.    USE - The method is useful for removing water from a biofuel consisting of biofuel intermediate, a biofuel feedstock and biodiesel (all claimed), where the biofuel is useful in diesel engine vehicles.    ADVANTAGE - The method can reduce water and water soluble or dispersed contaminants from the biofuel to a predetermined level in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biofuel composition comprising at least one biofuel consisting of a biofuel intermediate and/or a biofuel feedstock, and a demulsifier.
NOVELTY - Increasing hydrogen recovery of a hydrogen production plant, involves recovering additional hydrogen from a low pressure waste gas stream from a pressure swing adsorption unit producing hydrogen, by feeding the low pressure waste gas stream to an electrochemical cell, separating the additional hydrogen from the low pressure waste gas stream; recovering and combining the additional hydrogen with a high pressure hydrogen product from the pressure swing adsorption unit resulting in increased hydrogen recovery.    USE - For increasing hydrogen recovery of hydrogen production plant (claimed).    ADVANTAGE - The method is improved method for increasing hydrogen recovery of hydrogen production plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing (M1) hydrogen involving feeding a synthesis gas mixture to a pressure swing adsorption unit; producing hydrogen from the synthesis gas mixture in the pressure swing adsorption unit; feeding the remainder of the synthesis gas mixture at low pressure to an electrochemical cell where additional hydrogen is separated from the remainder of the synthesis gas mixture; feeding the additional hydrogen from the electrochemical cell to join with the produced hydrogen to form a combined hydrogen product; and recovering the combined hydrogen product.
NOVELTY - Producing methane hydrogen mixture and hydrogen, comprises mixing flow of natural gas as a feedstock source with water vapor, heating, and performing high-temperature conversion in an adiabatic reactor filled with a catalyst to obtain adiabatic conversion products. The high-temperature conversion is carried out by partial oxidation of flow of natural gas via oxygen by electrolysis.    USE - The method is useful for producing methane hydrogen mixture and hydrogen (claimed).
NOVELTY - A catalyst contains strontium-phosphate apatite.    USE - A catalyst for synthesis of butanol or butanol-containing composition from ethanol (all claimed).    ADVANTAGE - Butanol is manufactured with high selectivity from ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) synthesis of alcohol for synthesizing butanol from ethanol which involves contacting catalyst and ethanol; and    (2) synthesis of butanol-containing composition which involves contacting catalyst and ethanol.
NOVELTY - A chlor-alkali process is performed by supplying hydrogen as fuel to fuel cell stack (14) and supplying caustic solution as electrolyte to fuel cell stack.    USE - A chlor-alkali process using electrolytic membrane cell for electrolyzing brine to produce chlorine, hydrogen, and caustic solution (claimed).    ADVANTAGE - Energy is recovered from hydrogen using a simple and cost-effective fuel cell system, and processes and plant required to maintain a satisfactory electrolyte for the fuel cell system are simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for chemical process plant (10) comprising electrolytic membrane cell (12) for performing chlor-alkali process by electrolyzing brine to produce chlorine, hydrogen, and caustic solution, fuel cell stack, part to supply hydrogen as fuel from electrolytic membrane cell to fuel cell stack, and part to supply caustic solution as electrolyte from electrolytic membrane cells to fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a chemical process plant incorporating the chlor-alkali process.    Chemical process plant (10)    Electrolytic membrane cell (12)    Fuel cell stack (14)    Anode compartment (16)    Anode (17)
NOVELTY - A hydrogen water generator device (10) consists of electrode portion which consists of an anode and a cathode, a support portion which supports the electrode portion, and a control circuit which rises a pressure voltage supplied from a battery stored in the support portion and applies boost voltage to the electrode portion. The electrode portion is inserted in a container of drinking water and immersed in the drinking water.    USE - Device is used for generating hydrogen water (claimed) in residence and office.    ADVANTAGE - The economical and small-sized hydrogen water generator device has excellent portability, and easily generates hydrogen water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen water generator method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen water generator device. (Drawing includes non-English language text)    Hydrogen water generator device (10)    Mainframe (11)    Cover portion (12)    Switch (13)    Notification portion (14)
NOVELTY - Microalgae deposited as FERM BP-22090 is subjected to hydrolysis at 130-160 degrees C in presence of acid catalyst to separate free fatty acid from phospholipids of microalgae, and lipids and fatty acid contained in the cells of microalgae are esterified in presence of alcohol at 60-100 degrees C to obtain biofuel.    USE - Production of biofuel used as fuel for diesel engines of motor vehicles, boats and ships, and aircraft.    ADVANTAGE - The method enables economical, efficient and continuous production of biofuel with high fats and oils content.
NOVELTY - A reactor system consists of system vessel (110) having inner surface and subcritical zone (180) for receiving fluid at subcritical conditions, and at least one corrosion protection layer comprising glass and silicon carbide positioned within subcritical zone to provide physical barrier which protects at least portion of the inner surface from corrosion by fluid.    USE - Reactor system is used for generation of methane fuel (claimed) used for powering an engine, producing electricity and generating heat.    ADVANTAGE - Occurrence of corrosion in reactor system is eliminated, by effective and cost-efficient method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of reactor system; and    (2) manufacture of corrosion protection layer of reactor system using crystal encapsulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the supercritical water reactor system.    Supercritical water reactor system (100)    System vessel (110)    Heat exchangers (115,125)    Slurry (155)    Pre-heater (175)    Subcritical zone (180)
NOVELTY - Circulating renewable energy centralized using agricultural waste, comprises either (a) preprocessing waste generated from an agricultural cultivation facility (100), drying and heating under vacuum condition to obtain zero pellet, (b) supplying the zero pellet in a boiler as heat source, and (c) supplying the generated waste heat from the boiler in the agricultural cultivation facilities via a heat exchanger.    USE - The method is useful for circulating renewable energy centralized using agricultural waste (claimed).    ADVANTAGE - The method is environmentally friendly, maximizes waste chemical re-cycling, saves energy and increases income of agro-industry and marine products industry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for circulating renewable energy centralized using aquatic waste, comprising (i) preprocessing waste generated from aquatic waste, drying and heating under vacuum condition to obtain zero pellet, (ii) supplying the zero pellet in a boiler as heat source, and (iii) supplying the generated waste heat from the boiler in the aquatic processing facility (100a) via an air conditioning system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow chart of the method for circulating renewable energy centralized using agricultural waste (Drawing includes non-English language text).    Agricultural cultivation facility (100)    Aquatic product processing facility (100a)    Cold warehouse (110, 110a)    Drying equipment (120)
NOVELTY - Fuel cell comprises (a) anode conductive material, (b) graphite cathode material, (c) cation exchange membrane, (d) liquid cathode, (e) microbial media, (f) lithotrophs microbes, (g) anode and cathode cables, (h) container, and (i) cover, where the lithotrophs microbes are hydrogen-oxidizing bacteria, anode is anode material, the cation exchange membrane is prepared using zeolite, clay, cement and their mixture, and the liquid cathode is polyaluminum chloride, sodium hypochlorite solution or acetic acid.    USE - The fuel cell is useful for producing electricity.    ADVANTAGE - The fuel cell is environmentally-friendly, cost-effective and enables to produce higher electric energy.    DETAILED DESCRIPTION - Fuel cell comprises (a) anode conductive material to capture electrons, (b) graphite cathode material to bind cations, (c) cation exchange membrane to bind cations, (d) liquid cathode placed in cathode chamber to attract cations (hydrogen ions) from anode, (e) microbial media placed in the anode chamber as source of nutrients for microbes, (f) lithotrophs microbes placed in the anode chamber for performing oxidation, (g) anode and cathode cables to supply power, where the cable is placed between the cathode and anode, (h) container for placing anode, cathode, liquid cathode, microbes, media and cation exchange membrane, and (i) cover to seal the container, where the lithotrophs microbes are hydrogen-oxidizing bacteria, anode is zinc anode material, the cation exchange membrane is prepared using zeolite, clay, cement and their mixture, and the liquid cathode is polyaluminum chloride, sodium hypochlorite solution or acetic acid.
NOVELTY - Separating or recovering animal protein derived from an aqueous liquid containing animal proteins, comprises generating gas bubbles from a gas or gas mixture in the liquid, and forming a foam. The gas is hydrogen gas, a hydrogen gas-containing gas mixture, gas or gas mixture generated electrochemically in the liquid, or hydrogen gas generated electrochemically in the liquid.    USE - The hydrogen gas or a hydrogen-containing gas mixture is useful for generating foam in the liquid-containing animal proteins, for obtaining or removing animal proteins from the liquid, for cleaning or depleting of liquid from animal proteins for the treatment of process water, waste water or solutions containing animal proteins (claimed).    ADVANTAGE - The method is simple and improves fuel enrichment in the foam.
NOVELTY - Manufacture of mesoporous aluminosilicate containing micropore and mesopore involves ion-exchanging aluminosilicate material having micropore using dissociated form of ammonia material and secondary group element-containing material, and heat-treating obtained ion-exchanged aluminosilicate to form mesopores.    USE - Manufacture of mesoporous aluminosilicate used as absorber for absorbing cation pigment, water, hydrogen, carbon dioxide, methane, benzene and toluene (all claimed), and for catalyst.    ADVANTAGE - The mesoporous aluminosilicate is economically manufactured with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for adsorption method of material chosen from cation pigment, water, hydrogen, carbon dioxide, methane, benzene and toluene, by using the mesoporous aluminosilicate as absorber.
NOVELTY - The method involves partially heating and separating the nitrogen-rich, methane-containing liquid fraction (5) in a nitrogen-rich, methane-depleted gas fraction (7) and a methane-rich liquid fraction (11) by rectification (T1). The separation of the partially condensed fraction (2) is carried out in a separator (D) or in a separating column. The rectification recovers the nitrogen-rich, methane-depleted gas fraction which has a specific residual methane content.    USE - Method for separating trace components selected from nitrogen, methane and helium-containing fraction.    ADVANTAGE - The method involves partially heating and separating the nitrogen-rich, methane-containing liquid fraction in a nitrogen-rich, methane-depleted gas fraction and a methane-rich liquid fraction by rectification, and hence ensures obtaining nitrogen-rich liquid fraction, which contains specific methane residue content.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a trace components separating method.    Partially condensed fraction (2)    Nitrogen-rich, methane-containing liquid fraction (5)    Nitrogen-rich, methane-depleted gas fraction (7)    Methane-rich liquid fraction (11)    Separator (D)    Rectification (T1)
NOVELTY - The electrochemical reaction apparatus (10) has a photoelectrode (11) that is comprised with gallium oxide single crystal that generates an electronic-hole pair by receiving irradiation of an UV ray. A counter electrode (12) is electrically connected with the photoelectrode. An electrolyte solution tank (14) accommodates the electrolyte solution (13) that contacts the photoelectrode and the counter electrode. A bias power supply is connected between photoelectrode and counter electrode.    USE - Electrochemical reaction apparatus.    ADVANTAGE - The electrochemical reaction apparatus obtains highly efficient and stable photocatalytic function. The electrochemical reaction apparatus synthesizes or decomposes the organic substance and the inorganic material.    DETAILED DESCRIPTION - The photoelectrode is comprised by n-type gallium oxide monocrystal substrate with specific carrier concentration. The electrolyte solution generates hydrogen from the counter electrode by irradiation of the UV light to the photoelectrode. The light source is comprised, so that deep UV light is irradiated to the photoelectrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of electrochemical reaction apparatus.    Electrochemical reaction apparatus (10)    Photoelectrode (11)    Counter electrode (12)    Electrolyte solution (13)    Electrolyte solution tank (14)
NOVELTY - The reformer (1) has a plasma generation unit (12) that generates plasma in a catalyst unit which decomposes a hydrogen-containing compound according to the catalytic reaction of a catalyst, and generates hydrogen. A plasma starting control unit controls starting of plasma generation unit. A plasma starting control unit (16) starts the plasma generation unit during start-up of reformer when temperature of the catalyst is lower than the catalytic reaction temperature which decomposes the hydrogen-containing compound.    USE - Reformer used in motor vehicle for decomposing hydrogen containing compound to generate hydrogen according to catalytic reaction.    ADVANTAGE - The generation of hydrogen from start-up of a reformer is enabled for a short time. Since portion of discharge energy of plasma is utilized for disassembly of a hydrogen-containing compound, the hydrogen generation becomes possible from start-up of the reformer for a short time. The portion of discharge energy of the plasma is utilized for the heating of the catalyst portion efficiently by generating plasma in the catalyst portion. The temperature sensor is installed in the catalyst portion to detect the temperature of a catalyst. The heat insulating material is installed in the outer periphery of the reformation chamber, so that catalyst unit is heated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reformer.    Reformer (1)    Reformation chamber (10)    Plasma generation unit (12)    Heating apparatus (14)    Plasma starting control unit (16)
NOVELTY - The electrolyzer (10) has an electrolysis cell (12) that is connected with the product outlet tubes (20,22) for leading-out product flow from electrolysis cell. An adsorption element (26) is connected with the product outlet tubes and is arranged downstream from the electrolysis cell. Substance contained in the product flow is adsorbed by the adsorption element. The electrolysis cell is partially temperature-controlled by the adsorption element.    USE - Electrolyzer for generating hydrogen gas, and used for converting energy temporarily (all claimed).    ADVANTAGE - Since the adsorption element is arranged downstream from the electrolysis cell, the efficiency of the electrolyzer is improved. The heating of the electrolysis cell is realized in a simple manner and with reduced cost. The adsorption element is thermally combinable with the temperature control medium conduit which guides the temperature control medium, so that the exceptionally effective heating of electrolysis cell is realized. The required space of the electrolyzer is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyzer.    Electrolyzer (10)    Electrolysis cell (12)    Electrodes (16,18)    Product outlet tubes (20,22)    Adsorption element (26)
NOVELTY - The system has an electric power generation/electrolysis unit which includes an electrolysis function for electrolyzing water steam supplied from a hydrogen-producing unit at the time of regeneration of electric power. A gas flow path circulates the gas which contains hydrogen and water steam between the hydrogen-producing unit and electric power generation/electrolysis unit. A water replenishment unit replenishes water to the gas flow path, when the electric power generation/electrolysis unit produces electric power and performs electrolyzing process.    USE - Secondary battery type fuel cell system.    ADVANTAGE - Since the water replenishment unit replenishes water to the gas flow path when the electric power generation/electrolysis unit produces electric power and performs electrolyzing process, the stable electric power generation and charge are attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the secondary battery type fuel cell system.(Drawing includes non-English language text)    Hydrogen-producing element (1)    Fuel cell unit (2)    Heat insulation container (9)    Pressure sensor (12)    System controller (23)
NOVELTY - The system (100) a material supply switch unit that is switched to another material supply unit (2) when raw material of one material supply unit (1) used as supply source of raw material is exhausted. A modifier (6) generates a hydrogen-containing-gas using the raw material supplied from material supply units and air supplied from outside. A controller (7) performs control so that ratio of amount of material flow and air flow amount which are supplied to modifier becomes predetermined value according to switch signal which shows switch of supply source of raw material.    USE - Hydrogen generation system used in fuel cell system (claimed).    ADVANTAGE - Since the ratio of amount of material flow and air flow amount which are supplied to modifier becomes predetermined value according to switch signal which shows switch of supply source of raw material, the excessive temperature rise in the modifier is prevented effectively by changing the supply source of raw material to another material supply unit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the hydrogen generation system.(Drawing includes non-English language text)    One material supply unit (1)    Another material supply unit (2)    Modifier (6)    Controller (7)    Hydrogen generation system (100)
NOVELTY - A gas-hydrate particle (3) is obtained by making methane or natural gas component (1) and heavy water (4) contact under low-temperature and high-pressure conditions rather than methane- or natural gas component-heavy water-hydrate phase-equilibrium thermal-stress conditions. Water molecule which makes up a cage-like structure (2) is heavy water.    USE - A gas-hydrate particle (claimed).    ADVANTAGE - Decomposition of gas-hydrate particle to more than freezing point temperature and at high temperature is suppressed, allowing gas-hydrate particle to be handled at high temperature during transport and storage and reducing required energy for cooling. Separation process of the additive decomposition water after gasification becomes unnecessary.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas-hydrate storage method of storing methane hydrate or natural-gas-component-containing hydrate.    DESCRIPTION OF DRAWING(S) - The drawings show cross-sectional diagrams of a gas-hydrate particle. (Drawing includes non-English language text).    Gas molecule e.g. methane (1)    Cage structure (2)    Gas hydrate particles e.g. methane hydrate (3)    Heavy water or water containing heavy water (4)
NOVELTY - Method of preparing compost, involves obtaining fallen leaves, removing impurities from the fallen leaves, drying, pulverizing the dried leaves, adding 45 wt.% pulverized fallen leaves, residues of herbal medicine, 8-12 wt.% effective microorganisms, 8-12 wt.% sugar and 80 wt.% water, and fermenting the mixture at constant temperature to obtain the product.    USE - The compost is useful for promoting the growth of plants and protecting plants from pests.    ADVANTAGE - The compost does not affect the fertility of soil, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compost which is prepared by the above method.
NOVELTY - The device has a reactor that is comprised with an inner wall (9) which is comprised with a compost bin (7). A stir shaft (5) is located in the center position of the compost bin. A stir pole (4) is uniformly distributed with several aeration holes. The tail end of a pneumatic compost vessel (21) is equipped with a valve (2). The stir shaft is provided with a roller, and a gas dryer is configured for drying the gas passed into a gas pre-heater. A gas pipe is connected with the stir shaft through a flexible connecting portion.    USE - Pressurized aeration composting device.    ADVANTAGE - The material is stirred uniformly and sufficient aeration is ensured. The time required for the composting reaction process is reduced, and the generation of bad smell is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pressurized aeration composting device.    Valve (2)    Stir pole (4)    Stir shaft (5)    Compost bin (7)    Inner wall (9)    Pneumatic compost vessel (21)
NOVELTY - Method for preparing liquid fertilizer using fish wastes, involves crushing fish wastes after performing pasteurization of fish waste, performing proteolytic decomposition of crushed fish wastes using aerobic microorganism, performing segmentation of mixture to obtain vortex particles, performing anaerobic microbial fermentation and stabilization processes of the obtained mixture, re-processing mixture, and preparing fish liquid fertilizer.    USE - The method is useful for preparing liquid fertilizer using fish wastes (claimed).    ADVANTAGE - The method is environmentally-friendly, and prepares liquid fertilizer with high quality.
NOVELTY - Fertilizer composition comprises glucose, beer liquid, leaves hummus, beef heart powder, soybean residue and a mixture of tea leaves, yeast, urea, deionized water and potassium permanganate solution.    USE - Fertilizer composition used for new-type garden planting (claimed).    ADVANTAGE - The fertilizer composition has strong fertility effect, faster fertilizer effect, disease resistance ability and vigorous growth property.
NOVELTY - The device has a stabilization bath (20) in which organic waste is flowed in. A cleaning solution supply unit is connected to stabilization bath for feeding removal of dissolved oxygen liquid within stabilization bath. The mixers (60,61) are installed within stabilization bath for stirring organic waste and removal of dissolved oxygen liquid. A mixed solution discharge pipe is positioned in bottom surface of stabilization bath for discharging mixed solution generated in stabilization bath. The mixed solution is configured to remove dissolved oxygen contained in organic waste.    USE - Anaerobic digestion device for stabilizing of organic waste.    ADVANTAGE - Since the dissolved oxygen contained in the organic waste is removed, the organic waste is stabilized quickly. The anaerobic digestion efficiency of the organic waste is enhanced. The biogas is produced steadily in the anaerobic digestion. The environmental load which the microorganism of the anaerobic digestion receives is minimized. The dwell time of the organic waste is shortened in the anaerobic digestion device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic digestion method for stabilizing of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion device for stabilizing of organic waste. (Drawing includes non-English language text)    Stabilization bath (20)    Gas supply blower (40)    Heating tube (50)    Mixers (60,61)    Controller (70)
NOVELTY - Electrolysis method with high electrical efficiency, is claimed.    USE - Electrolysis method is used for splitting of water molecule for creating hydrogen and oxygen, and liquid electrolyte e.g. sodium acetate into gases.    ADVANTAGE - The method enables efficient and economical electrolysis process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of two electrode sets of electrolysis system.    Electrodes (C)    Mofsets (J)    Super capacitors (K)    Internal diodes (L)    Main supply (M)
NOVELTY - Gas production involves initiating heating biomass to a gasification stage partial oxidation gases and exposure to ultraviolet rays by action of a plasma torch. The biomass is preheated in a phase reactants fluids including water, water vapor, oxygen, air, carbon dioxide or hydrogen at increased pressure. The temperature of the raw material is raised to 250-900 degrees C.    USE - Method for producing gas from biomass, preferably organic biomass material.    ADVANTAGE - The method performs gasification of biomass in a simple manner.    DETAILED DESCRIPTION - Gas production involves initiating heating biomass to a gasification stage partial oxidation gases and exposure to ultraviolet rays by action of a plasma torch. The biomass is preheated in a phase reactants fluids including water, water vapor, oxygen, air, carbon dioxide or hydrogen at increased pressure. The temperature of the raw material is raised to 250-900 degrees C. The heated material is treated with of ultraviolet rays at 1150-1250 degrees CC by action of a plasma torch generated synthesis gas, where the resulting gas is cooled by transmitting directly or indirectly to raw material in solid or gaseous fluids as reactants. The resulted gas is analyzed to determine molar ratio of hydrogen or carbon monoxide and carbon monoxide or carbon dioxide. An INDEPENDENT CLAIM is included for a device for implementing the method for producing gas, which comprises an outer container with an inlet and outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing gas.    Non-volatile fluid (2)    Fluid reactant (3)    Heat exchanger (4)    Inner container (5)    Outer container (15)
NOVELTY - The device (2) has a number of intermediate plates arranged between two end plates, where the intermediate plates are electrically insulated to form compartments in which an electrolyte (6) is foreseeable. One of the end plates is connected to a voltage source (12) for use in the application of voltage on the end plates. The electrolyte comprises potassium hydroxide, where amount of the potassium hydroxide in the electrolyte is between 6 and 20 g/liter, preferably between 12 and 18 g /liter and most preferably about 16g/liter.    USE - Electrolytic device for production of hydrogen and/or oxygen for a water heater or central heating system and a motor or generator that is utilized in a vehicle (all claimed).    ADVANTAGE - The device is provided with a power limiter that is adjusted in such a way that the product of the cell voltage and cell current remains the same so as to maintain the cell voltage of the cell and ensure the positive effect on the stability of the operation of the device. The device is simple in structure, and provides the hydrogen and/or oxygen for the water heater or central heating system and a motor or generator in a simple and effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a water heater or heating system    (2) a motor or generator    (3) a method for producing hydrogen gas supplying to an electrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrolytic device.    Electrolytic device (2)    Container (4)    Electrolyte (6)    Electrode (8)    Voltage source (12)
NOVELTY - Preparation of nutrition sand comprises preparing water sand, preparing sand-based slow-release fertilizer, and mixing until uniform sand water and sand-based slow-release fertilizer at 99:1-50:50 volume ratios.    USE - Method for preparing nutrition sand (claimed).    ADVANTAGE - The method has simple technique, low cost and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the preparation method of nutrition sand (Drawing includes non-English language text).
NOVELTY - Potato fertilizer comprises 100-120 pts. wt. cattle manure, 10-12 pts. wt. coal, 10-12 pts. wt. clay, 3-4 pts. wt. attapulgite powder, 4-5 pts. wt. starch, 30-34 pts. wt. urea, 2-3 pts. wt. manganese sulfate, 2-3 pts. wt. ferrous sulfate, 2-3 pts. wt. zinc sulfate, 1-2 pts. wt. chitosan, 1-2 pts. wt. lignin sulfonate, 1-2 pts. wt. polyacrylamide, 3-4 pts. wt. microbial inoculum and 4-6 pts. wt. film-forming agent.    USE - Potato fertilizer used for enhancing quality and growth of potatoes.    ADVANTAGE - The potato fertilizer is nutrient-rich, and has water-seepage property.    DETAILED DESCRIPTION - Potato fertilizer comprises 100-120 pts. wt. cattle manure, 10-12 pts. wt. coal, 10-12 pts. wt. clay, 3-4 pts. wt. attapulgite powder, 4-5 pts. wt. starch, 30-34 pts. wt. urea, 2-3 pts. wt. manganese sulfate, 2-3 pts. wt. ferrous sulfate, 2-3 pts. wt. zinc sulfate, 1-2 pts. wt. chitosan, 1-2 pts. wt. lignin sulfonate, 1-2 pts. wt. polyacrylamide, 3-4 pts. wt. microbial inoculum and 4-6 pts. wt. film-forming agent. The film-forming agent comprises 12-15 pts. wt. dimethicone, 13-16 pts. wt. butyl methacrylate, 1-2 pts. wt. crosslinking agent, 0.1-0.2 pt. wt. nanocarbon, 1-2 pts. wt. medical stone powder and 1-2 pts. wt. boric acid.
NOVELTY - Preparation of 2-amino-5-thio benzoic acid involves reacting 2-nitro-5-halogenated benzoic acid as raw material with sulfur-containing reagent in alkaline aqueous solution by nucleophilic substituted reaction, where the mole ratio of the 2-nitro -5-halogenated benzoic acid and sulfur-containing reagent is 1: 1 to 4, then adding nitro reduction agent which is prepared through two step conversion in the same container.    USE - For preparation of 2-amino-5-thio benzoic acid (claimed) which is used in the production of bio-synthesis, pharmaceutical and pesticide.    ADVANTAGE - The process uses raw material which is easy to obtain; provides little pollution to the environment; is simple; provides high chemical yield and strong practicability; and is suitable for industrial production.
NOVELTY - Forming ortho-aminoanisole involves feeding 4000 l of ortho-nitroanisole into reduction reactor, closing valves, replacing oxygen in kettle with nitrogen, starting stirrer, adding 15 kg catalyst, heating to 60 C, adding hydrogen in 600 cubic meters, maintaining jacket and disk tube temperature to 130 C, controlling temperature to 60-150 C and pressure at 0.8-3.0 MPa, reducing temperature to 40 C, stopping stirring, settling catalyst, filtering catalyst, passing ortho-anisidine to mixer, standing, layering, rectifying and refining, where catalyst is palladium on carbon and nickel alloy.    USE - For the preparation of ortho-aminoanisole (claimed) used to produce azo dyes; ice-dyeing dye and naphthol AS-OL dyes; in antidiarrheal medicine; and for preparing vanillin.    ADVANTAGE - The method avoids need for distillation, reduces steam energy consumption by more than 80%, and improves productivity. The method saves steam energy, reduces preparation cost, and is environment-friendly.    DETAILED DESCRIPTION - Preparation of ortho-aminoanisole involves feeding 4000 l of ortho-nitroanisole using feeding pump into reduction reactor, closing all valves of the reduction reactor, replacing oxygen in the reaction kettle with nitrogen, after replacement, starting reduction reactor stirrer, adding 15 kg catalyst and starting heating to 60 C, adding hydrogen in 600 cubic meters, maintaining jacket and disk tube temperature to 130 C, controlling reaction process temperature to 60-150 C, and reaction pressure at 0.8-3.0 MPa, reducing temperature in the kettle to 40 C, stopping stirring, settling catalyst, filtering the catalyst, passing ortho-anisidine to mixer, standing and layering, rectifying and then refining to form ortho-anisidine, where the catalyst is palladium on carbon and nickel alloy, and weight ratio of the palladium on carbon and nickel alloy is 1:1.
NOVELTY - Methods for treating waste water involves (a) equalizing the waste water, (b) passing equalized waste water through a series of forced and gravity controlled up-flow anaerobic floating filter (UAFF), and (c) passing semi treated water through a series of gravity controlled facultative bacterial tank (FBT).    USE - The method is useful for treating waste water (claimed).    ADVANTAGE - The method has zero sludge production, is free of mechanical moving components and hence do not consume energy and cost, and produces alternative fuel e.g. biogas as a by-product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anti clogging bacterial growth mechanism.
NOVELTY - Process comprises (a) mixing a microbial biomass, having a moisture level and comprising oil-containing microbes, and at least one grinding agent capable of absorbing oil, to provide a disrupted biomass mix, (b) blending at least one binding agent with the disrupted biomass mix to provide a fixable mix capable of forming a solid pellet, and (c) forming the solid pellet from the fixable mix.    USE - The process is useful for forming solid pellets to prepare pelletized oil-containing microbial biomass (all claimed).    ADVANTAGE - The process efficiently recovers oil from microbial biomass with high yield and good moisture content, and increases the disruption efficiency of at least 50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid pellet comprising (i) 70-98.5 wt.% of disrupted biomass comprising oil-containing microbes, (ii) 1-20 wt.% of grinding agent, and (iii) 0.5-10 wt.% of binding agent, where the wt.% of (i), (ii) and (iii) are based on the summation of (i), (ii) and (iii) in the solid pellet.
NOVELTY - Additive containing spherical layered structure onion-like particles, comprises 10-6-10-1 wt.% of carbon nanosized spherical clusters (CNOs) and balance amount of solvatosol (sic) containing solvent. The CNOs are dispersed in the solvent and have a size of 1-500 nm, and consist of laminated partially closed cockleshell-like form graphene layers with substituents.    USE - The additive is useful for producing fuels, lubricants (claimed), petroleum, bioethanol, biodiesel fuels, oils, greases, and technical fluids, which are useful in engines of automobile and aircraft.    ADVANTAGE - The additive simply and reliably produces the fuels and lubricants with increased antifriction, antiscoring, antiwear, anticorrosive and antioxidant properties, and improved operational lubricity, thus reducing accident rate of aircraft and automobile.
NOVELTY - Preparing cow dung briquette comprises mixing 100 pts. wt. cow dung and 27-95 pts. wt. vegetative parts of plants, enhancing a viscosity of the mixture by adding coal composition, stirring the obtained mixture for 3-6 hours and then drying to reduce a moisture content of the mixture to 47-62%, further drying the mixture to reduce the moisture content of the mixture to 13-22%, molding the dried product and then aging for 5 days, and packaging the aged product and then sealing with a sealing material.    USE - The method is useful for preparing cow dung briquette (claimed), which is useful as a fuel.    ADVANTAGE - The method is capable of economically and rapidly preparing the cow dung briquette with improved flammability and storage stability and without bad odor.
NOVELTY - The device comprises a fluidized-bed reactor provided for modifying tar that is generated during gasification process of coal or biomass, and a catalytic membrane for reforming the modified tar. The fluidized-bed reactor is operated at 400-900 degrees C. The catalytic membrane: has a single layer or multiple layers; is prepared by molding ceramic powder and then sintering; is a porous catalytic membrane having a particle size of 0.01-100 mu m; has a plate-like shape or tubular shape; and is present in contact with the fluidized-bed reactor.    USE - The device is useful for reforming tar (claimed).    ADVANTAGE - The device is capable of reforming the tar with improved yield.    DETAILED DESCRIPTION - The device comprises a fluidized-bed reactor provided for modifying tar that is generated during gasification process of coal or biomass, and a catalytic membrane for reforming the modified tar. The fluidized-bed reactor is operated at 400-900 degrees C. The catalytic membrane: has a single layer or multiple layers; is prepared by molding ceramic powder and then sintering; is a porous catalytic membrane having a particle size of 0.01-100 mu m; has a plate-like shape or tubular shape; and is present in contact with the fluidized-bed reactor. The device further comprises an outlet that is arranged in a bottom portion of the fluidized-bed reactor.
NOVELTY - A methane fermentation tank (100) comprises methane fermentation tank body (1), fluid pressure acquisition stage (3) which injects liquid in bottom part of methane fermentation tank body inner side, and discharge unit (4) to discharge sediment deposited on bottom part of methane fermentation tank body. Sediment migrating with liquid injected from fluid pressure acquisition stage is discharged by discharge unit.    USE - A methane fermentation tank for anaerobic fermentation of organic waste e.g. sewage sludge and foodstuff waste material.    ADVANTAGE - Sediment in methane fermentation tank body inner side can be easily discharged from tank, without opening methane fermentation tank body inner side.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sediment removal method in methane fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the methane fermentation tank.    Methane fermentation tank body (1)    Stirrer (2)    Fluid pressure acquisition stage (3)    Discharge unit (4)    Methane fermentation tank (100)
NOVELTY - An ammonia-removal device (100) comprises 1st catalyst (1) which is an oxidation catalyst which reduces ammonia in hydrogen-containing-gas by oxidation reaction, and 2nd catalyst (2) which contains oxidation catalyst different from 1st catalyst and methanation catalyst that reduces carbon monoxide in hydrogen-containing-gas by methanation reaction.    USE - An ammonia-removal device (claimed).    ADVANTAGE - Temperature of catalyst which decomposes ammonia in hydrogen-containing-gas to appropriate temperature is kept simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an ammonia removal process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the ammonia-removal device. (Drawing includes non-English language text).    1st catalyst (1)    2nd catalyst (2)    Ammonia-removal device (100)
NOVELTY - Producing liquid natural gas, comprises: recovering carbon dioxide from the atmosphere; reacting the recovered carbon dioxide together with hydrogen to provide methane; and liquefying the methane to derive the liquid natural gas.    USE - The method is useful for producing liquid natural gas.    ADVANTAGE - The method enables flexibility regarding the location between assembly components and enables efficient operation of the assembly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plant assembly for producing liquid natural gas, comprising: a carbon dioxide recovery module for recovering carbon dioxide from the atmosphere; a reactor for combining the recovered carbon dioxide together with hydrogen to provide methane; and a liquefaction module for liquefying the methane from which the liquid natural gas is derived.
NOVELTY - Preparing substituted (6aS)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole compound (II), as a racemic mixture or its single enantiomer or salt, comprises oxidizing (6aS)-1-(nitromethyl)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole compound (III), and optionally converting (II) to another compound (II) or its salt.    USE - The method is useful for preparing (II), where the compounds (II), (III), (IV) or (V) are useful as intermediates for preparing telaprevir (all claimed) to treat hepatitis C infections. No biological data given.    ADVANTAGE - The method is capable of easily preparing (II) with high yield and high purity in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing substituted (6aS)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole compound of formula (II), as a racemic mixture or its single enantiomer or salt, comprises oxidizing (6aS)-1-(nitromethyl)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole compound of formula (III), and optionally converting (II) to another compound (II) or its salt.    R = 1-12C-alkyl, 3-10C- cycloalkyl, (hetero)aryl (all optionally substituted) or H;    P1 = H or amino protecting group; and    R1 = H or methyl.    INDEPENDENT CLAIMS are included for:    (1) a process for preparing (III), comprising adding nitro compound of formula (R1CH2NO) (VI), to racemic (6aS)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole (VII); and    (2) the compound (III), (1S,6aS)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrole-1-carbaldehyde compound of formula (IV) or 1-((1S,6aS)-1,2,3,3a,4,5,6,6a-octahydrocyclopenta(c)pyrrol-1-yl)ethanone compound of formula (V) (where P is not tert-butyloxycarbonyl).
NOVELTY - Aerosol device comprises a container, one or more propellants, a composition comprising one or more sebum absorbing powders having a sebum uptake power of greater than or equal to 35 ml/100 g, where the propellants are present in the composition or in the container separated from the composition, and a unit for distributing the composition comprising a diffuser provided with at least two, preferably three spraying orifices.    USE - The aerosol device is useful for dry cleaning and cosmetic treatment of keratin materials, preferably hair (all claimed) of humans.    ADVANTAGE - The aerosol device ensures easy and comfort application of the composition to the hair, and provides optimum cleaning activity, thus leaving less residues and increasing the volume of the hair.
NOVELTY - Aerosol device comprises a container containing one or more propellants, and a composition comprising one or more sebum absorbing powders having a sebum uptake power of greater than or equal to 35 ml/100 g, one or more hair styling powders comprising calcium carbonate and less than 10 wt.% of one or more 2-4C monoalcohols.    USE - The aerosol device is useful for dry cleaning and cosmetic treatment of keratin materials, preferably hair (all claimed) of humans.    ADVANTAGE - The aerosol device provides optimum cleaning activity, thus leaving fewer residues and increasing the volume of the hair.
NOVELTY - Aerosol device comprises a container, one or more propellants, a composition comprising one or more sebum absorbing powders having a sebum uptake power of greater than or equal to 35 ml/100 g, and a unit for distributing the composition, comprising a diffuser provided with at least two, preferably three spraying orifices. The propellants are present in the composition or in the container separated from the composition.    USE - The aerosol device is useful for dry cleaning and cosmetic treatment of keratin materials, preferably hair (all claimed) of humans.    ADVANTAGE - The aerosol device evenly distributes the composition to the hair root, thus providing optimum cleaning activity, leaving fewer residues and increasing the volume of the hair.
NOVELTY - Use of at least one modified alkylphenol-aldehyde resin as an additive for improving oxidation and/or storage stability of a fuel composition or a liquid hydrocarbon fuel, is claimed. The modified alkylphenol-aldehyde resin is obtained by a Mannich reaction of an alkylphenol-aldehyde condensation resin with at least one 1-8C-aldehyde and/or one 1-8C-ketone and at least one hydrocarbon compound having at least one 4-30C-alkylmonoamine or 4-30C-alkylpolyamine group (alkylamine).    USE - The modified alkylphenol-aldehyde resin is useful as an additive for improving oxidation and/or storage stability of a fuel composition or a liquid hydrocarbon fuel including gas oils, diesel fuel, gasoline, biofuels, jet fuel, fuel oils, domestic fuel oil and heavy fuel oils (all claimed).    ADVANTAGE - The modified alkylphenol-aldehyde resin effectively improves temperature stability of fuels and liquid hydrocarbon fuels.    DETAILED DESCRIPTION - Use of at least one modified alkylphenol-aldehyde resin as an additive for improving oxidation and/or storage stability of a fuel composition or a liquid hydrocarbon fuel, is claimed. The modified alkylphenol-aldehyde resin is obtained by a Mannich reaction of an alkylphenol-aldehyde condensation resin with at least one 1-8C-aldehyde and/or 1-8C-ketone and at least one hydrocarbon compound having at least one 4-30C-alkylmonoamine or 4-30C-alkylpolyamine group (alkylamine), and by condensation of at least one alkylphenol substituted by at least one linear or branched 1-30C-alkyl and at least one 1-8C-aldehyde and/or 1-8C-ketone.
NOVELTY - Producing drying agent comprises mixing 2000 Kcal/kg of waste coal, calcium sulfate, wet organic waste including food waste, livestock manure, pig manure, agriculture waste and fisheries waste and zeolite powder and then fermenting at 60 degrees C for more than 10 days.    USE - The method is useful for producing a drying agent (claimed).    ADVANTAGE - The method is capable of efficiently and economically producing the drying agent in an environmentally-friendly manner.
NOVELTY - Preparing 4-(4-aminophenyl)-3-morpholinone comprises (a) adding 4-(4-nitrophenyl)-3-morpholinone in a solvent to prepare a solution, and (b) reacting sodium hydrosulfite with the solution.    USE - The method is useful for preparing 4-(4-aminophenyl)-3-morpholinone (claimed), which is useful as a key intermediate for synthesizing rivaroxaban.    ADVANTAGE - The method prepares 4-(4-aminophenyl)-3-morpholinone with high yield and high purity, without using high-temperature and high-pressure hydrogen gas and expensive hydrogenation catalyst, hence the method is less expensive, environmentally friendly and suitable for industrial large-scale production.
NOVELTY - Use of biopolymer additive is claimed in manufacturing process of biodegradable polymer, where the additive is prepared from biomass of broken microorganism cell.    USE - The biopolymer additive is useful in manufacturing process of biodegradable polymer which is useful in composition (all claimed) used in plastic production.    ADVANTAGE - The biodegradable additive has enhanced rheological property and biodegradability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition comprising 0.05-10 wt.% biopolymer additive, and biodegradable polymer; and    (2) method for preparing the biopolymer additive, involves (a) obtaining microorganism biomass, (b) breaking microorganism cell of the biomass, and (c) powdering the biomass.
NOVELTY - The system has a methanol synthesis unit (1) that includes a water cooler (4), a compressor (3), a separator (5) and a pre-heater (2). The pressurizing gas exit of compressor is connected to inlet of pre-heater which raises temperature of gas as raw material to synthesize methanol. An exit of pre-heater is connected to water cooler. The exit of water cooler is connected to inlet of separator, and the top gas exit of separator is connected to air inlet of compressor. The methanol synthesis unit is arranged to synthesize methanol from raw gas.    USE - System for synthesizing methanol from coke oven gas.    ADVANTAGE - The carbon utilization rate is increased, the greenhouse gas discharging is reduced and the economic benefit of system is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for synthesizing methanol from coke oven gas. (Drawing includes non-English language text)    Methanol synthesis unit (1)    Pre-heater (2)    Compressor (3)    Water cooler (4)    Separator (5)
NOVELTY - Nitrogen, phosphorus and potassium containing special fertilizer comprises (in pts.wt.): wooden meal (30-35), sawdust (18-25), ochre (15-20), calcium powder (10-12), lentinan (1-2), phenyltriethoxysilane (3-4), manganese carbonate (2-4), sweet potato slag (3-5), modified maize straw (8-10), boric acid (2-4), manganese chloride (1-2), blueberry (10-15), cauliflower (15-20), spinach (10-12), cabbage (15-20) and Bacillus (2-4).    USE - Nitrogen, phosphorus and potassium containing special fertilizer for cultivation of licorice (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nitrogen, phosphorus and potassium containing special fertilizer, which involves:    (A) weighing each raw material;    (B) taking wooden meal, ochre and calcium powder, and then putting at 180-250 degrees C for 3-4 hours;    (C) adding sweet potato residue, modified maize straw, cauliflower, spinach and cabbage residue, and then grinding to obtain powder;    (D) adding other material to the powder; and    (E) heating the mixture at 75-80 degrees C, and then stirring and granulating to obtain the finished product.
NOVELTY - A livestock manure anti-cropping agent comprises 200-300 pts. wt. chicken manure, 200-300 pts. wt. pig manure, 200-300 pts. wt. mushroom residue, 10-15 pts. wt. composite fermenting agent, 10-15 pts. wt. ferrous sulfate, 10-15 pts. wt. ammonium citrate, 15-20 pts. wt. boric acid, 7-10 pts. wt. zinc sulfate, 8-10 pts. wt. heteroauxing, 20-25 pts. wt. attapulgite and 20-25 pts. wt. functional composite microbial inoculum.    USE - Livestock manure anti-cropping agent.    ADVANTAGE - The anti-cropping agent improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of livestock manure anti-cropping agent comprising mixing chicken manure, pig manure and mushroom residue, adjusting water, adding composite fermenting agent, crushing, sieving, adding ferrous sulfate, ammonium citrate, boric acid, zinc sulfate, heteroauxing and attapulgite, mixing, adding nitrogen, phosphorus and potassium nutrient, granulating, adding functional composite microbial inoculum preparation, and drying at 50 degrees C.
NOVELTY - A fruit tree special fertilizer comprises base fertilizer and foliage fertilizer. The base fertilizer comprises organic fertilizer, urea, monoammonium phosphate and potassium chloride. Foliage fertilizer comprises urea, monopotassium phosphate, agricultural chitosan oligosaccharide, 6-benzylaminopurine, paclobutrazol, triazolone, polyethylene glycol 200, sodium tetraborate, copper sulfate, ferrous sulfate, zinc sulfate, manganese sulfate, magnesium chloride and balance water.    USE - Fruit tree special fertilizer.    ADVANTAGE - The fertilizer increases moisture retention.    DETAILED DESCRIPTION - A fruit tree special fertilizer comprises base fertilizer and foliage fertilizer. The base fertilizer comprises 2800-3200 pts. wt. organic fertilizer, 250-300 pts. wt. urea, 150-200 pts. wt. monoammonium phosphate and 150-200 pts. wt. potassium chloride. Foliage fertilizer comprises 10-15 wt.% urea, 3-5 wt.% monopotassium phosphate, 0.3-0.5 wt.% agricultural chitosan oligosaccharide, 0.1-0.2 wt.% 6-benzylaminopurine, 0.1-0.2 wt.% paclobutrazol, 1-2 wt.% triazolone, 3-5 wt.% polyethylene glycol 200, 0.1-0.2 wt.% sodium tetraborate, 0.01 wt.% copper sulfate, 0.03 wt.% ferrous sulfate, 0.03 wt.% zinc sulfate, 0.01 wt.% manganese sulfate, 0.02 wt.% magnesium chloride and balance water. An INDEPENDENT CLAIM is included for preparation of fruit tree special fertilizer comprising crushing chicken manure, adding corn, rice hull, fruit tree leaf, bean cake and needle mushroom slag, stirring, spray drying, adding microbial inoculum, fermenting for 7-10 days at 28-36 degrees C, drying, granulating to obtain organic fertilizer, mixing organic fertilizer, urea, monoammonium phosphate and potassium chloride to prepare base fertilizer, taking foliage raw materials, and mixing.
NOVELTY - Preparation of organic-inorganic compound fertilizer includes mixing 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite to obtain component A, mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B, crushing red plum dried roots to obtain component C, mixing 1 pt. wt. baking powder and 45-55 pts. wt. and livestock manure, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran and 1 pt. wt. yeast, fermenting for 40-45 days, adding 200 pts. wt. charcoal powder to obtain component D and mixing all components.    USE - Method for preparing organic-inorganic compound fertilizer comprises used for red plum (claimed).    ADVANTAGE - The fertilizer is environment-friendly and increases yield of red plum to 13-20%.    DETAILED DESCRIPTION - Preparation of organic-inorganic compound fertilizer comprises taking 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite, stirring at 60-65 degrees C for 10-15 minutes and cooling to obtain component A; mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B; crushing red plum dried roots and sieving into 100-mesh sieve to obtain component C; mixing 1 pt. wt. baking powder, 9-11 pts. wt. red plum root powder and 45-55 pts. wt. and livestock manure, fermenting for 40-45 days, stirring after every 9 days, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran, 50 pts. wt. tea seed meal, 39 pts. wt. soybean meal and 1 pt. wt. yeast, fermenting at 65-75 degrees C for 40-45 days and adding 200 pts. wt. charcoal powder to obtain component D; and mixing 1 pt. wt. component A, 1 pt. wt. component B, 1 pt. wt. component C and 7-13 pts. wt. component D to obtain compound fertilizer containing nitrogen, phosphorus pentoxide, potassium oxide and organic matter at 15%:18%:12%:55% and granulating.
NOVELTY - The device has a gasification reaction chamber (4) whose upper portion is provided with a gas supply tube (5), and middle portion is provided with a steam distributing tube (7). A baffle carbon is provided in lower portion of the gasification reaction chamber. An active carbon discharging cavity is provided with a rotary scraper and an active carbon spraying tube. A grate (8) and a grate external power mechanism (12) rare connected with the furnace outer cavity gas exhaust line (13).    USE - Biomass gasification and active carbon producing device.    ADVANTAGE - The efficient use of the biomass resource is achieved, and the economic benefit is increased. The active carbon co-production is performed environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for biomass gasification and active carbon producing device.    Gasification reaction chamber (4)    Gas supply tube (5)    Steam distributing tube (7)    Grate (8)    Grate external power mechanism (12)    Furnace outer cavity gas exhaust line (13)
NOVELTY - Method for cultivating orange, involves planting orange seedlings in sandy soil of 6-6.7 pH, and fertilizing soil using 16-20% potash, 9-19% nitrogen, 55-65% organic fertilizer, 7-11% rapeseed and 0.3-0.6% fermentation agent, where the organic fertilizer includes manure, straw powder, ash and organic waste, and amount of the fertilizer applied is 45-55 kg/mu.    USE - The method is useful for cultivating orange (claimed).    ADVANTAGE - The method promotes yield of the orange, improves quality of orange, and is cost-effective.
NOVELTY - The apparatus (2) has a photovoltaic installation (4) which is provided with a photovoltaic module (10) for generating a direct current voltage (U) conductively coupled to an electric intermediate circuit (18). A central photovoltaic inverter (16) supplies power to a power grid (22), and an electrolyzer (6). The electrolyzer is directly connected to the electric intermediate circuit.    USE - Apparatus for photovoltaic production of hydrogen from hydrogen-containing compounds.    ADVANTAGE - The hydrogen photovoltaic generation is optimized, so that energy from the power supply is ensured. The hydrogen photovoltaic generation is relatively at low cost, so that extraction of energy from the grid is enhanced. The cost of the transformation of the exchange energy provided through the power distribution network is reduced effectively. The overall efficiency of the apparatus is improved effectively, as the reduction of the hardware overhead is realized. The direct connection of the electrolyzer at the intermediate voltage of the cost of a conversion of the alternating current power grid is eliminated. The performance is optimized, so that efficiency of the converter is improved effectively. The need for additional power measurement is not required.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for photovoltaic production of hydrogen from hydrogen-containing compounds.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for photovoltaic production of hydrogen.    Apparatus for photovoltaic production of hydrogen (2)    Photovoltaic installation (4)    Electrolyzer (6)    Photovoltaic module (10)    Photovoltaic inverter (16)    Electric intermediate circuit (18)    Power grid (22)    Direct current voltage (U)
NOVELTY - The system has first and second engageable arms (56,54) that are engaged to a top surface of a tamper platen. A brace bar is provided with the first and second ends and configured to position and re-position under and in contact with an external surface of a bottom floor of a compost receptacle at the first and second location respectively. The first and second hydraulic pistons (70,72) are removably coupled directly or indirectly at one end to the first and second engageable arms and the opposite end to the first and second ends of the brace bar respectively.    USE - Mushroom compost compacting system for composting mushroom compost.    ADVANTAGE - Since the engageable arms is quickly disconnected from the hydraulic cylinders or pistons, or the first and second trolley fixtures, the mushroom grow time cycle is reduced and thus more consistent compost compaction is produced to enhanced yield in a shorter grow time cycle. Since the roller assembly is mounted at a distance that is spaced apart from the front end or proximal end of the compost receptacle, the space is left at the front end or proximal end of the compost receptacle and thus the?worker is permitted to introduce mushroom compost onto the web or conveyor or liner. The tamper platen and braces are formed of a material that does not easily corrode or rust to withstand compressive forces. Since the upper portion is in contact with the bottom surface of the tamper platen and the lower portion is in contact with the bottom of the compost receptacle, the compost material is provided with uniform degree of compression.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of the mushroom compost compacting system.    Sidewalls (20)    Engageable arms (56,54)    Hydraulic pistons (70,72)    Trolley fixture (80,82)    Guide rail (102,104)
NOVELTY - Manure comprises livestock excretion and food waste, where the excretion is free of odor. The manure is prepared by mixing livestock excretion and food waste, adding mixture into culture medium, inoculating Bacillus safensis strain ESJ (KACC 91902P) and culturing mixture, where the medium comprises by-product of pine nut.    USE - As manure.
NOVELTY - An aryl vinyl ketone compound (I) is cyclization-reacted in presence of an ionic liquid, to obtain a 1-indanone compound (II).    USE - Manufacture of 1-indanone compound used as raw material for catalyst of polymer synthesis, pharmaceuticals and agrochemicals.    ADVANTAGE - The method enables manufacture of 1-indanone compound without using an organic solvent, by environmentally-friendly process.    DETAILED DESCRIPTION - An aryl vinyl ketone compound of formula (I) is cyclization-reacted in presence of an ionic liquid, to obtain a 1-indanone compound of formula (II).    R1=H, halo, 1-10C alkyl or 1-10C aryl;and    R2=H or 1-10C alkyl.
NOVELTY - Producing hydrocarbons, comprises (a) anaerobically fermenting a fermentable raw material to produce volatile fatty acids; (b) elongating the volatile fatty acids produced in step (a) by fermentation with at least one bacterium of Megasphaera genus and extraction of the fatty acids produced from the fermentation broth; and (c) subjecting the fatty acids produced in step (b) to a Kolbe electrolysis.    USE - The method is useful for producing hydrocarbons, which are useful as biofuels, petrol and diesel.    ADVANTAGE - The method provides hydrocarbons form biomasses in an economical and ecological manner.
NOVELTY - Agricultural carrier comprises Bacillus subtilis FB17.    USE - The agricultural carrier is useful for enhancing the characteristic of a plant including corn plant, soybean plant, rice plant, tomato plant, Zinnia plant, barley plant, and bioenergy crop plant, where the characteristic of a plant includes increasing biomass, increasing drought tolerance, decreasing lignin content, increasing seed germination, increasing iron concentration and increasing tolerance to pathogens (all claimed), such as fungal pathogens. The resulting plants are useful in the production of biofuels and food. The ability of the agricultural carrier to treat fungal infections was tested against Magnaporthe oryzae in rice. The result showed that the Bacillus subtilis FB17 exhibited the percentage reduction of 75.59.
NOVELTY - Method for producing oil from algae, involves introducing a biological agent capable of biologically rupturing a cell wall and oil vesicles of an oil-producing algae into the oil-producing algae to release oil and allowing the agent to rupture the algae and release the oil.    USE - The method or system is useful for producing oil from algae which is used as biodiesel (claimed) which is used in transportation.    ADVANTAGE - The method is cost-effective and suitable for large-scale industries.    DETAILED DESCRIPTION - Method for producing oil from algae, involves (a) introducing a biological agent capable of biologically rupturing a cell wall and oil vesicles of an oil-producing algae into the oil-producing algae to release oil and allowing the agent to rupture the algae and release the oil, or (b) cultivating an oil-producing algae chosen from diatoms, green algae, blue-green algae, golden-brown algae, haptophytes, and their mixtures and extracting an algal oil from the oil-producing algae by biologically rupturing cell wall and oil vesicles of the oil-producing algae using a biological agent. An INDEPENDENT CLAIM is included for system which comprises algae growth reservoirs including a carbon dioxide source and a mixing mechanism configured to circulate an oil-producing algae within the algae growth reservoirs, an oil extraction bioreactor operatively connected to the algae growth reservoirs and configured for biologically rupturing algal oil vesicles of the oil-producing algae to form an algal oil and algal residue, and a biological agent source operatively connected to the oil extraction bioreactor, where the agent source comprises a biological agent that is capable of rupturing a cell wall and oil vesicles of the oil-producing algae.
NOVELTY - Method of preparing onion manure, involves mixing onion by-product, livestock excretion and microbial composition, drying the mixture, pulverizing, transferring to fermentation culture, then adding onion powder, jade powder, rice bran, protein source, oyster shell, distiller's grain, soybean cake and molasses, adding the bean-curd residue to the above mixture, then fermenting the mixture and drying the fermented product, where the microbial composition includes Lactobacillus casei and L.acidophilus.    USE - The method is useful for preparing onion manure (claimed).    DETAILED DESCRIPTION - Method of preparing onion manure, involves mixing 40-60 wt.% onion by-product, 10-50 pts. wt. livestock excretion and 1-10 pts. wt. microbial composition, drying the mixture, pulverizing the mixture to 80-150 meshes sieve size, transferring to fermentation culture, then adding 20-30 wt.% onion powder, 20-30 wt.% jade powder, 40-50 wt.% rice bran, 2-5 wt.% protein source, 1-5 wt.% oyster shell, 1-5 wt.% distiller's grain, 2-5 wt.% soybean cake and 0.1-1 wt.% molasses, adding the bean-curd residue to the above mixture, then fermenting the mixture at room temperature for 24-48 hours and drying the fermented product at 30-40 degrees C for 36-48 hours until the water content is 35-40%, where the microbial composition comprises Lactobacillus casei, L.acidophilus, L.plantarum, L.brevis, Streptococcus faecalis, Bacillus subtilis and B.putrificus. An INDEPENDENT CLAIM is included for onion manure prepared by the above method.
NOVELTY - The cell for electrolyzing water with electromagnetic separation process of two generated gases, preferably hydrogen and oxygen, by combined use of an electric field between three electrodes (19, 20, 21) and a magnetic field created by two magnetic circuits (14, 16) for the physical separation of two generated gases, is claimed. A high voltage alternating current is applied between the electrodes for dissociation of the water, and an alternating magnetic field of the same frequency is applied for electrolyzing the water using current created by two inductors (24, 25) in magnetic circuits.    USE - The cell is useful for electrolyzing water such as pure water, reverse osmosis water and demineralized water (all claimed) with electromagnetic separation of hydrogen and oxygen.    ADVANTAGE - The cell electrolyzes the water with less amount of current and without clogging and damaging the electrodes.    DETAILED DESCRIPTION - The cell for electrolyzing water with electromagnetic separation process of two generated gases, preferably hydrogen and oxygen, by combined use of an electric field between three electrodes (19, 20, 21) and a magnetic field created by two magnetic circuits (14, 16) for the physical separation of two generated gases, is claimed. A high voltage alternating current is applied between the electrodes for dissociation of the water, and an alternating magnetic field of the same frequency is applied for electrolyzing the water using current created by two inductors (24, 25) in the magnetic circuits. The cell is supplied with pressurized water through an injector for electronic regulation of the internal water level in the cell. Separate outlets (3, 4) collect the two recovered gases separated under pressure.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of a cell for electrolyzing water.    Outlets (3, 4)    Magnetic circuits (14, 16)    Gases (17, 18)    Electrodes (19, 20, 21)    Inductors. (24, 25)
NOVELTY - System (100) comprises: a fermentation sub-system (102) for fermenting a carbon source with microorganism to produce a fermentation broth comprising L-glutamic acid; a microfiltration sub-system (104) for separating the microorganism from the fermentation broth; and a nanofiltration sub-system (106) for recovering L-glutamic acid.    USE - The system is useful to produce L-glutamic acid from carbon sources, preferably sugarcane juice (all claimed). The L-glutamic acid is useful: to decrease or prevent nerve damage caused by anticancer drug; to improve CNS function and cortical brain function for neurasthenia patients; and as a nitrogen source in the culture of Aspergillus fumigatus for fumagillin production. No biological data given.    ADVANTAGE - The system is capable of continuously producing L-glutamic acid from renewable carbon sources with high yield and purity in a simple and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous production of L-glutamic acid, comprising (a) fermenting a carbon source in a fermentation system with microorganism to produce a fermentation broth comprising L-glutamic acid, separating the microorganism from the fermentation froth and recovering L-glutamic acid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a system for continuous production of L-glutamic acid from renewable carbon source.    System for continuous production of L-glutamic acid (100)    Fermentation sub-system (102)    Microfiltration sub-system (104)    Nanofiltration sub-system (106)    Feed tank. (108)
NOVELTY - N-Methyl-2-ketone compound preparation involves oxidizing methyl thiazole-based compound with copper salt and an oxidizing agent in an organic solvent in inert atmosphere to give N-methyl-thiazol-2-ketone compound.    USE - Method for preparing N-methyl-2-ketone compound (claimed).    ADVANTAGE - The method prepares N-methyl-2-ketone compound in a simple, eco-friendly and cost-effective manner with high yield by using cheap catalyst under high reaction activity and mild reaction conditions in a reduced reaction time.
NOVELTY - Alicante medoxomil preparation involves oxidizing trityl losartan under alkaline conditions in presence of catalyst in polar organic solvent under appropriate temperature conditions, where the reaction mixture is filtered to obtain a filtrate containing aldehyde compound (I). The obtained filtrate is oxidized in acidic conditions at suitable temperature by using an oxidizing agents to obtain carboxylic compound (III).    USE - Method for preparing Alicante medoxomil (claimed).    ADVANTAGE - The method prepares the Alicante medoxomil in a simple, cost-effective and eco-friendly manner with high yield at industrial scale.    DETAILED DESCRIPTION - Alicante medoxomil preparation involves oxidizing trityl losartan under alkaline conditions in presence of catalyst in polar organic solvent under appropriate temperature conditions, where the reaction mixture is filtered to obtain a filtrate containing aldehyde compound of formula (I). The obtained filtrate is oxidized in acidic conditions at suitable temperature by using an oxidizing agents to obtain carboxylic compound of formula (II). The oxidizing agent is selected form hydrogen peroxide, sodium chlorite, resorcinol, sodium chlorite, amino acid, sodium chlorite, 2-methyl-2-butene or sodium chlorite. The obtained carboxylic compound is treated with methyl isopropyl carbonate at suitable temperature to form diketone compound of formula (III). The obtained diketone compound is de-protected for producing Alicante medoxomil, which is refined and purified to give Alicante medoxomil.
NOVELTY - Anti-platelet aggregation drug ticagrelor preparation involves reacting (1S,2S,3R,5S)-3-amino-5-(2-hydroxyethyl)cyclopentane-1,2-diol with a nitro pyridine compound (I) in presence of an alkali to give cyclopentane compound (II). The obtained cyclopentane compound (I) is reduced for producing amino cyclopentane compound (III), which is treated with an alkali metal to give a thio pyridine compound (II). The obtained thio pyridine compound (II) or its salt is treated with a 2-(3,4-difluorophenyl)cyclopropan-1-amine in presence of an alkali to give the desired compound ticagrelor.    USE - Method for preparing anti-platelet aggregation drug ticagrelor (claimed).    ADVANTAGE - The method prepares anti-platelet aggregation drug ticagrelor in a simple, cost-effective and eco-friendly manner on industrial scale.    DETAILED DESCRIPTION - Anti-platelet aggregation drug ticagrelor preparation involves reacting (1S,2S,3R,5S)-3-amino-5-(2-hydroxyethyl)cyclopentane-1,2-diol with a nitro pyridine compound of formula (I) in presence of an alkali to give cyclopentane compound of formula (II). The obtained cyclopentane compound of formula (II) is reduced for producing amino cyclopentane compound of formula (III), which is treated with an alkali metal to give a thio pyridine compound of formula (IV). The obtained thio pyridine compound of formula (IV) or its salt is treated with a 2-(3,4-difluorophenyl)cyclopropan-1-amine in presence of an alkali to give the desired compound ticagrelor.    Y'=selected from halogen, R7C(O)O acyloxy or R8S(O2)O carbamate;    R7=selected from 1-6C alkyl, trifluoromethyl or aryl group; and    R8=1-6C alkyl, 1-6C fluoroalkyl or aryl group.
NOVELTY - Soil repairing agent comprises Bacillus laterosporus spores, B.subtilis spores, organic fertilizer, peat and sepiolite, where number of viable bacterial spores in the agent is greater than 2x 107/g, number of viable B.laterosporus is 40-60% and number of viable B.subtilis is 40-60%.    USE - The soil repairing agent is useful for degrading heavy metals in soil and increasing fertility and activity of soil humus and microorganisms.    ADVANTAGE - The soil repairing agent improves biological environment of soil, soil structure, water retention property of soil, and yield and quality of agricultural product, reduces damage of soil with respect to pest.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves mixing B.laterosporus spores, B.subtilis spores, organic fertilizer, peat and sepiolite.
NOVELTY - Agent comprises Bacillus sp. strain CBW4 (KACC91722P), or Bacillus sp. strain EBW4 (KACC91749P) or its culture material, as an active ingredient. The strain is isolated from lugworm.    USE - The agent and method are useful for purifying organic wastewater. The agent is useful as microbial cleaning agent for organic wastewater (all claimed).    ADVANTAGE - The agent has excellent resistance to salinity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for purifying organic wastewater; and    (2) method for preparing the above-mentioned agent for purifying organic wastewater.
NOVELTY - Preparation of 4-hydroxythieno(3,2-d)pyrimidine-7-carboxylic acid (I) involves halogenating triazaindene compound (IV) to obtain indene compound (III), oxidizing resulting compound to produce indene carbaldehyde (II), and oxidizing resulting compound.    USE - Preparation of 4-hydroxythieno(3,2-d)pyrimidine-7-carboxylic acid for producing 4-chloro-thieno(3,2-d)pyrimidine-7-carbonyl chloride (all claimed).    ADVANTAGE - 4-Hydroxythieno(3,2-d)pyrimidine-7-carboxylic acid having high purity is produced economically with high yield, without affecting the environment.    DETAILED DESCRIPTION - Preparation of 4-hydroxythieno(3,2-d)pyrimidine-7-carboxylic acid of formula (I) involves halogenating triazaindene compound of formula (IV) to obtain indene compound of formula (III), oxidizing resulting compound to produce indene carbaldehyde of formula (II), and oxidizing resulting compound.    X=halo;and    Z=halo or hydroxy.    An INDEPENDENT CLAIM is included for preparation of 4-chloro-thieno(3,2-d)pyrimidine-7-carbonyl chloride of formula (V), which involves chlorinating 4-hydroxythieno(3,2-d)pyrimidine-7-carboxylic acid (I).
NOVELTY - The fuel cell system (100) has an oxidant gas supply device (6) which supplies an oxidant gas to a catalyst (4). A controller (7) is provided to control the oxidant gas supply device and performs oxidation-treatment of the catalyst before taking out the catalyst outside from container. The base metal is contained in the catalyst. The conversion catalyst, hydrodesulfurization catalyst, methanation catalyst and modification catalyst are used. A carbon monoxide removal device reduces carbon monoxide in a hydrogen-containing-gas by oxidation reaction.    USE - Fuel cell system.    ADVANTAGE - The controller is provided to control the oxidant gas supply device and to perform oxidation-treatment of catalyst before taking out catalyst outside, thus the emitted-heat amount by the oxidation reaction of the catalyst is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.    Fuel cell (3)    Catalyst (4)    Oxidant gas supply device (6)    Controller (7)    Fuel cell system (100)
NOVELTY - Method of producing fuel ethanol using wood fiber as raw material, involves adding sulfonated cooking liquor into wood fiber, heating the material using microwave at 100-120 KPa and 110-130 degrees C, boiling the filtered material, adding sodium acetate buffering liquid into the residue, performing hydrothermal reaction at 110-130 degrees C and obtaining the finished product.    USE - The method is useful for producing ethanol using wood fiber as raw material (claimed).    ADVANTAGE - The method reduces sulfonating temperature by more than 40 degrees C, efficiently degrades cellulose, reduces hydrothermal reaction temperature by more than 60 degrees C, consumes less energy and reduces generation of fermentation inhibitor.
NOVELTY - Alkyl trityl phenyl ether compounds (I) are new.    USE - (I) are useful for marking the petroleum hydrocarbon or liquid biologically derived fuels (claimed) and oils such as crude oil, lubricating oil, hydraulic fluid, brake fluid, gasoline, diesel fuel, kerosene, jet fuel and heating oil.    ADVANTAGE - (I) have improved solubility properties.    DETAILED DESCRIPTION - Alkyl trityl phenyl ether compounds of formula (I) are new.    R1-R3 = 1-6C alkyl;    R4 = 1-18C alkyl or 4-18C heteroalkyl;    m = 0-3;    n = 1-3; and    j-s = 0-2, with provided that at least one of j-s is not zero.    An INDEPENDENT CLAIM is included for marking a petroleum hydrocarbon or a liquid biologically derived fuel, comprising adding the petroleum hydrocarbon or liquid biologically derived fuel to (I), where (I) are present at a level of 0.01-20 ppm.
NOVELTY - The method involves mixing organic sludge with the organic solvent under a normal temperature and normal pressure. The solvent containing organic sludge having volatile property is provided in a mixing tank (4). A sludge feed route (45) is passed from the mixing tank. The solvent containing organic sludge (B) is supplied to a filter press (5). The compressed air (12) is made to flow backward to the sludge feed route, and the remained solvent containing organic sludge is collected from the dehydrator side after spin-drying.    USE - Method for collecting organic solvent in dehydrating system of organic sludge (claimed) such as used tea leaves in sewage treatment.    ADVANTAGE - The organic solvent currently mixed in the organic sludge which remained on the sludge feed route from the mixing tank to the dehydrator is collected and recycled. The used quantity of the organic solvent newly added is reduced. The alcohol solvent is used effectively, without wasting. The moisture content of organic sludge is reduced easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the dehydrating system of the organic sludge. (Drawing includes non-English language text)    Mixing tank (4)    Filter press (5)    Compressed air (12)    Sludge feed route (45)    Solvent containing organic sludge (B)
NOVELTY - A zinc complex having repeating unit (I), is new, and exhibits an octahedral structure.    USE - New zinc complex is used as catalyst for acylating hydroxyl group, carbonating hydroxyl group, and deacylating carboxylate ester (all claimed), pharmaceutical intermediate, functional material and structural material.    ADVANTAGE - The zinc complex has excellent stability, and is prepared efficiently by economical and environmentally-friendly process. The catalyst containing the zinc complex has high catalytic activity.    DETAILED DESCRIPTION - A zinc complex having repeating unit of formula (I), is new, and exhibits an octahedral structure.    L=linker moiety;and    R1=1-4C alkyl or 1-4C alkyl having halo.    INDEPENDENT CLAIMS are included for the following:    (1) catalyst, which consists of zinc complex;    (2) method of acylating hydroxyl group, which involves reacting carboxylic acid or its ester in presence of catalyst;    (3) method of carbonating hydroxyl group, which involves reacting carbonate ester in presence of catalyst;    (4) method of deacylating carboxylate ester, which involves deacylating carboxylate ester in presence of the catalyst; and    (5) manufacture of zinc complex.
NOVELTY - The hydrogen water formation apparatus (1000) has cable (340) which is provided to connect hydrogen water production rod (100) and controller (300), so that the power source and control sign are supplied to hydrogen water production rod and electrolysis action and hydrogen production rod are controlled. The power is permitted in hydrogen water production rod so as to adjust the hydrogen water generation time. The hydrogen water production rod is inserted into container in which natural water bottle or water is held to generate the hydrogen water.    USE - Apparatus for forming hydrogen water filled in water bottle accommodated in bag and vehicle using electrode.    ADVANTAGE - The aging and disease occurred to the human being is prevented. The water-tightness between the top portion and bottom portion of the hydrogen water formation apparatus are maintained efficiently. The functional hydrogen water is produced efficiently. The waste product in the hydrogen water is removed effectively. The efficiency of the alkaline water is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen water formation apparatus. (Drawing includes non-English language text)    Hydrogen water production rod (100)    Controller (300)    Cable (340)    Electrolysis control knob (370)    Hydrogen water formation apparatus (1000)
NOVELTY - Method for biosynthesis of reduced graphene oxide involves (a) culturing Bacillus mycoides strain 001 in a liquid culture medium until it reaches log phase, and collecting culture supernatant, and (b) adding the obtained culture supernatant to graphene oxide solution in volume ratio of 1:1, increasing pH of the obtained solution to 9 and reacting the resulting solution for 5 minutes to obtain product.    USE - The method is useful for biosynthesizing reduced graphene oxide (claimed), which is used in electronic, environment, agriculture and biomedical applications.    ADVANTAGE - The method is simple, rapid, environmentally-friendly and cost-effective and ensures to synthesize reduced graphene oxide stable at normal temperature.
NOVELTY - Boronic acid containing ratiometric fluorescent chemosensor (I) capable of selectively binding to mercury(II) ion, is new.    USE - (I) is useful for selectively detecting mercury(II) ions (claimed) in ground water, water environments (rivers), and biological samples.    ADVANTAGE - (I) can selectively detect mercury(II) ions in 100% aqueous solution or aqueous organic solution in presence of other metal ions by measuring fluorescent intensity, thus quantitative analysis of mercury(II) ions in the sample is easily performed; can be separated from the analyte; and is environmentally friendly.    DETAILED DESCRIPTION - Boronic acid containing ratiometric fluorescent chemosensor of formula (I) capable of selectively binding to mercury(II) ion, is new.    R=-NR1R2 or -OR1;    R1, R2=H or 1-6C alkyl;    Q, W1=6-12C aryl boronic acid (optionally substituted by halo, 1-4C haloalkyl, OH, 1-4C alkoxy, amine or nitro), pyrenyl or anthracenyl;    Z1, Z2=-C(=O)-, -CH2- or -S(=O)2-;    l, m=0-3; and    n=1-6.    Provided that: Q and W1 are different; one of Q and W1 is 6-12C aryl boronic acid; and at least one of Z1 and Z2 is -C(=O)-. INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) detecting mercury(II) ions, comprising adding (I) to the sample in which presence or absence of mercury(II) ions is to be detected, and selectively detecting mercury(II) ions by measuring fluorescent signal generated by reaction product generated by the formation of covalent bond between mercury(II) ions and (I).
NOVELTY - Nifuratel preparation involves mixing epichlorohydrin and sodium thiomethoxide in presence of phase transfer catalyst for performing substitution reaction at 95-98 degrees C to obtain propylene sulfide. The obtained product is mixed with hydrazine hydrate in presence of methanethiol to obtain 3-(methylthio)-2-hydroxy-propyl hydrazine, which is heated with dimethyl carbonate or diethyl carbonate to obtain N-amino-5-methylthio-2-oxazolidinone. The obtained product is mixed with 5-nitrofurfural under dark conditions for performing condensation reaction to obtain desired product.    USE - Method for preparing nifuratel (claimed).    ADVANTAGE - The method enables to prepare nifuratel in eco-friendly manner with high yield and high purity of product.
NOVELTY - Preventing and treating hawthorn anthracnose, involves (a) implementing whole garden hawthorn growing grass to 10-20 cm deep, and planting the whole garden grass in early October, (b) planting for 7-8 months under shade net, and (c) adding Chinese medicinal herb extraction liquid, and obtaining product.    USE - The method is useful for preventing and treating hawthorn anthracnose (claimed).    ADVANTAGE - The method is environmentally-friendly and cost-effective, has no residues, and 99.3% efficiency.
NOVELTY - A soil free diatomaceous earth composite is produced by crushing and drying carbon slurry, adding lime, peat, straw, manure and sawdust, fermenting, compacting, drying, treating with sulfuric acid, adding diatomite, coal, and ammonium hydrogen carbonate, sealing, adding zinc sulfate, magnesium sulfate and potassium sulfate, stirring with celite water degradable polymer, heating, cooling, filtering, separating, washing with deionized water, and precipitating.    USE - Method for producing soil free diatomaceous earth composite used for ginseng culture (claimed).    ADVANTAGE - The composite improves yield and mass of ginseng.    DETAILED DESCRIPTION - A soil free diatomaceous earth composite is produced by crushing dried peat, adding lime, stirring uniformly, adjusting pH to 7.0-7.2, adding peat, straw, manure and sawdust, mixing uniformly, fermenting at 60-70degreesC for 10-15 days, compacting, drying, treating with 15-30% dilute sulfuric acid, adding 20-30% diatomite, coal, and ammonium hydrogen carbonate, sealing at 20?o C for 12-15 days, adding zinc sulfate, magnesium sulfate and potassium sulfate and preparing celite water degradable polymer composite material by stirring with 100 g dispersing agent comprising Span 60, 15 g acrylate, 20 g celite, 20 g starch, 1 g potassium persulfate initiator and 1 g crosslinking agent in 200 ml cyclohexane for stirred 30 -60 minutes, increasing the temperature to 70-75degreesC, reacting for 2-3 hours, cooling the solution to room temperature with stirring, separating by suction and washing with deionized water to give a white precipitate of diatomite composite water degradable polymer materials;    from soluble reacting with added cyclohexane, stirring for 30-60 minutes, heating at 70-75degreesC for 2-3 hours, cooling to room temperature, filtering, separating, washing with deionized water and precipitating.
NOVELTY - The system has two spacers for regularly maintaining interval formed among multiple laminated dielectric plates. The laminated dielectric plates are connected to an external power supply unit. A dielectric barrier discharge apparatus is installed at an internal space of a chamber. A flow separation board is installed in a front side of the dielectric barrier discharge apparatus for uniformly diffusing steam. Multiple through-holes are formed in a central part of the flow separation board to allow flow of the steam into an inner side of the flow separation board.    USE - System for gasifying water by using a low temperature plasma device for producing high concentration hydrogen.    ADVANTAGE - The system passes the steam through the dielectric barrier discharge apparatus, and a low temperature plasma device is operated at atmospheric pressure condition, so that yield of high concentration hydrogen and aqueous gasification reactivity can be increased and requirement of expensive catalyst is avoided.    DETAILED DESCRIPTION - The dielectric plates are made of aluminum oxide/alumina. The spacers are made of acrylic matter. An INDEPENDENT CLAIM is also included for a method for gasifying water by using a low temperature plasma device for producing high concentration hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for gasifying water by using a low temperature plasma device for producing high concentration hydrogen. '(Drawing includes non-English language text)'
NOVELTY - The system has a fuel oil feedstock injector connected to a first end of a reactor and injecting a fuel oil feedstock into the reactor. A first polyol feedstock injector is connected at or near the first end of the reactor, and injects a polyol feedstock into the reactor. A second polyol feedstock injector is connected to the reactor at a location that is more proximate to a second end of the reactor than the first polyol feedstock injector, where each polyol feedstock injector injects and mixes the polyol feedstock with the fuel oil feedstock and a hydrotreating catalyst to generate alkanes.    USE - System for producing renewable fuels from biomass e.g. carbohydrates, starches and lignins, in petroleum industries.    ADVANTAGE - The system demonstrates hydrotreating of the liquefied biomass feedstock with a diesel feedstock to produce alkanes to prevent damage to the reactor catalyst, reduce coke production and convert nearly all of the polyols to alkanes. The diesel feedstock is fed over the reactor catalyst with multiple injections of the polyol feedstock along the reactor to mitigate a potential coking issue and to moderate temperature of the catalyst bed while maintaining high conversion for sugar alcohol to hydrocarbon through the hydrotreating process.    DETAILED DESCRIPTION - The fuel oil feedstock is selected from a group consisting of petrol, jet fuel, kerosene, heating oil, fuel oils, diesel fuel, petro-diesel, bio-diesel, synthetic diesel and blended diesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a process for hydrotreating sugar alcohols to hydrocarbons.
NOVELTY - The fuel cell system (100) has a temperature sensor (112) to sense temperature. A control unit (114) controls the driving of the fuel cell system according to the thermal energy generated in a fuel cell stack (106) at a fixed time interval. The fuel cell stack generates the thermal energy corresponding to temperature of the warm water stored in a radiator (110). The radiator stores the warm water that is heated while circulating in a heat exchanger (108), where the heat exchanger collects the warm water. The temperature sensor is provided in the lower part of the radiator.    USE - Fuel cell system.    ADVANTAGE - The control unit controls the driving of the fuel cell system according to the thermal energy generated in a fuel cell stack at a fixed time interval, and thus reduces the wastage related to energy, and also ensures that the efficiency of the fuel cell system is improved in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system. (Drawing includes non-English language text).    Fuel cell system (100)    Fuel cell stack (106)    Heat exchanger (108)    Radiator (110)    Temperature sensor (112)    Control unit (114)
NOVELTY - The apparatus has a component extraction module (20) with several separate vessels (22) within each of which a flow path is provided for mixture. Several membrane elements having flow tubes with membrane tubes are placed concentrically in vessels and sized to create an annular space. The component selectively permeates the membrane tubes in each vessel and steadily reduces the content of the component in the mixture when a mixture at a positive pressure enters the annular spaces around the membrane tubes and travels the length of the membrane element in each vessel.    USE - Apparatus for separating component from solvent/water vapor mixture for use in industries such as biofuels, water purification, hydrocarbon separation, and acid-gas separation.    ADVANTAGE - The cost required to construct the apparatus is reduced, a series of repeating smaller vessels each with multiple membranes that together form an overall module is used.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a component extraction module.    Component extraction module (20)    Vessel (22)    External frame (24)
NOVELTY - A dendritic amphiphilic block copolymer H-PLA-b-TPGS (I) is new.    USE - Dendritic amphiphilic block copolymer H-PLA-b-TPGS used for preparing drug loading nanoparticles, or drug loading microsphere composite tissue engineering bracket (all claimed).    ADVANTAGE - The method is simple and pollution-free. The copolymer has good biological compatibility and biological degradability.    DETAILED DESCRIPTION - An dendritic amphiphilic block copolymer H-PLA-b-TPGS of formula (I) is new.    m=16-42;    n=16-64;    H'=hyperbranched polyester Boltorn H20, H30 or H40; and    TPGS=radical of formula (II).    p=23.    An INDEPENDENT CLAIM is included for preparation of dendritic amphiphilic block copolymer H-PLA-b-TPGS (I).
NOVELTY - Fertilizer comprises (in pts.wt.): urea (40-50), sodium silicate (20-30), peat (10-15), calcium superphosphate (8-10), ferrous sulfate (3-5), magnesium chloride (2-4), straw (20-30), sodium sulfate (0.1-0.2), ammonium hydrogen carbonate (0.3-0.5), carboxymethyl cellulose (2-4), nano spherical iron oxide magnetic powder (5-6) and microbial inoculant (0.1-0.2).    USE - Fertilizer for cultivation of Atractylodes (claimed).    ADVANTAGE - The fertilizer improves physical and chemical properties of soil, increases the utilization ratio of fertilizer, and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing the nanometer sodium silicate, peat, straw powder, water and sizing agent;    (B) heating the mixture at 75-80 degrees C, and then adding urea, calcium phosphate, ferrous sulfate, magnesium chloride, magnesium sulfate, sodium persulfate and ammonium hydrogen carbonate;    (C) continuously grinding the mixture for 1-2 hours;    (D) adding carboxymethyl cellulose, nano spherical iron oxide magnetic powder and microbial inoculants to the mixture; and    (E) standing the mixture for 3-5 days, and then drying and granulating to obtain the product.
NOVELTY - The method involves peeling support base material (14) from an electrolytic membrane (12). A second catalyst layer (32) is joined to a side opposite to the side to which a first catalyst layer (22) of membrane is joined by passing through and pressing between a pair of rolls (62,64). Inspection of transfer defect and thickness of second catalyst layer joined to the membrane is conducted. The operation of rolls is feedback-controlled based on inspection of second catalyst layer. A second transfer base material (34) is peeled from second catalyst layer joined to the membrane.    USE - Method for manufacturing fuel cell (claimed).    ADVANTAGE - The catalyst layer is joined efficiently to the electrolytic membrane with improved quality. The manufacturing process is simplified, cost required for manufacturing fuel cell is reduced, resource-saved, and the usability of product is improved. The manufacturing error of product is reduced. The short circuit by the lack of thickness of membrane electrode assembly in fuel cell and the transfer defect of catalyst layer is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the membrane electrode assembly (MEA) production facility used to produce membrane electrode assembly.    Electrolytic membrane (12)    Support base material (14)    Catalyst layers (22,32)    Second transfer base material (34)    Rolls (62,64)
NOVELTY - Method for preparing 4-androstenedione by fermenting and degrading plant sterol using single water phase system, involves isolating Mycobacterium smegmatis strain from seed culture medium, emulsifying substrate, preferably plant sterol under the action of emulsifier, inoculating the M.smegmatis in a fermentation culture medium, adding emulsified plant sterol in fermentation culture medium, culturing, and extracting the finished product.    USE - The method is useful for preparing 4-androstenedione by fermenting and degrading plant sterol using single water phase system (claimed).    ADVANTAGE - The method provides increased yield as it utilizes emulsifier, is cost-effective and environmentally-friendly, and exhibits reduced stress and pollution to environment.
NOVELTY - A cellulosic biomass processing method includes the following steps (a) feeding cellulosic biomass into a storage container. (b) closing the storage container, and introducing carbon dioxide, until the pressure within the storage container is 10kPa to 7MPa. (c) introducing the hydrolysis solution into storage container, until the pressure within the storage container is 45MPa to 450MPa. (d) wait for a set time under the pressure and vent to give a sacchariferous solution or porous cellulosic porous biomass materials. By introducing hydrolysis solutioninto the storage container to produce a high pressure, enchance the solubility of carbon dioxide to produce a dilute acid catalyzed hydrolysis reaction, and both of the temperature and pressure is lower than conventional technologies, the capital cost and energy consumption is reduced.
NOVELTY - Production of molded solid fuel involves pulverizing low-grade coal, obtaining slurry by mixing pulverized low-grade coal and solvent oil, obtaining dehydrated slurry by heating and dehydrating slurry, obtaining cake by separating solvent oil from dehydrated slurry, obtaining powdery modified coal by heating cake, separating solvent oil from cake, and pressurizing and molding powdery modified coal using molding machine, without the addition/mixture of binder. In molding process, coolant is sprayed on the surface of molding machine.    USE - Production of molded solid fuel from low-grade coals e.g. wood coal and subbituminous coal.    ADVANTAGE - The method enables production of economical molded solid fuel with high strength. The temperature difference between surface, portion and interior is small. Occurrence of distortion is suppressed. The difference in moisture content between inside and surface portion by evaporation of water is inhibited by reduced humidification. High cooling effect is provided by water having high specific heat.    DETAILED DESCRIPTION - Production of molded solid fuel involves pulverizing low-grade coal, obtaining slurry by mixing pulverized low-grade coal and solvent oil, obtaining dehydrated slurry by heating and dehydrating slurry, obtaining cake by separating solvent oil from dehydrated slurry, obtaining powdery modified coal by heating cake, separating solvent oil from cake, and pressurizing and molding powdery modified coal using molding machine, without the addition/mixture of binder. In molding process, coolant is sprayed on the surface of molding machine. The surface temperature of molding machine is maintained at 100 degrees C or less.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the molding portion.    Molding chamber (61)    Material supply apparatus (63b)    Water spraying apparatus (64)    Sieve apparatus (65)    Recycle line (66)
NOVELTY - This utility new type relates to a livestock and poultry one with harmless mechanism fertilizer device, comprising a shell, a motor, a main shaft, a U-shaped fermentation jar, radial stir pole, stamp knife, a crusher, a power control box, a belt conveyor, a heating tube, part, set in a part of U-shaped fermentation jar, U-shaped fermentation jar with a main shaft set with inner shell, the right end of the main shaft and the motor is connected with a main shaft at intervals of fixed with several a uniform radial stir pole, radial stir end of pole is welded with stamp, U-shaped fermentation jar bottom outer side set with a heating tube, the heating tube is equipped with inner, U-shaped fermentation jar of a side wall mounting with sensor, a U-shaped fermentation jar of the bottom set with a discharging port, a discharging port lower end set with a belt conveyor, the shell body of upper end set with a rail, a rail set with an upper cover, upper end of the shell body and the upper cover corresponding to the fixed side wall with a crusher, a shell set with a human ladder, with an electric control box set up on the front end side wall of the shell.
NOVELTY - This utility new type relates to farm field, specifically a poultry waste one storage device, the storage device include main body, upper half part set on the ground upper part, lower half part set on the lower part the ground, the top front edge and rear edge are connected with the ground through a slope, a a storage device main body set with at least one upper part opening of a waste reservoir unit, waste reservoir unit inner wall and bottom set with a waterproof layer, a storage device main body set with a ceiling. This utility new type prevent dirt into a waste reservoir unit is convenient for people to save force operation, avoid the solarization and rain, prevent fertilizer effect, but also a valid preventing mosquito entering into, a waterproof layer preventing a waste leakage pollution, rear fermenting a kill bacteria, reduce the smell, waste reservoir unit in period for collecting excrement, staging fermentation, aritificial and machinery and it is convenient for loading and unloading operation, plate, a baffle plate and an inverted excrement opening a human and to prevent the careless falling into the waste in waste reservoir unit.
NOVELTY - Tricyclene, camphene or isoborneol as raw material is dissolved in organic solvent, and reacted in presence of catalyst and anhydrous oxalic acid. The catalyst and unreacted oxalic acid are removed by filtration, washed and supernatant liquid is removed by evaporating the solvent. The resulting mixture is subjected to steam distillation, unreacted camphene or tricyclene is removed, and the resulting material is recrystallized to obtain isobornyl oxalate.    USE - Synthesis of isobornyl oxalate (claimed).    ADVANTAGE - The method provides isobornyl oxalate with high yield under mild reaction condition, by a simple process.
NOVELTY - A traditional Chinese medicine comprises 6-14 pts. wt. Dysosma versipellis, 6-14 pts. wt. monkshood, 6-14 pts. wt. plantain, 6-14 pts. wt. white batryticated silkworm, 26-34 pts. wt. Serissa serissoides, 4-8 pts. wt. alum, 6-14 pts. wt. white ox bile, 26-34 pts. wt. Angelica dahurica, 4-8 pts. wt. herba schizonepetae and 11-19 pts. wt. Spatholobus stem.    USE - Traditional Chinese medicine in the form of lotion used for treating gestational pudendum eczema (all claimed).    ADVANTAGE - The medicine has mild adverse reactions, and high safety features.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of traditional Chinese medicine comprising: crushing Serissa serissoides, white ox bile, Angelica dahurica and herba schizonepetae into rough powder, steam distilling, extracting volatile oil, collecting, and mixing to obtain material A; distilling Dysosma versipellis, monkshood, plantain, white batryticated silkworm and Spatholobus stem, extracting volatile oil, adding 4-6 times and 3-5 times water, extracting for 2 hours and for 1.0 hours, combining, adding material A, filtering, concentrating at 60 degrees C to relative density of 1.09-1.13, cooling, adding ethanol to alcohol content of 65-75%, stirring uniformly, standing at 5 degrees C for 24 hours, filtering, recovering ethanol, concentrating at 60 degrees C to relative density of 1.07-1.12, water diluting, stirring, standing to 2-5 degrees C for 24 hours, and filtering; and adding alum, stirring, regulating pH to 4.5-6.0, adding 1000 pts. wt. water, filtering, and sterilizing.
NOVELTY - Preparation of organic-inorganic compound fertilizer includes mixing 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite to obtain component A, mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B, crushing tobacco dried roots to obtain component C, mixing 1 pt. wt. baking powder and 45-55 pts. wt. and livestock manure, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran and 1 pt. wt. yeast, fermenting for 40-45 days, adding 200 pts. wt. charcoal powder to obtain component D and mixing all components.    USE - Method for preparing of organic-inorganic compound fertilizer used for tobacco (claimed).    ADVANTAGE - The fertilizer is environment-friendly and increases yield of tobacco to 11-12%.    DETAILED DESCRIPTION - Preparation of organic-inorganic compound fertilizer comprises taking 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite, stirring at 60-65 degrees C for 10-15 minutes and cooling to obtain component A; mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B; crushing tobacco dried roots and sieving into 100-mesh sieve to obtain component C; mixing 1 pt. wt. baking powder, 9-11 pts. wt. tobacco root powder and 45-55 pts. wt. and livestock manure, fermenting for 40-45 days, stirring after every 9 days, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran, 50 pts. wt. tea seed meal, 39 pts. wt. soybean meal and 1 pt. wt. yeast, fermenting at 65-75 degrees C for 40-45 days and adding 200 pts. wt. charcoal powder to obtain component D; and mixing 1 pt. wt. component A, 1 pt. wt. component B, 1 pt. wt. component C and 7-13 pts. wt. component D to obtain compound fertilizer containing nitrogen, phosphorus pentoxide, potassium oxide and organic matter at 15%:15%:15%:55% and granulating.
NOVELTY - Preparation of organic-inorganic compound fertilizer includes mixing 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite to obtain component A, mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B, crushing mulberry dried roots to obtain component C, mixing 1 pt. wt. baking powder and 45-55 pts. wt. and livestock manure, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran and 1 pt. wt. yeast, fermenting for 40-45 days, adding 200 pts. wt. charcoal powder to obtain component D and mixing all components.    USE - Method for preparing organic-inorganic compound fertilizer comprises used for mulberry (claimed).    ADVANTAGE - The fertilizer is environment-friendly and increases yield of mulberry to 15-20%.    DETAILED DESCRIPTION - Preparation of organic-inorganic compound fertilizer comprises taking 1 pt. wt. carbonized wood slag powder and 6-10 pts. wt. expanded perlite, stirring at 60-65 degrees C for 10-15 minutes and cooling to obtain component A; mixing 1 pt. wt. starch and 45-55 pts. wt. clay powder to obtain component B; crushing mulberry dried roots and sieving into 100-mesh sieve to obtain component C; mixing 1 pt. wt. baking powder, 9-11 pts. wt. mulberry root powder and 45-55 pts. wt. and livestock manure, fermenting for 40-45 days, stirring after every 9 days, adding 10 pts. wt. sucrose and 100 pts. wt. water, stirring at 60 degrees C, adding 50 pts. wt. rice bran, 50 pts. wt. tea seed meal, 39 pts. wt. soybean meal and 1 pt. wt. yeast, fermenting at 65-75 degrees C for 40-45 days and adding 200 pts. wt. charcoal powder to obtain component D; and mixing 1 pt. wt. component A, 1 pt. wt. component B, 1 pt. wt. component C and 7-13 pts. wt. component D to obtain compound fertilizer containing nitrogen, phosphorus pentoxide, potassium oxide and organic matter at 20%:8%:12%:60% and granulating.
NOVELTY - Method for treating sewage, involves subjecting sewage to aeration process in fixed bed packed with carbon fiber, and suppressing generation of nitrous oxide using microorganisms integrated to the carbon fiber.    USE - The method is useful for treating sewage, and wastewater from livestock (all claimed) e.g. pigsty and cow shed.    ADVANTAGE - The method suppresses release of dinitrogen monoxide during wastewater treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage treatment unit.
NOVELTY - Producing solid fuel comprises (a) collecting municipal waste including organic waste and inorganic waste, (b) injecting the collected municipal waste into a waste disposal device, (c) removing magnetic metallic material by screening with magnetic force, (d) shredding, (e) mixing by adding additive into the shredded municipal waste, (f) drying, (g) removing non-magnetic metallic material from the dried municipal waste by screening, (h) pulverizing the dried municipal waste, (i) molding the pulverized municipal waste into unimodal solid fuel, and (j) cooling the molded solid fuel.    USE - The method is useful for producing solid fuel (claimed).    ADVANTAGE - The method removes odor of waste; improves combustibility of solid fuel; increases frictional heat generation; prevents volatile content destruction; and is cost efficient.    DETAILED DESCRIPTION - Producing solid fuel comprises (a) collecting municipal waste including organic waste and inorganic waste, (b) injecting the collected municipal waste into a waste disposal device, (c) removing magnetic metallic material from the injected municipal waste by screening with magnetic force, (d) shredding the magnetic metallic material removed municipal waste, (e) mixing by adding additive into the shredded municipal waste, (f) drying additive mixed municipal waste, (g) removing non-magnetic metallic material from the dried municipal waste by screening, (h) pulverizing the dried municipal waste, (i) molding the pulverized municipal waste into unimodal solid fuel, and (j) cooling the molded solid fuel, where the organic waste comprises food waste, sewage sludge and livestock manure and the inorganic waste comprises paper, resin, metal or glass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for producing solid fuel (Drawing includes non-English language text).
NOVELTY - A raw material generation system (1) comprises a drying unit (3) for dry-processing organic waste, and mixing unit (4) to generate the raw material whose moisture content is lower than that of organic waste (W1) by mixing the organic waste (W2) of moisture content lower than that of organic waste (W1) subjected to drying by drying unit with the organic waste (W1) which is dry-recycled. The raw material generation system uses the organic waste and generates a raw material.    USE - Raw material generation system is used for producing raw material (claimed).    ADVANTAGE - The raw material generation system enables efficient and economical production of raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for raw material production, which involves drying the organic waste (W1), and generating the raw material whose moisture content is less than that of organic waste (W1).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of raw material generating system. (Drawing includes non-English language text)    Raw material generation system (1)    Gasifier (2)    Drying unit (3)    Mixing unit (4)    Heat-source portion (5)
NOVELTY - A furaldehyde (I) or its derivative is reacted in a reaction system containing noble metal-supported solid catalyst comprising palladium, inorganic acid catalyst, and solvent, to obtain alkyl furan (II).    USE - Manufacture of alkyl furan e.g. 2,5-dimethyl furan used as biofuel (claimed).    ADVANTAGE - The method enables manufacture of alkyl furan with high yield and high selectivity under mild condition.    DETAILED DESCRIPTION - A furaldehyde of formula (I) or its derivative is reacted in a reaction system containing noble metal-supported solid catalyst comprising palladium, inorganic acid catalyst, and solvent, to obtain alkyl furan of formula (II).    R1=hydroxymethyl or aldehyde;    R2=H, methyl, or hydroxymethyl;    R1' =methyl;and    R2'=H or methyl.
NOVELTY - A weedproof material comprises a substance (I) chosen from calcium oxide, slaked lime, calcined dolomite, hydroxylation dolomite and baking dust, and a substance (II) chosen from water washing sludge of limestone, water washing sludge of dolomite, a crushed material, a crushed stone and a crushed stone.    USE - Weedproof material. Uses include but are not limited to planting zone of plant site, housing site, city area footpath besides farmland and wood land, central lane separator strip of roadway, bottom of road shoulder of roadway and track, solar panel installation zone, park and garden, parking lot, playground, elevated structure, etc.    ADVANTAGE - The weedproof material has excellent weedproof characteristics, does not spoil scene, and can be economically and easily constructed by environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for construction of weedproof material, which involves covering weedproof material to thickness of 2-30 cm.
NOVELTY - Preparation of 1-nitro-4-((4-nitrophenyl)sulfanyl)benzene (I), involves reacting 1-chloro-4-nitrobenzene (II) with carbonyl group-containing compound (III), in presence of base and in solvent.    USE - Preparation of 1-nitro-4-4-nitrophenyl-sulfanyl-benzene used for preparation of 4-4'-diamino-diphenylsulphone (claimed) useful for exhibiting antibacterial effect and treating dermatological diseases, preferably leprosy.    ADVANTAGE - The method enables environmentally-friendly and economical preparation of 1-nitro-4-4-nitrophenyl-sulfanyl-benzene with improved yield and purity, and is suitable for industrial preparation.    DETAILED DESCRIPTION - Preparation of 1-nitro-4-((4-nitrophenyl)sulfanyl)benzene of formula (I), involves reacting 1-chloro-4-nitrobenzene of formula (II) with carbonyl group-containing compound of formula (III), in presence of base and in solvent    R=1-6C alkyl or phenyl.    INDEPENDENT CLAIMS are included for the following:    (1) Dapsone as crystalline anhydrous form A, which has a melting point of 178.8?oC, and a XRPD spectrum, in which the intense peaks fall at 10.39, 11.47, 11.77, 15.48, 18.04, 19.00, 19.56, 20.29, 20.83, and 21.79\|0.2?oC in 2(~q); and    (2) preparation of 4-4'-diamino-diphenylsulphone of formula (IV), which involves using 1-nitro-4-((4-nitrophenyl)sulfanyl)benzene of formula (I) as starting material.
NOVELTY - Coal and uncrushed coconut palm seed shell are supplied to grinder and grinded, and the obtained co-ground product is directly supplied to furnace of fluidized bed boiler and burned to obtain electric power along with vapor. The particle diameter of obtained co-ground coal is such that, less than 5 %mass sieve residue passes through mesh of 5 mmx 5 mm and 30-70 %mass sieve residue passes through mesh of 1.78 mmx 1.78 mm.    USE - Electrical power generation method (claimed).    ADVANTAGE - The method enables stable and effective generation of electric power by futilely discarding coconut palm seed shells in large quantities, with reduced energy consumption, and reduced carbon dioxide, nitrogen oxide and sulfur oxide generation.
NOVELTY - A recombinant eukaryotic host cell comprising exogenous nucleic acid encoding a THIC enzyme, is new. The recombinant eukaryotic host cell expresses nucleic acid and is capable of growing in a thiamine-free culture medium.    USE - The recombinant eukaryotic host cell is useful for producing oil (all claimed), transportation fuels chosen from renewable diesel, biodiesel, and renewable jet fuel, and oleochemicals chosen from functional fluids, surfactants, soaps and lubricants.    ADVANTAGE - The recombinant eukaryotic host cell enables to produce oil cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for cultivating recombinant eukaryotic host cell comprising an exogenous nucleic acid encoding a THIC enzyme, involves inoculating the recombinant eukaryotic host cell into a culture medium, where the culture medium is essentially free of thiamine, cultivating the host cell to a desired cell density, and harvesting the host cell from the culture medium, where the recombinant eukaryotic host cell expresses the nucleic acid and is capable of growing in a thiamine-free culture medium; and    (2) method for producing an oil involves inoculating a recombinant eukaryotic host cell into a culture medium, where the culture medium is essentially free of thiamine, the recombinant eukaryotic host cell comprises an exogenous nucleic acid encoding a THIC enzyme, the recombinant eukaryotic host cell expresses the nucleic acid and is capable of growing in a thiamine-free culture medium, cultivating the host cell to a desired cell density, harvesting the host cell from the culture medium, and extracting the oil from the host cell.
NOVELTY - Substituted tetrahydropyridine derivatives (I) are new.    USE - (I) are useful for treating bacterial infection in a subject such as animal including human (all claimed), where the bacteria include methicillin-resistant Staphylococcus spp., vancomycin-resistant Enterococcus spp. and penicillin-resistant Streptococcus pneumoniae.    ADVANTAGE - (I) have improved antimicrobial activity, metabolic stability and pharmacokinetic profile, good in vivo efficacy and less side effects and toxicity, and are easy to absorb and show good oral bioavailability and plasma protein binding effect.    DETAILED DESCRIPTION - Substituted tetrahydropyridine derivatives of formula (I) and their salts or stereoisomers are new.    X = N or CH;    Y1 = NR1 or CHR1;    Z = C(R2)(R3); either    R1-R3 = H or alkyl; or    R2+C+R3 = optionally substituted 3-7 membered ring containing 0-3 heteroatoms comprising N, O, NH or CO, where the optional substituent is R4; or    R1+C+R2, R1+N+R2 = 5-membered fused ring;    R4 = alkyl, -COOR5, -COR5 -CON(R5)2, SO2R5, -CO(CH2)2C(O)OR5, -COCH2N(R5)R5 or cycloalkyl;    R5 = H, alkyl, cycloalkyl or heterocyclyl; and    n = 0 or 1.    An INDEPENDENT CLAIM is included for a process for the preparation of (I).
NOVELTY - The method involves joining an anode and a cathode to both sides of an electrolytic membrane in a membrane electrode assembly. A sealing portion (80) is arranged at an opposite end surface of an outer peripheral portion between adjacent fuel cells. The cells are laminated to form a fuel cell module (40). The cell module is press-processed in a lamination direction of the cell, so as to form a seal site by the sealing portion. The thickness of the cell module in the lamination direction is controlled by controlling the load that presses the cell module.    USE - Method for manufacturing fuel cell.    ADVANTAGE - Since the fuel cell module is press-processed in the lamination direction of the fuel cell to form the seal site by the sealing portion, the difference of the thickness of the center portion and the outer peripheral portion is prevented. Hence the seal site is formed reliably. Since the thickness of the cell module in the lamination direction is controlled by controlling the load that presses the cell module, the stress concentration on the boundary between a center portion and an outer peripheral portion is prevented. Hence the damage of the laminated portion is prevented. Thus the thickness management of the laminated portion by the press load is enabled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for manufacturing the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a formation of a seal site by the press of the fuel cell module.    Fuel cell module (40)    Sealing portion (80)    Lamination direction thickness at time of center portion swelling at time of press load addition (H1)    Lamination direction thickness of peripheral part at time of press load addition (H2)
NOVELTY - Method of preparing onion manure, involves mixing onion by-product, livestock excretion and microbial composition, drying the mixture, pulverizing, transferring to fermentation culture, then adding onion powder, jade powder, rice bran, protein source, oyster shell, distiller's grain, soybean cake and molasses, adding the bean-curd residue to the above mixture, then fermenting the mixture and drying the fermented product, where the microbial composition includes Lactobacillus casei and L.acidophilus.    USE - The method is useful for preparing onion manure (claimed).    DETAILED DESCRIPTION - Method of preparing onion manure, involves mixing 40-60 wt.% onion by-product, 10-50 pts. wt. livestock excretion and 1-10 pts. wt. microbial composition, drying the mixture, pulverizing the mixture to 80-150 meshes sieve size, transferring to fermentation culture, then adding 20-30 wt.% onion powder, 20-30 wt.% jade powder, 40-50 wt.% rice bran, 2-5 wt.% protein source, 1-5 wt.% oyster shell, 1-5 wt.% distiller's grain, 2-5 wt.% soybean cake and 0.1-1 wt.% molasses, adding the bean curd residue to the above mixture, then fermenting the mixture at room temperature for 24-48 hours and drying the fermented product at 30-40 degrees C for 36-48 hours until the water content is 35-40%, where the microbial composition comprises Lactobacillus casei, L.acidophilus, L.plantarum, L.brevis, Streptococcus faecalis, Bacillus subtilis and B.putrificus. An INDEPENDENT CLAIM is included for onion manure prepared by the above method.
NOVELTY - Microbial agent comprises cultured material of Rhodococcus pyridinivorans EDB2 (KACC91762P), which is identified from coastal mud flat.    USE - The microbial agent is useful for purifying oxalic acid organic wastewater (claimed).    ADVANTAGE - The microbial agent has salinity tolerance and digestive effect of organic material (claimed), and is environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for (I) purifying oxalic acid organic wastewater by decomposing discharged organic matter, comprising spraying the microbial agent in a wastewater reaction tank which contains wastewater; and (II) producing microbial agent, comprising (a) culturing the Rhodococcus pyridinivorans in culture medium by inoculating at 25-42 degrees C, and pH of 5-10, (b) adding diluting agent for color adjusting in liquid preparation, diluting agent for improving storability and/or diluting agent for activating enzyme in the obtained culture, (c) aseptically drying the obtained resultant, (d) aseptically pulverizing the dried resultant, and (e) adding diluting agent for microbial fermentation or diluting agent for improving storability into the pulverized resultant.
NOVELTY - The method involves cooling water from a proton-exchange-membran-technology (PEM) electrolyzer (6) in a cooling device (10) in a water circuit, and then supplying cooling water to an ion exchanger (4) for processing the water. The water is supplied after the processing in ion exchanger to PEM electrolyzer. The heat is extracted from the water before supplied to the cooling device and a portion of extracted heat is fed back to the water after processing in the ion exchanger and before entry into the PEM electrolyzer.    USE - Method for operating electrolysis device (claimed) for generating hydrogen.    ADVANTAGE - The operation method is improved with a smaller amount of distilled water. The intensive exchange of heat between the two water streams is achieved. The efficiency of electrolysis process is increased by the heating of the outgoing water from the ion exchanger prior to entering the PEM electrolyser, without overload of ion-exchange of heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis device.    Electrolysis device (2)    Ion exchanger (4)    PEM electrolyzer (6)    Heat exchanger (8)    Cooling device (10)
NOVELTY - 9,9-bis((4-hydroxyethoxy)phenyl)fluorene is synthesized by reacting 9,9-bis(4-hydroxyphenyl)fluorene with 2-halogenated ethanol in solvent and alkali.    USE - Synthesis of 9,9-bis((4-hydroxyethoxy)phenyl)fluorene (claimed).    ADVANTAGE - Synthesis of 9,9-bis((4-hydroxyethoxy)phenyl)fluorene is simple and environment-friendly, has high reaction yield, and uses cheap and easy to obtain raw materials.
NOVELTY - A saxagliptin intermediate (I) or (II) or its salt is new.    USE - Saxagliptin intermediate used for preparation of saxagliptin (claimed).    ADVANTAGE - The compound (I) has easy and simple preparation which is environment-friendly and has mild reaction condition.    DETAILED DESCRIPTION - A saxagliptin intermediate of formula (I) or (II) or its salt is new.    R1=methyl, ethyl, n-propyl, isopropyl, n-butyl or isobutyl; and    R2=H, 4-methoxyphenyl, 4-halophenyl, 2-methoxyphenyl or 2-halogenated phenyl.
NOVELTY - Synthesizing intermediate of 11 alpha-hydroxylation involves culturing Aspergillus ochraceus or other fungal strain that produces ochratoxin in a seed culture medium.    USE - Method for synthesizing intermediate of 11 alpha-hydroxylation (claimed).    ADVANTAGE - The method enables to synthesize intermediate of 11 alpha-hydroxylation that is steroidal in nature, eco-friendly, and has high conversion rate in a cost-effective manner.    DETAILED DESCRIPTION - Synthesizing intermediate of 11 alpha-hydroxylation involves culturing Aspergillus ochraceus or other fungal strain that produces ochratoxin in a seed culture medium. Substrate emulsion is prepared by dissolving 17 alpha-hydroxyprogesterone, 4-androstenone or 16,17alpha-epoxyprogesterone with a surfactant. Fermentation is performed, where the cultured fungal growth of Aspergillus ochraceus is mixed with Rhizopus, and incubated for certain period of time, where the enzyme secreted by Rhizopus degrade ochratoxin present in the test sample. The prepared substrate emulsion is then mixed with fermentation broth comprising fungal growth to extract intermediate of 11 alpha-hydroxylation from the fermentation mixture.
NOVELTY - This utility new type claims a one kitchen garbage aerobic compost system of online monitoring system, a kitchen waste aerobic compost system include fittings contactor, contactor, a feeding machine contactor, the contactor to rotate, an exhaust fan contactor, wherein the online monitoring system include temperature and humidity probe, a temperature and humidity sensor, the communication module group, serial server, an industrial control machine and an I/O module, a temperature and humidity probe monitoring mounting of the kitchen waste aerobic composting system cabin body inner of through temperature and humidity sensor collect, then transmitting through the communication module group to a serial, rear serial server by a data conversion transmission to the industrial control machine, machine contactor, contactor, a feeding machine contactor, the contactor to rotate, an exhaust fan contactor are connecting to input end of I/O module, output end of said I/O module a connecting to the industrial control machine through the communication module group, a serial. This utility new type a increase working efficiency of kitchen waste aerobic compost system.
NOVELTY - A phosphate slag flotation modifier utilization method involves selecting slag as raw material, which is generated by industrial phosphoric acid. The raw material is pumped directly to the tank with phosphate flotation modifiers followed by performing anti-flotation process to obtain phosphate flotation modifier index during dehydrate wet process of phosphoric acid production.    USE - Method for utilization of phosphate slag flotation modifier.    ADVANTAGE - The method enables utilization of modifier with strong applicability in an environment-friendly and simple manner.
NOVELTY - The apparatus (100) has a modifier (20) that generates a hydrogen-containing-gas using raw material which passed desulfurizer (12). First temperature detector (16) detects the temperature of desulphurization catalyst (14) of a predetermined portion. Second temperature detector (18) detects the temperature of the desulphurization catalyst of the site further than predetermined portion from first heat source (10). A controller (30) controls the heating of desulphurization catalyst by first heat source based on detection result of temperature detectors respectively.    USE - Hydrogen generating apparatus for use in fuel cell system (claimed).    ADVANTAGE - The temperature of desulphurization catalyst can be maintained easily at appropriate range, using hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Heat source (10)    Desulfurizer (12)    Desulphurization catalyst (14)    Temperature detectors (16,18)    Modifier (20)    Controller (30)    Hydrogen generating apparatus (100)
NOVELTY - A carfilzomib intermediate comprising resin solid phase carrier coupled with tetrapeptide intermediate having tetrapeptide midbody, is new.    USE - The carfilzomib intermediate is useful for preparing carfilzomib for treating multiple myeloma.    ADVANTAGE - The preparation method provides high yield, small pollution, and simple and controllable reaction, and has strong operability.    DETAILED DESCRIPTION - A carfilzomib intermediate comprising resin solid phase carrier coupled with tetrapeptide intermediate having tetrapeptide midbody of formula (I), is new. INDEPENDENT CLAIMS are:    (1) a method for preparing carfilzomib intermediate; and    (2) a method for preparing tetrapeptide intermediate for carfilzomib intermediate, comprising using carfilzomib intermediates in the presence of cleaving agent, e.g. trifluoroacetic acid (TFA) or trifluoroethanol (TFE) at 4-15 5 ml/g.
NOVELTY - The gas-liquid separator has gas discharge port (33) that discharges the gas after the separation. A liquid outlet (32) discharges the liquid after the separation. A partition plate (35) partitions off the interior space (31d) into an upper space and lower space and consists of a mesh shaped element (35a2) which transmits the liquid. A container main portion (31) opens the mixing liquid flow entrance (34) and the gas discharge port, and opens the liquid outlet to side of lower space (31e).    USE - Gas-liquid separator of hydrogen and oxygen generation apparatus (claimed).    ADVANTAGE - The improvement of the gas-liquid separation performance of a gas-liquid separator is achieved effectively, and hydrogen and an oxygen generation apparatus with easy compactizing a size are provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen and oxygen generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross sectional view of the gas liquid separator.    Container main portion (31)    Lower space (31e)    Interior space (31d)    Liquid outlet (32)    Gas discharge port (33)    Liquid flow entrance (34)    Partition plate (35)    Mesh-shaped element (35a2)
NOVELTY - The cell unit has interconnector (6) for connecting cathode (3), solid electrolyte layer (4), and anode (5) with electrolysis element (A) which generates the gas containing hydrogen and is laminated successively and contains water vapor. A cover arranged at other end of cell, has space for circulating fluid between flow-holes. The pressure loss in one end side of width direction of electrolysis cell and other end side in space is 5 times or more of the pressure loss in inlet port of flow-hole to which water vapor is supplied.    USE - Electrolysis-cell unit for electrolysis cell stack apparatus of electrolyzer.    ADVANTAGE - The size of the electrolysis-cell unit is reduced and the structure is simplified. The efficient electrolysis reaction is carried out.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an electrolysis cell stack apparatus; and    (2) an electrolyzer.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view and perspective view of the electrolysis cell.    Cathode (3)    Solid electrolyte layer (4)    Anode (5)    Interconnector (6)    Electrolysis element (A)
NOVELTY - The method involves welding a plate-shaped workpiece along a closed-circuit-shaped welding area so that the path in which weld scar in circumference of through-hole is closed. Laser (L1) is irradiated and welded to a welding area along an opening portion (141) in jig element (131). Second opening portion of second jig element exposed in welding area other than welding area of opening portion (141) is replaced with jig element (131), such that fixing jig element (133) is mounted. The laser is irradiated and welded to welding area along second opening portion in second jig element.    USE - Manufacturing method of fuel cell associated component.    ADVANTAGE - The attachment or detachment of jig elements with respect to fixing jig element is easily performed by utilizing clamp structure. The number of the jig element or fixing element in welding tool apparatus is decreased. The laser welding of closed circuit shape in fuel cell associated component is performed reliably.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell associated component; and    (2) a welding tool apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of welding system.    Jig element (131)    Fixing jig element (133)    Clamp structure (135)    Opening portion (141)    Laser (L1)
NOVELTY - The apparatus (10) has electrolysis chambers (16,16a,16b) which are configured to accommodate the electrolyzed water solution which contacts hydrogen gas generation portion and oxygen gas production portion. The oxygen gas production portion is formed in back surface of conductive substrate in which semiconductor thin film of second element in other edge portion of element laminated portion (12). The ionic permeability and gas impermeability diaphragm (20) is provided between electrolysis chambers. The hydrogen generation catalyst is provided as platinum.    USE - Apparatus for manufacturing gas such as hydrogen and oxygen for solar cell.    ADVANTAGE - The high gas production efficiency of the gas-manufacturing apparatus is maintained. The gas of hydrogen and oxygen stably is manufactured stably as highly purified gas separated completely. The conversion efficiency from the solar energy to hydrogen is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gas-making apparatus.    Apparatus for manufacturing gas (10)    Element laminated portion (12)    Electrolysis chambers (16,16a,16b)    Ionic permeability and gas impermeability diaphragm (20)    Buffer layer (30)
NOVELTY - An oxidizing agent comprises acid in an amount below equivalent with respect to 2-6C carboxylate ester compound, hydrogen peroxide solution, and substrate.    USE - Oxidizing agent is used for manufacture of 1,4-benzoquinone compound used as intermediate for preparing pharmaceutical bioactive substance, agrochemical, metabolism and mental symptoms improving agent, thromboxane A2 synthase inhibitor, thromboxane A2 receptor antagonist, 5-lipoxygenase inhibitor, oxygen free radical scavenger, antiasthmatic agent and hepatic disorder treatment agent.    ADVANTAGE - The oxidizing agent is environmentally-friendly and can be economically prepared. The 1,4-benzoquinone compound is efficiently manufactured using the oxidizing agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of 1,4-benzoquinone compound of formula (I), which involves reacting methoxybenzene compound of formula (II) with oxidizing agent.    R1-R4=H, 1-6C alkyl, 1-6C alkoxy or phenyl.
NOVELTY - Production of gas hydrate involves mixing methane with carbon dioxide-air mixture gas, decomposing methane in the mixture, and maintaining the concentration of methane and mixture gas to less than the critical methane concentration which is a point within the chemical potential of methane in gas phase and solid phase.    USE - Production of gas hydrate used for production of natural gas.
NOVELTY - The composting processor has feedstocks which are arranged from bottom portion to top portion with perforated partitions so as to perform decomposition process with high speed and certainties. The feedstock in advanced-stage decomposition process acts as effective filter and barrier to contain undesirable emittance.    USE - Composting processor e.g. upcycling accelerated composting processor (UACP) used in kitchen and lounge for urban farming and indoor farming. Can also be used in food factory.    ADVANTAGE - The feedstock in advanced-stage decomposition process acts as effective filter and barrier to contain undesirable emittance, so that the undesirable emittance contained in the composting processor is reduced. The composting process is performed easily and quickly. The structure of the composting processor is simplified easily. The appearance of the processor is increased. The hostile wastes from the living space are prevented. The transportation and disposal cost of the processor is reduced. The plants are grown efficiently in the tray.
NOVELTY - An improved preparation of 3,5-diamino-6-(2,3-dichlorophenyl)-1,2,4-triazine (I) involves reacting 2,3-dichlorobenzoyl chloride (II) with metal cyanide in o-dichlorobenzene and further isolating with a solvent to produce pure 2,3-dichlorobenzoyl cyanide (III); reacting the cyanide (III) with aminoguanidine bicarbonate to produce intermediate 2-(2,3-dichlorophenyl)-2-guanidinyliminoacetonitrile (IV); and cyclizing the nitrile (IV) in presence of alcohol.    USE - For preparation of 3,5-diamino-6-(2,3-dichlorophenyl)-1,2,4-triazine (claimed) useful for treating CNS disorders.    ADVANTAGE - The process is simple, eco-friendly, inexpensive, produces pure lamotrigine in better yields with a lower amount of impurities, robust and is well suited on an industrial scale. The process produces lamotrigine of high grade purity and satisfactory impurity profile. The process produces lamotrigine with improved quality and yield, consistently without requirement of further purification. The process is cost effective and scalable process.    DETAILED DESCRIPTION - An improved preparation of 3,5-diamino-6-(2,3-dichlorophenyl)-1,2,4-triazine of formula (I) involves reacting 2,3-dichlorobenzoyl chloride of formula (II) with metal cyanide in o-dichlorobenzene and further isolating with a solvent to produce pure 2,3-dichlorobenzoyl cyanide of formula (III); reacting the cyanide (III) with aminoguanidine bicarbonate to produce intermediate 2-(2,3-dichlorophenyl)-2-guanidinyliminoacetonitrile of formula (IV); and cyclizing the nitrile (IV) in presence of alcohol.
NOVELTY - A fluroxypyr salt is prepared by mixing fluroxypyr, inorganic alkali or organic alkali and solvent, fully stirring, reacting, cooling, crystallizing and drying.    USE - Method for preparing fluroxypyr salt (claimed) used for farmland weeding.    ADVANTAGE - The prepared fluroxypyr salt is environment-friendly, avoids use of harmful solvent, reduces the shift and harm of traditional Chinese medicine, and has faster weeding speed.
NOVELTY - This utility new type relates to a greenhouse a spraying fertilizing one composite work machine, using a technology solution is as follows: comprise machine frame, minimally invasive mechanism, spray device, airflow auxiliary mechanism and walking mechanism. A machine frame for a fixed, spray device and other support mechanism; a minimally invasive mechanism for a minimally invasive tobacco young leaves, the spray device for spray vaccine inoculating liquid, spray pesticide or foliar fertilizer, said gas auxiliary mechanism of the blade used for blowing a minimally invasive mechanism, used for turning or auxiliary blade; the walking mechanism for driving machinery bracket tobacco seedling breeding area. This utility new type tobacco a machinery, aiming at the problem of the existing plant protection machinery low efficiency, using a of water with a rotate for tobacco young leaves a minimally invasive, and the auxiliary air flow spray a liquid vaccine inoculating process, increase the seedling rate a, a and a precise medicine or precise spraying foliage fertilizer and so on a multi-composite function, wherein the machine for a tobacco and a spraying fertilizer of different planting, a comprehensive management of greenhouse seedling.
NOVELTY - First pressurizing this utility new type claims a one for coal bed gas enriching process of system, the system comprise diethyl ether solvent for a for a coal bed gas in absorbing process of absorbing tower for absorbing rear for a solvent-rich liquid a desorption of the flash of a separate, and removing flash tower in inner desorption separate methane gas from low temperature separate tank of diethyl ether, an absorbing tower, a tower, a low temperature separate tank in turn, a absorption tower for the ethyl ether solvent, of a pressurized gas, a cooling component and a cooling component with a first a and low temperature separate tank and the tower set for a rich gas process, cooling a second pressurizing component and second cooling module. The supply of used for coal bed gas for a gathering of system, convenient operation, less device, heat the integrated rear can fully utilize a self-heat, a most cold common engineering loss is less.
NOVELTY - This utility new type claims a acid-base one electric beam irradiation intelligent waste gas processing system, comprising a waste gas collecting device comprise, alkali gas collecting device, main reactor, an electrostatic dust collector, first gas pre-heating device and second gas pre-heating device, inner main reactor set with a beam and a main reaction cavity, a beam generator of electric beam irradiation end extends into the inner main reaction cavity, main reaction cavity has a waste gas inlet, alkali gas air inlet and air outlet, the air inlet of first gas pre-heating device through pipeline and the waste acid gas collecting device is connected, and the air outlet of first gas pre-heating device through pipeline connecting the waste acid gas of main reaction cavity upper air inlet, the air inlet of second gas pre-heating device through pipeline and the waste gas collecting device is connected. This utility new type using a beam irradiation for a valid gas desulfuration, denitrification, it can avoid produce waste liquid, reduces the second pollution, and a nitrogenous fertilizer, it changes waste into valuable.
NOVELTY - Preparing organic green fertilizer involves (a) taking chicken manure, pig manure, rice chaff, and peanut shell powder as raw materials, (b) stirring raw materials, (c) naturally stacking stirred raw materials, and carrying out composting of stacked materials by adding bacteria to stack, (d) turning compost, piling turned materials after completion of first turning process, and turning materials for second time, and (e) packing compost mixture after internal temperature of stacked materials falls to room temperature.    USE - The method is useful for preparing organic green fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly. The fertilizer exhibits good microbial activity, and decomposes compost plants rapidly and thoroughly, and thus kills weeds.    DETAILED DESCRIPTION - Preparing organic green fertilizer involves (a) taking 70 wt.% chicken manure, 10 wt.% pig manure, 5 wt.% rice chaff, and 15 wt.% peanut shell powder as raw materials, (b) stirring the raw materials, (c) naturally stacking the stirred raw materials, and carrying out composting of the stacked materials by adding bacteria to the stack, (d) turning the compost using compost turner until the internal temperature of stacked materials reaches 44-46 degrees C, piling the turned materials after completion of first turning process, and turning the materials for the second time until the internal temperature of stacked materials reaches 59-61 degrees C, and (e) packing the compost mixture after the internal temperature of stacked materials falls to room temperature.
NOVELTY - Substrate composition comprises 50-60 %mass Pleurotus eryngii, 10-15 %mass dairy manure, 20-25 %mass corncob, 3 %mass bioenzyme, 1.5 %mass gypsum powder, 1.5 %mass calcium carbonate powder, and 4 %mass wollastonite powder.    USE - The substrate composition is useful for cultivating Agaricus bisporus (claimed).    ADVANTAGE - The composition improves yield, appearance and quality of A.bisporus, and uses cost-effective raw materials and thus reduces cost of production by 50-55%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the substrate composition, which involves (a) drying and crushing P.eryngii and dairy manure into powder, (b) crushing corncob into sheet-shaped or coarse particles, (c) uniformly mixing bioenzyme, gypsum powder, the above-mentioned powder of step (a) and product of step (b), (d) regulating water content of mixture at 75%, (e) performing fermentation of the mixture 65 degrees C, (f) adding calcium carbonate powder to fermented product, stirring added material, and regulating pH of stirred product at 8.5-9 and water content of stirred product at 65-68%, (g) again fermenting stirred product at 72 degrees C, and collected fermented product to obtain product.
NOVELTY - Pyrolysis and gasification of biomass comprises (i) performing pyrolysis of biomass raw material of moisture content 10-20% under atmospheric pressure at 550-650 degrees C to obtain gas-phase product and solid-phase product; (ii) separating solid-phase product from the gas-phase product, removing from the reaction system, and combusting through combustion heat used for biomass gasification; and (iii) cracking gas-phase product at 800-950, removing tar and reducing hydrocarbon content including methane to improve hydrogen content and yield in the gas product; and (iv) igniting the gas.    USE - The method is useful for pyrolysis and gasification of biomass (claimed).    ADVANTAGE - The method utilizes wide range of raw material, produces small amount of biomass ash, reduces energy consumption and is economical.
NOVELTY - An oil soluble additive comprises 35-45 wt.% methanol or denatured ethanol, 50-65 wt.% alkane, olefin and aromatic hydrocarbon mixture, 1-2.5 wt.% salt, 1-5 wt.% isopropyl alcohol or n-butyl alcohol, and 0.2-1 wt.% nitric acid.    USE - Oil soluble additive used for alcohol ether gasoline (claimed).    ADVANTAGE - The oil soluble additive is cheap, has low consumption, and solves problem such as high gasoline consumption, not enough power, acid-base corrosion and rubber swelling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an alcohol ether gasoline comprising 10-65 wt.% oil-soluble additive and 35-60 wt.% gasoline.
NOVELTY - Continuous supercritical catalysis of biodiesel comprises preheating oil; heating tubular reactor; filling solid catalyst into column packing machine using tubular reactor, and sealing tubular reactor's inlet and outlet with sieve plate; filtering oil impurities, pumping oil and methanol as acyl acceptor into mixer, mixing, and feeding into tubular reactor to carry out supercritical reaction; and separating methanol, collecting coarse biological diesel oil middle layer, flash evaporating to evaporate residual methanol and obtain biodiesel and crude glycerin, and refining.    USE - Method for continuous supercritical catalysis of biodiesel (claimed).    ADVANTAGE - The method is simple, achieves conversion rate of up to 90-100%, does not produce any impurities, and it has improved supercritical reaction in harsh conditions.    DETAILED DESCRIPTION - Continuous supercritical catalysis of biodiesel comprises:    (A) preheating oil to 35-65 degrees C;    (B) heating tubular reactor to 260-330 degrees C through furnace, and adjusting pressure control valve while maintaining internal pressure of operating system to10-19 MPa;    (C) filling solid catalyst into column packing machine using tubular reactor, and sealing tubular reactor's inlet and outlet with sieve plate;    (D) filtering oil impurities, pumping oil and methanol as acyl acceptor at molar ratio of 1:35-1:70 into mixer, mixing, and feeding into tubular reactor to carry out supercritical reaction; and    (E) feeding into gas-liquid separator, separating methanol, cooling to generate heat, returning back methanol into reaction system, and using generated heat to preheat oil; collecting coarse biological diesel oil middle layer, flash evaporating to evaporate residual methanol and obtain biodiesel and crude glycerin, and subjecting to subsequent processing and refining.
NOVELTY - The biomass melting furnace comprises a pyrolysis reactor main body and a biomass gasification chamber. The pyrolysis reactor main body comprises an outer furnace body and a crucible. The biomass gasification chamber comprises a biomass pyrolysis chamber and a combustion chamber. The combustion chamber is connected to the crucible through a pre-heating tube. An upper end of the pyrolysis reactor main body is connected with a feeding system. The feeding system comprises a spiral conveyor and a gas-solid separator.    USE - Biomass melting furnace.    ADVANTAGE - The biomass melting furnace exhibits improved combustion stability and rate.    DETAILED DESCRIPTION - The biomass melting furnace comprises a pyrolysis reactor main body and a biomass gasification chamber. The pyrolysis reactor main body comprises an outer furnace body and a crucible. The biomass gasification chamber comprises a biomass pyrolysis chamber and a combustion chamber. The combustion chamber is connected to the crucible through a pre-heating tube. An upper end of the pyrolysis reactor main body is connected with a feeding system. The feeding system comprises a spiral conveyor and a gas-solid separator. The gas-solid separator is connected to an output end of the spiral conveying tube through a screw. An input end of the spiral conveying tube is connected with a material level height regulating device and a spiral propelling regulator. The material level height regulating device is provided with a material level radar controller. The spiral propelling regulator is provided with a variable frequency regulator. A lower end of the pyrolysis reactor body is connected to fire grates. The grates are provided with temperature perforation plates. The fire grates are connected with an air supply device comprising a pipeline and a multiple air supply regulator.
NOVELTY - This utility new type claims a one active carbon production tail pneuma recovery using system, include biomass gasification furnace, set with combustible gas in a pipeline under continuous carbonizing furnace cavity, a biomass gasification furnace set with an air outlet pipeline, a gas outlet pipeline connected cyclone dust collector, a cyclone dust collector set with pneuma pipeline, at the same time connected combustible gas recovery pipeline, pipeline the biomass gasification furnace produce of combustion gas and a combustible gas pipeline a of a combustible gas to the spray purifier, gas exit of said spray purifier upper end a flue gas purifier, a gas purifier rear purification of the combustible gas via a fan conveying to burner, said burner and continuous carbonizing furnace of carbonizing pipeline connect. This utility new type rear of a continuous type carbonizing furnace inner cavity for a produce a waste pneuma process, to reach a reciprocating circulation heating carbonizing of effect and has a wide market popularization value.
NOVELTY - This new type utility claims one using a micro-organism electrolytic cell technology in repairing underground water of device, cathode room, anode room and cathode room comprise a seal set in the ground water combined polluted water of the anode room and seal are provided with a small hole, inner anode room and cathode room set anode electrode and a cathode electrode, an anode electrode and a cathode electrode is connected with a high potential end of voltage stabilizing power supply and a low potential end, the surface of the anode electrode to a power generating microorganism. This utility new type can obtain hydrogen can be removed at the same time in a reducing organic pollutant of sewage. In addition, it also can remove some low reduction potential of Pb2 +, Ni2 +, chlorinated hydrocarbons and quadrivalent aranium and so on.
NOVELTY - This utility new type relates to one with a pre-aeration of a sewage regulating tank, belonging to sewage treatment device technology field. Comprise straight gallery channel and bending end channel is composed of track type regulating tank, set with aeration in the part thereof channel, the aeration connecting with air supply pipe, air supply pipe connecting with air blower, air blower is air source of air supply pipe, the gallery channel until the channel connect end set with several a propeller, a propeller with a set. This utility new type is applied to the sewage processing process in to ensure the valid mix of sewage, reduces the fluctuation of sewage water, the pre-aeration in the sewage transmission process, reduces the pollutant content and sewage.
NOVELTY - Inner two level power circulation a for removing nitrogen and phosphorus in a sludge reactor, include reactor main body, set with multiple reactor main body inner cavity of the vertical clapboard, an inclined bottom plate and a guide plate, a reactor main body bottom to top is divided into return cloth water unit, inner circulation reaction unit, discharging unit, a multifunctional three phase separate area, the water and sludge recovery unit, refluxing and distributing water unit comprise return area, the inner circulation reaction unit by vertical clapboard from left to right in turn is divided into aerobic area one, one flow area, an anaerobic area, reducing a flow area, second aerobic area, second area a six compartment, discharging unit in turn up to down set with residual mud sludge and sludge-rich sludge multi-functional three phase separate area comprise a variable angle fender, the overflow weir, the water and sludge recovery unit include the water groove and a water outlet. This utility new type of beneficial effects as follows: using two level aeration pushing inner circulation, mass transfer and mix preferably property, a synchronous denitrification and dephosphorization inner in the same reactor.
NOVELTY - This utility new type relates to one a sewage treatment device, specifically to a one micro-aeration filling biological film sewage processing device, belonging to the sewage processing technology field. Include the air compressor, an air storage tank, a water tank and micro-aeration biological membrane filling material, an air compressor through gas tube connecting tank, inner water tank set with a multi-micro-aeration biological membrane filling material. Micro-aeration biological membrane filling material comprise multi-parallel to each other of a hollow fiber membrane, a hollow fiber membrane of multi-air inlet end are a gas inlet end head, a multi-hollow fiber film of air outlet end common connecting outlet end sealing head. This utility new type for filling a non-foaming air supply does not produce sludge does not need mounting air blower and sludge processing device, valid reduces the cost of sewage treatment, reduces the working noise, saves the energy, filling biological film has great specific surface area, which can reduce the volume of valid water tank.
NOVELTY - This utility new type claims a precipitate one glass steel biomass pool purification, include front, rear two end is a cylindrical horizontal glass steel tank body, water inlet tube and water outlet tube of a spherical end enclosure and the front, rear two end is a spherical end enclosure part connected, tank body by a front sealing head clapboard, inner clapboard inner post and rear sealing head clapboard is in turn divided into front seal head chamber, anaerobic fermentation room, filling a room, a room and rear is rear sealing head chamber, and flowing through the water hole and vent hole a marsh gas tank body and sewage of this utility new type bridge belongs to the domestic sewage treatment, sewage for sedimentation and fermentation process purification treatment and produce marsh gas and inorganic fertilizer, use without leakage pollution and purification treatment of high integrity is good, and the cost is low, the use life is long, at the same time it has convenient mounting and small floor space and so on, and it has wide of agricultural popularization value.
NOVELTY - This utility new type relates to a waste of livestock and poultry one rapid environment protection and treatment machine, set in part with a U-shaped fermentation jar, U-shaped fermentation jar with a main shaft set with inner the shell, right end of main motor, main shaft is hollow, the left end of the main shaft through bearing and pipeline connecting with air blower, a main shaft a uniform interval of fixed with several radial connecting rod, a radial connecting pole is welded with a cutting knife, a radial end of pole is welded with stamp, radial connecting rod is hollow, the two side upper radial connecting pole of cutting knife is set with discharge hole, a U-shaped fermentation jar with the stamping knife corresponding to the inner side of the bottom is welded with a stamp card groove cutter, a U-shaped fermentation jar bottom outer side set with a heating tube, the heating tube is equipped with inner, U-shaped fermentation jar of a side wall mounting with sensor, a U-shaped fermentation jar of rear end set with a discharging port, a discharging port is set with a belt conveyor, with an electric control box set with a front end side wall of the shell, set with a rail on the upper end of shell body, a rail set with a with an upper cover.
NOVELTY - This utility new type claims a one box type sludge composting device include fermentation box body, a fermenting box of one side set with double pull door, fermenting in a horizontal box body set used for the fermentation box body is divided into the upper layer, a lower layer, a clapboard ventilation structure, the upper top of a waste gas treatment device, a lower air blower, one end said upper inner set with a silk layer, a silk connecting a controller, and the other end of a solar energy controller. This utility new type structure design is reasonable, through a silk heating inner of the fermentation box, solves the problem that the sludge composting temperature, stack temperature, compost period is too long is not a problem.
NOVELTY - This utility new type claims a biological straw a one of a fertilizer device, comprise: powder crush machine, a stirrer, an electric transmission belt, a fermentation tank, a device, temperature sensor, monitoring computer,, and packing machine, the powder crush machine set with most front end of stirrer set at the back of the powder crush machine, the electric conveying belt set at the back of a device of stirrer, the fermentation tank set at the back of the electric, the set in the inner centre of the fermentation tank, the temperature sensor set in a fermentation tank upper end, the monitoring computer set in the temperature sensor, and the drying room set at the back of fermentation tank, the air in the drying chamber set with one side wall. This utility new type a process machine, intelligent control, time-saving force, operation specification is accurate, production period is short, the production efficiency is high, and it is easy to popularize.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically to a one organic fertilizer production with fermentation. rotten accelerator for organic materials. Include with feed inlet and discharge hole of expansion cylinder, a feeding port and a discharging port with a feeding door and mounting, by driving mechanism and a push toothed ring rotate, in the inner cavity of a, from feeding port to discharging port set with a stagnation zone in turn and pushing area, stagnation zone of inner wall set with multi up until a reading plate, uniform distribute a multi-inclined paper upper pushing plate inner wall of area, mounting with a spraying tube fixed on the upper inner wall of expansion cylinder, a cylinder wall of a set with pneuma hole, a pneuma in mounting hole and filter screen door. The device structure is simple, a continuous production, convenient operation, which is good for a large scale continuous production is convenient to realize normalizing operation, the product quality stable.
NOVELTY - This utility new type claims a combined multi-joint one fast biomass carbonization device, include baking intervention treatment system, continuous carbonizing system, a tail pneuma purification system, a tail pneuma combustion system and electric power and the control system and 5 part. Agriculture and forestry waste biomass oven intervention through a pre-heating and drying treatment, and then entering into continuous carbonization system, conversion is biological carbon lower in the sub-high temperature anoxic condition, with inserting a carbonizing room bottom plate and a carbon discharging auger. Carbonization process produce a combustion pneuma of pneuma purification system by the tail pneuma liquid separate and a solid separate, and finally entering into tail pneuma. pilot combustion. Produce a heat energy for baking intervention of a system or a steam electric generator and battery of electric power and the control system use, realize energy circulation.
NOVELTY - This utility new type claims a one horizontal cracking biomass gasification furnace, the structure include furnace body (1), a feeding port (8), a gas nozzle (9), an air inlet (5), dust outlet (7), a feeding port is set on rear end furnace body, the furnace body (1) is an interlayer structure, wherein the interlayer is a gasification room (11), middle air inlet room (12), feed inlet (8) and gas nozzle (9) is connected with the gasification room connected, an air inlet (5) with the air inlet room connected; the furnace body installed on the bottom conveying mechanism (4), a gasification room (11) and air inlet room (12) are connected on the conveying mechanism position. This utility new type of horizontal cracking biomass gasification furnace, introducing cold air inlet, furnace wall and reciprocating grate used for cooling, but also a rear absorbing heat of the heat air flow through reciprocating furnace rows from the material layer upwards from the bottom flow, using a downward from a counter mode, material layer do not overlap in the hybrid operation of reciprocating fire grate, forming a multi-tower-type material layer for schizolysis and gasification, the fire grate a safety stable operation.
NOVELTY - A feeding tube lower This utility new type provide a one integrated biomass gasification furnace, comprise by oxygen supplying device and making device composed of a gasification system, a feeding system and a integrated control box (18), an oxygen supply device comprise a fan (1), connected to the fan (1) of the air inlet pipeline (3), connected to the air inlet pipeline (3) of the oxygen supply room (6), gas-making system include gas reaction room (9), an ash ignition port (7) and gas (11), a feeding system comprise storehouse (13), set with the fuel bin (13), (16), the packing auger shaft set with inner feeding tube (16) (15), a feeding tube (16) of a feeding port (12) connected gas reaction room (9), the feeding tube (16) is close to feeding port (12) is set with air port (2), a pneuma pneuma seal (2) with the air inlet pipeline (3). This utility new type has simple structure, function, there is no tar and smoke discharge, no residue, not a bulk, a operation and so on.
(CN203768315-U)   NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace control system, include the reaction with a furnace body, a feeding device, a feeding motor, a stirring and ash falling device, a stirring motor, a combustion device, a, reaction furnace temperature sensor, a feeding device set on the top of the furnace body., combustion-supporting device set with the reaction furnace body up, stirring and ash.... the inner furnace body. the bottom of the furnace, reaction furnace temperature sensor, reaction furnace temperature sensor and the main control chip input end of electric connecting the feeding motor and stirring motor and the output end of a main control chip electric connect, form inner reaction furnace temperature closed loop control system, which can accurately control reaction furnace inner temperature, furnace body inner fire...
NOVELTY - This utility new type relates to a biological diesel oil one... Mainly composed by storage tank, a tubular reactor, pump, a flow meter, a liquid tank, storage tank by insulating plate is divided into oil storage tank and catalyste methanol raw material storage tank, a tube-type reactor is wound up in the tank. This utility new type the storage tank of a two material design integrally a cylindrical storage tank, use tubular reactor coiled storage tank, reduces the device floor area, reduces the investment, saves land production cost.
NOVELTY - This new type utility claims one a semi-continuous fermentation reactor, include container main body, motor and magnetic force stirrer, gas and so on main body through inner container of vent tube adding straw fermenting a need of condition, the whole fermentation reaction device into the constant temperature box in, a need to ensure the stalk fermentation reaction a temperature condition. With the existing technology phase compare, this utility new type of beneficial effects as follows: add material and convenient sampling, stir uniform, fully fermenting, the fermentation time, the fermentation time is greatly reduced of cotton stalk, increase experiment working efficiency and ensures normal process of experiment.
NOVELTY - This new type utility claims one multi-pool in a water pressure type marsh gas tank, include mechanism moulded glass fiber reinforced plastic quadrate flat top cover, the rectangular fermentation button in the concrete built of a upper opening of pool wall, joint cement seal with seal paste, cement mortar, flat top cover of leakage with a feeding port and a conical feeding tube flange, bolt, inserted movable inserting board is not time seal glue seal, a discharge hole and fermentation, middle by movable plug board, glass steel pool and maintenance, large inner changing material, a fermenting tank time new material is inserted in movable inserting board to prevent the inner tank into water tank in new, marsh gas waste. The upper part of the top feeding port, stir is convenient to feed. Following multi-parallel water tank pressure type marsh gas tank embedded frozen in winter, feeding port and water pressure box is exposed out the ground, cover heat preservation plate heat preservation colour light increasing film. Multi-pool a water pressure type marsh gas tank in parallel, a parallel multi-pool composed of medium and small sized biogas engineering with marsh gas tank. The utility model following beneficial effects: low cost, pool construction, short construction period, low cost operation, energy-saving and environment-friendly, safety and reliable, little investment, high return, quick effect of advanced of marsh gas tank.
NOVELTY - This new type utility claims solar energy hydrogen energy storage device, belonging to the solar energy device technology field. This utility new type comprise solar energy battery plate, proton exchange membrane electrolytic groove and an electric control unit, an electric control unit comprise a one end, a second end, a end and control end, proton exchange membrane electrolytic groove comprise a anode room and cathode room, anode room and cathode room has a upper oxygen exit and hydrogen exit, proton exchange membrane electrolytic groove with electrolytic groove anode and electrolytic groove cathode end, a pipeline connected the anode and cathode of solar energy battery plate connecting a miniature battery of anode and cathode, anode and cathode of solar energy battery board a connecting electric source end one of the anode and cathode of control end connecting pneuma pump, pump connected pneuma, pneuma and pump with a valve a, pneuma pump connected hydrogen exit; exit of a control end, and the control end of a a circuit mounting a valve one; a valve one.
NOVELTY - This utility new type relates to a one high temperature water vapour electrolytic hydrogen making device, wherein the device comprise a, depolymerizing kettle, H2 collector, depolymerization kettle between O2 collector, a bridge, a heat collector, a heating furnace and electrolytic bridge, wherein the heat source through a connecting bridge H depolymerizing kettle and O depolymerization kettle, depolymerization kettle and H2 collector a, depolymerizing kettle and O2 a collector, H depolymerizing kettle and O depolymerization kettle, and H and depolymerizing kettle and O depolymerization kettle through a pipeline a; electrolytic bridge location H depolymerizing kettle and O depolymerization lower part of kettle, and and H between the depolymerizing kettle and O depolymerization kettle through a connecting pipeline between the heat collector on the bridge and a cell bridge, the lower heat collector is equipped with heating furnace. This utility new type is a closeness, the inner system through the heating of water in the electrolytic kettle is changed into high temperature (pressure) steam, and then to the electrolytic kettle is a direct current preparation hydrogen, which can greatly increase efficiency of preparation.
NOVELTY - This utility new type claims a garbage processing, provide a one ecological garbage processing device, comprise of the outer wall body is set and used for collecting garbage fermentation produced a filtered liquid of a filtered liquid collecting room, a square of a percolate collecting room set with filter plate of a filtered liquid for garbage filter, a filter plate and a surrounding outer wall for forming stacking garbage and upper end is provided with an opening of the fermentation room, outer wall body of said upper end cover sealing a fermentation room set with a cover plate, said cover plate is opened with a feed inlet for a fermentation room throwing garbage of said door plate and cover used for sealing said inlet and said movable connecting a cover plate. This utility new type garbage in a fermentation process inner room in the fermentation, the fermentation room is a sealed space, it can ensure the valid environment temperature of microbial growth, increase speed of the garbage, and the garbage are piled on filter plate a, filtered liquid generated by the fermentation due to the action of gravity through the filter plate to the leachate collection chamber, is convenient to compare a percolate collection.
NOVELTY - This new type utility claims one a closed mud aerobic fermentation a oxygen supply control system, wherein it comprise PLC intelligent control host machine, an oxygen supply fan, an air inlet electric valve, an infrared temperature measuring device, an oxygen content detection and a signal transmitting system, an infrared temperature measuring device, an oxygen content detecting a mounting inner expansion cylinder fermentation, the signal output end connecting a PLC intelligent control host computer, a PLC intelligent control host of signal output end connecting oxygen supply fan and an air inlet electric valve, a PLC intelligent control host according to amount and temperature parameter inner the fermentation of a a a a linkage control oxygen supply control system of opening and closing operation, is a microorganism aerobic ferment level according to a material for oxygen, a fermentation temperature. This utility new type has simple structure, convenient operation, it has a good popularization value.
NOVELTY - This utility new type claims a animal organic fertilizer of one manufacturing device, the inlet of said connecting manure cleaning port and the waste opening, a connected manure anaerobic fermentation device, said anaerobic fermentation device set with a gas recovery device, said anaerobic fermentation device connecting solar energy drying set, a solar energy drying set comprise a solar energy drying system, solar energy electric energy drying system, a solar energy drying device set with a deodorizing device, a solar energy drying set connecting packing device. This utility new type through set with manufacturing device of organic fertilizer is livestock cultivation field, increase farm income, saves the cost and the natural resource a valid, is energy-saving and environment-friendly, sustainable development, it can through anaerobic processing the farm waste reuse, and anaerobic treatment process in a produce a gas can be a re-taking the animal cultivation field.
NOVELTY - This new type utility claims one a closed mud aerobic fermentation a a temperature sensing control system, wherein it comprise PLC intelligent control host machine, a transmission system and a multi-temperature sensing probe set on the inner of fermentation cylinder, fermenting cylinder connect with driving the winding axial direction a turning of the power device, the power device comprise motor and transmission system, motor connecting to the PLC intelligent control main machine, fermentation cylinder feeding section comprise of two end, the fermentation of the discharging section and middle section, a feeding section along the axial direction in turn set with a flange and an air inlet electric valve, a temperature sensing probe through a transmission system connecting the PLC intelligent control host computer, a PLC intelligent control host of signal output end connecting electric valve. This utility new type has simple structure, a convenient use and a good popularization value.
NOVELTY - A calcite ore rich in calcium carbonate as raw material is mixed with acid, and then template chosen from monosaccharide, disaccharide, oligosaccharides and sugar or its sugar derivative substances is added to mixture. The obtained mixture is dissolved in organic solvent chosen from methanol, ethanol and ethylene glycol, pH of the mixture is adjusted and reacted. The product is transferred to a hot porcelain boat, aged, calcined in a tube furnace and cooled using desiccator, to obtain porous alkali catalyst having large specific surface area and pore volume.    USE - Porous alkali catalyst is used in ethanol transesterification of fatty acid triglyceride in animal and vegetable oil for preparing biodiesel (all claimed).    ADVANTAGE - The porous alkali catalyst has catalytic activity increased by more than 40%, and high specific surface area and pore volume.    DETAILED DESCRIPTION - A calcite ore rich in calcium carbonate as raw material is mixed with an acid in mass ratio of 1:0.5-1:10, and then template chosen from monosaccharide, disaccharide, oligosaccharides and sugar or its sugar derivative substance is added to mixture. The obtained mixture is dissolved in an organic solvent chosen from methanol, ethanol and ethylene glycol, pH of the mixture is adjusted to 2-7, and reacted at 25-150 degrees C for 0.5-6 hours. The product is transferred to a hot porcelain boat, aged at 25-100 degrees C for 24-120 hours, calcined in a tube furnace at 600-850 degrees C for 1-5 hours and cooled using a desiccator, to obtain porous alkali catalyst having large specific surface area and pore volume.
NOVELTY - Tungsten oxide nanoball peroxidase, is claimed. The nanoball peroxidase is prepared by performing thermal reaction of tungsten hexaethoxide in ethanol solution to obtain tungsten oxide nanoparticle i.e. tungsten oxide nanoball peroxidase.    USE - The tungsten oxide nanoball peroxidase is useful for oxidative degradation of organic pollutant in sewage environment (claimed).    ADVANTAGE - The nanoball peroxidase has simple preparation process, has high reactivity and stability than natural peroxidase, and has high specific surface area and has good catalytic effect.    DETAILED DESCRIPTION - Tungsten oxide (W18O49) nanoball peroxidase, is claimed. The nanoball peroxidase is prepared by performing thermal reaction of tungsten hexaethoxide in ethanol solution to obtain tungsten oxide nanoparticle i.e. tungsten oxide nanoball peroxidase. An INDEPENDENT CLAIM is also included for preparing the tungsten oxide nanoball peroxidase, comprising dissolving tungsten hexaethoxide in 50 ml anhydrous ethanol to obtain 7.5 mM solution, conveying into 100 ml of polyfluortetraethylene reaction kettle, reacting at 200 degrees C for 24 hours, naturally cooling to room temperature to obtain blue substance, centrifuging, washing with ethanol for 3-5 times and vacuum drying for overnight at 60 degrees C to obtain tungsten oxide nanoparticle.
NOVELTY - This utility new type claims a biomass-coal a pyrolysis system, through co-acting microbial biomass and low-rank coal, biomass and a low-rank coal, biomass pyrolysis to promote a coal pyrolysis, in advance, at the same time, it can avoid the pyrolysis process produce sulphur dioxide. Technology scheme a biomass-coal a pyrolysis system, wherein, comprise ball-milling a bioreactor, kneader, a rotary kiln, a water collecting device and rotary dry distillation furnace.
NOVELTY - This new type utility claims one containing a biochemical process of low-rank coal extracting substance and clean efficient comprehensive utilization production line. Technology solution a containing biochemical treatment of low-rank coal extracting substance and clean efficient comprehensive utilization production line comprise washing coal pre-process unit, drying unit, low temperature pyrolysis unit, product collecting separate unit, wherein, further comprise biochemical treatment unit. This utility new type containing a biochemical process of low-rank coal extracting substance and clean efficient comprehensive utilization production line, can remove sulphur in coal in a front end to avoid the low temperature pyrolysis process in produce sulfur dioxide, which is good for environmental protection, at the same time can make the coal part decoupling, reducing energy consumption in a pyrolysis process, reduce the whole technique production cost, further can increase volatile yield, increase high value-added product, improves upgrading technique economic benefit.
NOVELTY - This utility new type claims a biomass of low-rank coal extracting substance and a clean efficient comprehensive utilization production line, through co-acting microbial biomass and low-rank coal, biomass and a low-rank coal, biomass pyrolysis to promote a coal pyrolysis, in advance, at the same time, it can avoid the pyrolysis process produce sulphur dioxide. Technology scheme a biomass of low-rank coal extracting substance and a clean efficient comprehensive utilization production line comprise washing coal pre-process unit, drying unit, low temperature pyrolysis unit, product collecting separate unit, wherein it further comprise a processing unit.
NOVELTY - Biomass fuel pneuma generating a one of a fired ceramic, include combustion pneuma and a purification system. The furnace body of said combustion pneuma generator is installed on the furnace frame upper, inner lower part ash bucket and furnace grate frame welding, an ash hopper set with spraying steam and oxygen distribution device, lower dust hopper is equipped with ash-scraping trolley, a furnace body set with three gas exit and a purification system is connected with the top of the furnace body inner cylinder, inner cylinder form storage hopper, inner cylinder upper part with a circular feeding port, with pneumatic valve is closed. A purification system by exit spray, whirlwind spraying, spray system, cyclone water, water, a sewage processing system and so on part. A combustion pneuma generating device further comprise front furnace bronchial, biscuit firing furnace and a draught fan, draught fan, kiln furnace and the branch pipeline front furnace in turn with each other through connecting, the output end with a device through a pipeline. A combustion pneuma generating device further comprise one electric control system. This utility new type material combustion and gasification stable, high gasification rate, simple operation, reduces the labour intensity.
NOVELTY - This utility new type relates to a dry fermentation one reinforcing mass transfer heat transfer device, belonging to the biomass by using technology field. The device comprise a dry fermentation tank upper support of bracket, said bracket is provided with a lifting up of the injection device. Said injection device comprises injection horizontal pipe, a lower injection pipe is equipped with one group of vertical injection needle tube, lower end of said injection needle tube hinged a pair of duck mouth-shaped injection nozzle of a opening and closing, injection nozzle of a two part outer side extending out a horizontal handle pole, said two injection nozzle is installed between the normally closed state of the tension spring. This utility model rationally utilizing an injection device, breaking through injection, injection to the biogas slurry in material, solves the problem that the fermenting material crust block of liquid, to ensure the biogas slurry mass transfer of heat.
NOVELTY - Inside this utility new type claims a one waste water biological depth treatment device, include anoxic bioreactor (pool) and sedimentation tank, a sedimentation tank in the anoxic bioreactor (pool), wherein said anoxic bioreactor (pool) lower end set with a water inlet I, the upper end set with a water port I, anoxic bioreactor (pool) set with stir device machinery, machinery stir device peripheral set with iron reducing filler. This utility new type through putting iron-containing reducing inner filler in anoxic bioreactor (pool), and machinery match stir the slurry fully mix of state, which avoids reducing filler surface due to adhesion by a microorganism, and a component and of the oxidizing substance in waste water in reducing filler fully reaction, slowly releasing metal ion, reduce anaerobic sludge reduction potential, increase waste water of a biodegradability and good for futher treatment is suitable for all by a low a B/C ratio rear conventional biological wastewater treatment.
NOVELTY - A one ecological aritificial fast and slow water filter sewage treatment device, comprise one leakage closeness, the leakage-proof building body by lower closeness to a set with slow water unit, a unit, impermeable, cover layer, the rapid infiltration unit by first filter layer and the second filter layer are staggered set with forming multi layer structure, and the multi layer structure of most upper layer and the most lower layer is a first filter material layer, a grid cloth water tube set in the multi-network layer structure a part of first material layer in the grid-type cloth water tube network through guide tube is connected, the most upper layer grid cloth water tube network a submersible sewage pump, the multi layer structure most of first material layer in the lower layer set with ventilation tube network, wherein said ventilating tube network connecting one auxiliary heat fan, inner the slow unit set with a third material layer, and one end of the slow water unit set with a slow penetration cloth water system, and the other end set with slow seepage and drainage system, one discharge-observation window set on the anti-leakage closeness building channel, the upper part of seepage through the covering layer to the atmosphere and quick-permeating unit connected.
NOVELTY - This new type utility claims one capable of a stable sewage treatment of biological filter tank, filter tank comprise main body (1) and the filter tank the inner body of a filter (2), a filter pool main body is fixedly connected with a long handle water gun (9), a filter tank body the outer high pressure cleaning machine, set with a long handle water gun comprise integrally connected a water inlet tube (3) and the water tube (4), a water inlet tube (3) is connected with the high pressure cleaning machine connecting tube, the water tube of two radial side is provided with multiple a pore diameter is 2 mm of water spraying hole (7), the filter pool main body outer wall is fixedly connected with a water tank (10). Rear using such a structure, rear long handle water gun with a high pressure cleaning machine extends into inner filter with high pressure water flushing dissipating a filter material, a set of spraying hole so that the flushing and can retain a certain amount of valid biological film, inner tank so as to optimize the microorganism ecological system, set with a water inlet way reduces the impact for a filter material, increase the biological filter tank treatment efficiency of, the biological filter tank can a stable sewage treatment.
NOVELTY - This utility new type claims a one for biological filter pool of water distribution system, comprise filter pool main body, mounting plate, and the upper filter pool main body outer wall is fixedly connected with a water tank, a water distribution box by insulating plate is divided into 4 equal of a cavity, the outer wall of a water distribution tank per a cavity a of each connecting a corresponding one of the filter pool main body connected at the bottom of water input tube and water output tube and the filter pool main body connected at the bottom form a water inlet, a filter head and the filter head mounting a detachable fixing connecting plate, head comprise head main body and a cap, the cap and the fixed inner match end of head main body is connected with a spring, two end main body are set with screw thread. This utility new type rear using such a structure, set in the water inlet of the filter pool water entering into a main body uniform distribute on the filter tank of the inner body, and through set with method of head so that water distribution uniformity, so the water flow quantity stable time, reduces the impact for a filter material, increase the biological filter tank treatment efficiency of water pollution.
NOVELTY - This utility new type claims a one for long handle gun of biological filter tank water reverse flushing system, comprise filter pool main body (1) and the filter tank of the filter head (2), a filter pool main body is fixedly connected with a long handle water gun (9), a filter tank body the outer high pressure cleaning machine, set with a long handle water gun comprise integrally connected a water inlet tube (3) and the water tube (4), a water inlet tube and the water level is 1/4 galvanized tube, a water inlet tube (3) is connected with the high pressure cleaning machine connecting tube, the water tube extends into the filter tank body inner and inserted into the inner filter, the water tube one end far away from the water inlet tube of the end is a sealed end, the water tube of two radial side is provided with multiple a pore diameter is 2 mm of water spraying hole (7) inner body. Rear using such a structure, rear long handle water gun with a high pressure cleaning machine extends into inner filter with high pressure water flushing stagnation block, the size of a water spraying hole is opened so that flushing can retain a certain amount of valid biological film, inner tank so as to optimize the microorganism ecological system.
NOVELTY - Pesticidal soluble granules comprise 1-70% nitenpyram, 1-10% wetting agent, 1-10% synergistic agent, and balance filler. The filler is soluble inorganic salt, lactose, or sugar alcohol.    USE - Nitenpyram soluble granules.    ADVANTAGE - The soluble granules are easy to store and transport, and have good stability, fast disintegration speed, good dispersibility, low impurity content and no environmental pollution. Preparation method is simple, easy to operate and environment-friendly, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for soluble granule preparation by uniformly mixing components, jet milling to obtain nitenpyram soluble powder, uniformly mixing with water, granulating, drying, and sieving.
NOVELTY - Extracting aucubin from Eucommia leaf by using chlorogenic acid involves mixing Eucommia leaf, 40-80% ethanol and chlorogenic acid, extracting at 60-100 degrees C for 1-3 hours to obtain aucubin crude extract, separating aucubin crude extract through NKA-2 macroporous resin adsorption chromatography column, collecting eluate, concentrating the eluate under pressure of -0.05 MPa to -0.09 MPa and at 45-55 degrees C, vacuum freezing and drying to obtain aucubin.    USE - For extracting aucubin from Eucommia leaf (claimed).    ADVANTAGE - The method is safe and suitable for industrial production, converts waste into treasure, is simple and reasonable, and is environmental friendly.
NOVELTY - Biological diesel oil methanol tail gas recovery device comprises esterification condensation system (1), methanol rectifying and purifying system (2), methyl ester vacuum distillation system (3), material transfer system (4), and methanol tail gas continuous recovery device (5).    USE - Biological diesel oil methanol tail gas recovery device.    ADVANTAGE - The device can save energy and reduces consumption, wastewater discharge, volatilization loss of methanol, and biological diesel production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biological diesel oil methanol tail gas recovery device.    Esterification condensation system (1)    Methanol rectifying and purifying system (2)    Methyl ester vacuum distillation system (3)    Material transfer system (4)    Methanol tail gas continuous recovery device (5)
NOVELTY - Processing kitchen waste comprises pretreating food waste by separating food waste and then pressing, biological fermenting waste and then drying, crushing food waste and then sieving, adding tenebrio molitor adults to sieved product, incubating mixture in breeding box to make tenebrio molitor adults lay eggs, preprocessing larva of tenebrio molitor by adding food waste, sieving insect dung from mixture using a screen, preventing the mixture from being infected, and adding pine powder, nitrogen, phosphorus, and potassium to the mixture to prepare an organic fertilizer.    USE - The method is useful for processing kitchen waste that is useful as an organic fertilizer and livestock feed (all claimed).    ADVANTAGE - The method is capable of rapidly processing the kitchen waste with rich nutrition content, protein content of 60% and less area consumption, and without bad odor in an environmentally friendly manner thus increasing the productivity of the fertilizer.    DETAILED DESCRIPTION - Processing kitchen waste comprises pretreating food waste by separating food waste and then pressing, biological fermenting the waste and then drying at temperature of 26-30 degrees C and relative humidity of 60-70%, crushing the food waste and then sieving using a sieve having 8 meshes, adding tenebrio molitor adults to the sieved product at a ratio of 1.2:0.5, incubating the mixture for 3-5 days in a breeding box to make the tenebrio molitor adults lay eggs, preprocessing a larva of tenebrio molitor by adding the food waste at a ratio of 1:2-3, where a density of the mixture is 3-4 cm3, sieving insect dung from the mixture using a screen having a size of 4-8 meshes for 1-3 times, preventing the mixture from being infected, and adding 3% of pine powder, nitrogen, phosphorus, and potassium to the mixture to prepare an organic fertilizer.
NOVELTY - Treatment of kitchen waste using Potosia brevitarsis comprises sorting kitchen waste, extruding, performing biological fermentation, drying until moisture content is 50-60% to obtain suitable food for insect, placing in box, adding P. brevitarsis to feed for 2-3 months and separating adult P. brevitarsis and treated kitchen waste.    USE - Method for treating kitchen waste using Potosia brevitarsis (claimed).    ADVANTAGE - The method is simple and has low operation cost.
NOVELTY - Production of hydrogen and magnesium hydroxide from metallic magnesium comprises mixing magnesium powder and organic solvent, transferring to reactor, heating, reacting, circulating water, cooling, adding hydrogen, controlling liquid level, controlling reactor parameters, discharging residual liquid, pumping gas and collecting. The production special device comprises reactor (1), water tank (2), raw magnesium case (3), hydrogen fuel battery (4), tail material box (5) and hydrogen collecting tank (7).    USE - Method for producing hydrogen and magnesium hydroxide from metallic magnesium.    ADVANTAGE - The device is safe, environment-friendly and energy saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of production special device.    Reactor (1)    Water tank (2)    Raw magnesium case (3)    Hydrogen fuel battery (4)    Tail material box (5)    Hydrogen collecting tank (7)
NOVELTY - River pollution is remediated by establishing intercepting dam on river bed of polluted river average flow surge at daytime to divide river into upstream and downstream, building N-curve pit channel type marsh gas tank in river shore for digestion of daily average flowing sewage, placing methane bacteria in N-curve pit channel type marsh gas tank, pumping intercepted upstream sewage in N-curve pit channel type marsh gas tank, administering anaerobic fermentation decomposition, disinfection, and sterilization for greater than or equal to 93 days, and directly discharging marsh gas residual liquid in downstream river.    USE - Remediation of river pollution (claimed).    ADVANTAGE - Remediation process removes polluted river smell and black color, effectively removes contaminants and kill pathogens, ecologically beautifies downstream river, promotes river with self-repairing capacity after flood, and uses biogas tank having low in cost operation and maintenance which saves investment and turns waste into treasure.    DETAILED DESCRIPTION - River pollution is remediated by establishing intercepting dam on river bed of polluted river average flow surge at daytime to divide river into upstream and downstream, building N-curve pit channel type marsh gas tank in river shore for digestion of daily average flowing sewage, placing methane bacteria in N-curve pit channel type marsh gas tank, pumping intercepted upstream sewage in N-curve pit channel type marsh gas tank, administering anaerobic fermentation decomposition, disinfection, and sterilization at room temperature for greater than or equal to 93 days in which obtained marsh gas is used for power generation or domestic use, and directly discharging biogas residual liquid in downstream river.
NOVELTY - An enhanced ecological floating bed is constructed by connecting polyvinyl chloride (PVC) pipe elbow into rectangular frame structure, laying 2-4 cm double nylon mesh, placing perspective elastic filler (4) into sewage intermittent natural biofilm, exposing for 1st 3 days to discharge 1/5 of water, injecting same amount of sewage, gradually increasing amount of water, forming complete biofilm for 2-3 weeks, controlling dissolved oxygen at 3-4 mg/L, hanging string suspension with density of 30-50, planting 20-30 plants (5) in each square meter of nylon mesh, and purifying using phosphorus.    USE - Construction of enhanced ecological floating bed for ecological restoration of natural water bodies.    ADVANTAGE - Construction process strengthens synergetic effect of microorganism and plant and enhances ability to remove pollutant. Product has good water absorbing effect and is non-sticky.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an enhanced ecological floating bed.    Perspective elastic filler (4)    Plants (5)
NOVELTY - Sewage deodorizing and sludge digesting integrated treatment is performed by setting microorganism cultivation device in biological reaction tank to form microorganism growth environment, sending sludge, sludge reducing agent, and pH regulator into microorganism cultivation device, and treating in which sludge reducing agent supplies nutrients required for growth of microorganism with deodorizing effect and pH regulator regulates pH in microorganism cultivation device.    USE - Sewage deodorizing and sludge digesting integrated treatment (claimed).    ADVANTAGE - Sewage deodorizing and sludge digesting integrated treatment promotes growth and breeding of microorganism with deodorizing function, and sewage deodorizing and sludge digesting integrated treatment device is simple and easy to maintain, has low investment and operation cost and good deodorizing effect, and reduces organic substances in sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for sewage deodorizing and sludge digesting integrated treatment. (Drawing includes non-English language text).
NOVELTY - Sewage treatment device comprises a tank body that is connected to a water inlet through a connecting tube, where the upper end of the tank body is connected to a water tube. The bottom end of the tank body is set with a primary filter layer (1), microorganism absorbing layer (2), filter cloth (3) and an active carbon absorbing layer (4). The microorganism absorbing layer is set with the microbe.    USE - Sewage treatment device used removing heavy metals from sewage (claimed).    ADVANTAGE - The sewage treatment device enables to remove the heavy metals from sewage in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for removing heavy metals from sewage, which involves selecting yeast and alkaline or weak alkaline solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sewage treatment device.    Primary filter layer (1)    Microorganism absorbing layer (2)    Filter cloth (3)    Active carbon absorbing layer (4)
NOVELTY - Method of removing heavy metal including copper, zinc and cadmium in pig manure involves weighing dried pig manure, adding the manure to different amounts of ultrapure water, shaking the resultant products to obtain manure solutions with different concentrations, providing the resultant product into conical bottle, then providing the conical bottle into ultrasonic tank in which ultrasonic process is carried out for 10-90 minutes at 5-40 KHz, filtering the resultant product, centrifuging and drying the resultant product at 40-70 degrees C.    USE - Method of removing heavy metal including copper, zinc and cadmium in pig manure (claimed).    ADVANTAGE - The heavy metal including copper, zinc and cadmium in pig manure is efficiently removed, by simple, economical and environmentally-friendly process.
NOVELTY - Processing sludge containing oil involves reducing the sludge containing oil in an oil concentrate tank, and entering sludge modifying agent into a horizontal spiral centrifugal tank, where the sludge is processed in presence of vacuum in a rotary drum filter to obtain mixture. The obtained mixture is filtered liquid and sludge cake. The modifying agent is acrylamide, acrylate or copolymer of methacrylic acid-containing ester, polyoxyethylene ether or polyether polyhydric alcohol. The sludge cake is processed in a sludge tempering tank.    USE - Method for processing sludge containing oil (claimed).    ADVANTAGE - The method enables to process the sludge containing oil in a cost-effective, simple and eco-friendly manner.    DETAILED DESCRIPTION - Processing sludge containing oil involves reducing the sludge containing oil in an oil concentrate tank, and entering sludge modifying agent into a horizontal spiral centrifugal tank, where the sludge is processed in presence of vacuum in a rotary drum filter to obtain mixture. The obtained mixture is filtered liquid and sludge cake. The modifying agent is acrylamide, acrylate or copolymer of methacrylic acid-containing ester, polyoxyethylene ether or polyether polyhydric alcohol. The sludge cake is processed in a sludge tempering tank. Viscosity reducing auxiliary agent is added into the sludge tempering tank. The viscosity reducing agent is lubricant, polyhydric alcohol or poly alpha-olefin.
NOVELTY - Extraction of water-soluble potassium comprises pulverizing hydromica ore, subjecting to acid treatment, mixing with barium chloride aqueous solution, adjusting pH value to 2-5, reacting to 30-70 degrees C for 1-5 hours to generate potassium ions, and collecting through filtration.    USE - Method for extraction of water-soluble potassium (claimed).    ADVANTAGE - The method is simple and suitable for industrial production, can maintain hydromica ore layer structure, and it has high extraction rate of potassium ion of up to 75%, low cost, and less environmental pollution.
NOVELTY - A composting device comprises composting tower, compost feeding port with first cover, and discharge port with second cover. The first cover is provided with central air supply tube, bracket welded on top supported by a blower, PVC hose sleeve located between the output terminal of blower and blower duct, and heating device. The discharge port is provided with stepped surface, filter, gaskets, exhaust port, and drain valve.    USE - Composting device.    ADVANTAGE - The device provides certain constant temperature to promote the growth of microorganism during piling and fermenting of organic material, accelerates fermentation, avoids odor leakage, and reduces floor area.
NOVELTY - An organic compound fertilizer comprises 15-20 pts. wt. human excrement, 4-6 pts. wt. animal manure, and 12-18 pts. wt. industrial material lees.    USE - Organic compound fertilizer.    ADVANTAGE - The fertilizer increases enzyme activity of saccharide, promotes granule structure in soil to achieve good water retention capacity, and solves depletion of water and organic matter contents problem on soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising mixing raw materials, and stirring.
NOVELTY - Production of tomato planting substrate comprises mixing mushroom residue, cattle manure and pig manure fermentation beds, crushing, adding earthworms to carry out earthworm fermentation, sieving, subjecting to stacking fermentation at certain temperature and humidity, adding fertilizer, checking quality when ferment is mature, reprocessing unqualified products while milling qualified products, and pressing into blocks.    USE - Method for production of tomato planting substrate (claimed).    ADVANTAGE - The method is environment-friendly, and it has wide source of raw materials, stable quality, low cost, and fast and convenient production.
NOVELTY - A hybrid structure three-dimensional fermentation system comprises fermentation material conveyor, ventilating device, dust removal device, deodorizing device, fermentation chamber, feeding device, and clinker conveyor. The system further comprises three-dimensional layered concrete structural frame provided with rows of vertical columns and multiple beams, mounting channel, and cross-rack supports.    USE - Hybrid structure three-dimensional fermentation system.    ADVANTAGE - The environment-friendly fermentation system has low manufacturing cost, long service life, and higher operation stability.
NOVELTY - A servo controlled eccentric block excitation vibration device comprises horizontal fermentation cylinder (16), storage bin door (17), hinge (18), discharging port (19), and cover (21). The device further comprises hollow shaft, spiral stir blade, second servo motor, second speed reducer, second hollow shaft joint, first hollow shaft joint, shaft, bearing, bearing base, eccentric block, first servo motor, first speed reducer, air blower, temperature and humidity regulating device, shaft joint, and pedestal.    USE - Servo controlled eccentric block excitation vibration device used for organic fertilizer fermentation equipment (claimed).    ADVANTAGE - The device accelerates fermenting speed, increases fermentation quality, and makes uniform fermented materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of servo controlled eccentric block excitation vibration device.    Horizontal fermentation cylinder (16)    Storage bin door (17)    Hinge (18)    Discharging port (19)    Cover (21)
NOVELTY - The propane and propylene separation apparatus includes a heat pump rectification system, a heat pump rectifying section, and a stripping heat pump rectification system. The heat pump rectification system comprises a tower top stream reflux pump (5), a rectifying section stream reflux pump (9), and a stripping section stream reflux pump (11).    USE - Propane and propylene separation apparatus.    ADVANTAGE - The propane and propylene separation apparatus optimizes energy coupling between two liquid streams, reduces energy consumption with traditional method, and total investment costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for separating propane and propylene.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the propane and propylene separation.    Propane-propylene separation distillation column (1)    Overhead stream compressor (3)    Condensing heat exchanger (4)    Tower top stream reflux pump (5)    Stream reflux pump (9)    Stripping section stream reflux pump (11)
NOVELTY - Producing methanol from coke oven gas comprises (a) pretreating coke oven gas using a purification apparatus and refining the gas under hydrogen pressure using a pressure swing adsorption hydrogen extraction unit, (b) pretreating 10800 Nm3/hour of methane as a natural gas using a pressure swing adsorption reference methane unit, (c) chemically producing a fuel gas using a wet decarbonization device, and (d) pretreating carbon dioxide gas and hydrogen gas using a gas mixture of hydrogen and carbon dioxide compression device, and pressurizing the gas using a distillation unit.    USE - The method is useful for producing methanol from coke oven gas (claimed).    ADVANTAGE - The method simply produces methanol with good operating conditions.    DETAILED DESCRIPTION - Producing methanol from coke oven gas comprises (a) pretreating coke oven gas using a purification apparatus and refining the gas under hydrogen pressure using a pressure swing adsorption hydrogen extraction unit, (b) pretreating 10800 Nm3/hour of methane as a natural gas using a pressure swing adsorption reference methane unit, (c) chemically producing a fuel gas using a wet decarbonization device, and (d) pretreating carbon dioxide gas and hydrogen gas using a gas mixture of hydrogen and carbon dioxide compression device, where the carbon dioxide gas and the hydrogen gas have a ratio of greater than 3:1 and pressurizing the gas at 5-8 MPa using a distillation unit.
NOVELTY - Synthesis of high purity florfenicol (I) comprises reacting D-threo-2-(dichloromethyl)-4,5-dihydro-5-(p-(methylsulfonyl)phenyl)oxazole-4-methanol (II) as raw material with Ishikawa reagent (III) in the presence of dichloromethane as solvent, washing with diluted alkaline solution, washing with water, adjusting pH to 7-8, concentrating, cooling, crystallizing, purifying, and separating to obtain (4S,5R)-2-(dichloro-acetyl)-4-(trifluoromethyl)-5-(4-(methylsulfonyl)phenyl)-4,5-dihydro-oxazole (IV); adding water as solvent, insulating, hydrolyzing, filtering, washing with pure water, and drying.    USE - Method for synthesizing high purity florfenicol (I) (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has high product purity, low impurity, no solvent residue, and low cost.    DETAILED DESCRIPTION - Synthesis of high purity florfenicol of formula (I) comprises reacting D-threo-2-(dichloromethyl)-4,5-dihydro-5-(p-(methylsulfonyl)phenyl)oxazole-4-methanol of formula (II) as raw material with Ishikawa reagent of formula (III) in the presence of dichloromethane as solvent, washing with diluted alkaline solution, washing with water, adjusting pH to 7-8, concentrating, cooling, crystallizing, purifying, and separating to obtain (4S,5R)-2-(dichloro-acetyl)-4-(trifluoromethyl)-5-(4-(methylsulfonyl)phenyl)-4,5-dihydro-oxazole of formula (IV); adding water as solvent, insulating, hydrolyzing at 50-100 degrees C for 0.5-5 hours, filtering using centrifugal filter, washing with pure water, and drying.
NOVELTY - Quinazoline derivative (II) and alkynyl-type compound (III) are reacted in presence of an organic solvent, and coupling reaction is carried out in presence of copper and/or copper salt and base to obtain erlotinib hydrochloride or its derivative (I).    USE - Preparation of erlotinib hydrochloride (claimed).    ADVANTAGE - The method efficiently provides erlotinib hydrochloride with high yield, under mild reaction condition without affecting the environment.    DETAILED DESCRIPTION - Quinazoline derivative of formula (II) and alkynyl-type compound of formula (III) are reacted in presence of an organic solvent, and coupling reaction is carried out in presence of copper and/or copper salt and base to obtain erlotinib hydrochloride or its derivative of formula (I).    R1=H, SiR1aR1bR1c, or group of formula (i) or (ii);    R2=H or R2a;    R3=halo, OC(O)R3a or OSO2R3b;and    R1a-R1c,R'1a-R'1c,R2a,R3a,R3b=1-8C linear alkyl or 6-12C aryl (both optionally substituted).
NOVELTY - Preparation of N-phenyl piperazine comprises taking aniline and bis-(2-chloroethyl) amine hydrochloride as raw materials at mole ratio of 1:1-2, melting and reacting at 160-250 degrees C, carrying out cyclization reaction, treating with alkaline aqueous solution, and purifying crude product by distilling under vacuum to meet purity requirements.    USE - Method for preparing N-phenyl piperazine (claimed).    ADVANTAGE - The method has simple operation, more than 75% yield, less waste liquid, low cost and more than 99.5% purity as measured by HPLC.
NOVELTY - Preparation of 4-(4-methyl-piperazin-1-ylmethyl)benzamide involves subjecting p-chloromethyl-benzonitrile and N-methylpiperazine to solid phase reaction, obtaining 4-(4-methyl-piperazin-1-ylmethyl)benzonitrile, and hydrolyzing.    USE - Preparation of 4-(4-methyl-piperazin-1-ylmethyl)benzamide (claimed).    ADVANTAGE - The method efficiently provides 4-(4-methyl-piperazin-1-ylmethyl)benzamide with high yield, by simple method without affecting the environment, in short period of time.
NOVELTY - Separation and extraction of ligustilide in Levisticum officinale comprises taking and drying Levisticum officinale, adding petroleum ether at liquid-solid ratio of 5-10 ml/g, soaking at room temperature for 1-5 hours, ultrasonic extracting for 1-5 times for 0.5-2 hours/extraction, mixing extracts, filtering, concentrating under vacuum to obtain paste; and subjecting paste into silicone gel column, adding 100 pts. wt. petroleum ether, and 0.5-5 pts. wt. diethyl ether, ethyl acetate and/or acetone to elute, carrying out thin-layer chromatography detection and concentrating.    USE - Method for separating and extracting ligustilide in Levisticum officinale (claimed).    ADVANTAGE - The method uses inexpensive raw materials, has simple operation, and low environmental pollution. The ligustilide has purity of more than 98%.
NOVELTY - Extraction of flavonoids from Moringa oleifera by drying Moringa oleifera, crushing, packing into filter basket, adding into subcritical extraction kettle, regulating pressure, adding organic extractant, regulating solid-liquid ratio, raising temperature to subcritical state, recovering solvent to obtain black green extract; adding water-saturated n-butanol, centrifuging, collecting extracting phase, concentrating extraction phase in rotary evaporator; and passing extract in macroporous resin column, gradient eluting, detecting, taking, and concentrating.    USE - Method for extracting flavonoids from Moringa oleifera (claimed).    ADVANTAGE - The method ensures flavonoid purity of more than 98%, high extraction efficiency, short operation period, high extraction agent recovery and less energy consumption.    DETAILED DESCRIPTION - Extraction of flavonoids from Moringa oleifera comprises drying Moringa oleifera, crushing, packing into filter basket, adding into subcritical extraction kettle, closing extracting kettle, regulating pressure to 0.06-0.1 MPa, adding organic extractant, regulating solid-liquid ratio at 1:5-20 g/ml, raising temperature to subcritical state, recovering solvent to obtain black green extract; adding 5 times water-saturated n-butanol, centrifuging, collecting extracting phase, concentrating extraction phase in rotary evaporator at 0.01-0.1 MPa to get yellow brown extract; and passing extract in macroporous resin column, gradient eluting, detecting, taking with more than 97% flavone content, and concentrating until dry powder is obtained.
NOVELTY - Preparation of biomass oil involves drying blue green algae mud, and performing pyrolysis in the presence of pyrolysis medium.    USE - Preparation of biomass oil for diesel oil, gasoline and kerosene (claimed).    ADVANTAGE - Biomass oil having high hydrogen content and low oxygen content, is produced with high yield.
NOVELTY - The method involves fixing an inner upper section with a biomass pyrolysis furnace of a heat exchanger. An inner lower section is fixed with an oil furnace. High temperature gas is filled in a furnace inner heat exchanger tube. A heating device is heated in a temperature tar catalytic cracking section. Biomass carbon ash is separated from a furnace bottom exit tube. A tube cracking furnace gas exit valve is connected to a dust-removing cooling scrubber tower. A pneuma furnace lower flow section and an adjustable section are located on a reflux inlet valve for regulating fuel gas.    USE - High temperature biomass gas cracking method.    ADVANTAGE - The method enables selecting high thermal value so as to avoid tar of the heat exchanger.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a high temperature biomass gas cracking method.
NOVELTY - The furnace has a shell (1) whose lower section is connected with a combustion chamber (8). An opening part is fixed with an annular gasifying agent tube. A gasification agent nozzle is mounted on the annular gasifying agent tube. The gasification agent nozzle is extended out of the shell. A bottom part of the combustion chamber is provided with a scroll casing (9). An outer side of the shell is fixed with a biomass raw material feeding hopper (11). A conical hopper (19) is fixed on the combustion chamber through a valve (22) and a discharging tube.    USE - External burner biomass gasification furnace.    ADVANTAGE - The furnace accurately identifies pyrolysis and gasification temperature in an efficient manner, reduces gasification furnace inner excess air amount, nitrogen content in combustion gas, slag carbon-containing amount and combustible biomass preparing cost, improves heat value of the combustion gas and heat utilization efficiency and ensures stable production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an external burner biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an external burner biomass gasification furnace in partial section.    Shell (1)    Combustion chamber (8)    Scroll casing (9)    Biomass raw material feeding hopper (11)    Conical hopper (19)    Valve (22)
NOVELTY - A fuel comprises ethylene glycol monomethyl ether, ethanol and gasoline. The fuel is obtained by mixing 10 ml ethylene glycol monomethyl ether, 5 ml ethanol and 10 ml gasoline at more than 56 degrees C.    USE - Fuel is used as direct ignition fuel (claimed).    ADVANTAGE - The fuel is Manufactured by environmentally-friendly method.
NOVELTY - An alcohol-based liquid fuel contains 90-95 mass parts refined methanol, 3-8 mass parts igniter, stabilizing agent, 0.5 mass part exposing agent, and 1 mass part deodorant.    USE - Alcohol-based liquid fuel for alternative to coal, diesel, and heavy oil used of boilers, industrial furnace, and domestic stove.    ADVANTAGE - Fuel is smokeless upon combustion, low cost, non-toxic, environment-friendly, safe to store and transport, simple to prepare, and has high heat of combustion and calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based fuel which involves placing refined methanol in container, adding igniter followed by deodorant, stirring for 3 minutes, adding exposing agent, stirring for 5 minutes, standing for 10 minutes, adding stabilizing agent, uniformly stirring, and subjecting to static reaction tank for 24 hours.
NOVELTY - A synthetic liquid fuel is obtained by mixing 78-90 %mass methanol and 10-22 %mass water as primary fuel and adding combustion improving agent and deodorant to primary fuel. The addition amount of combustion improving agent is 0.000014-0.000026 %mass. The addition amount of deodorant is 0.000066-0.000156 %mass. The combustion improving agent comprises sodium peroxide and ferrocene. The deodorant comprises potassium permanganate and ammonium nitrate.    USE - Synthetic liquid fuel (claimed).    ADVANTAGE - The synthetic liquid fuel has combustion value of 9000-10000 kcal, and does not produce smell during storage or combustion.
NOVELTY - A kitchen waste oil biofuel is regenerated by mixing methyl or ethyl ester treated waste oil and other oil in which weight ratio of treated waste oil and other oil is 1:0.1-1:2, other oil is kerosene, petroleum ether, naphtha, and/or diesel, and methyl or ethyl ester treated waste oil is prepared by reacting cooking oil with 1.2-10 times equivalent of methyl or ethanol for free fatty acid reaction, adding sulfuric acid, and refluxing for 4-16 hours.    USE - Regeneration of kitchen waste oil biofuel (claimed).    ADVANTAGE - Process is low cost and produces high quality product.
NOVELTY - A phase-stabilizing agent comprises liquid (A) containing 20-35 vol.% toluene, 35-55 vol.% xylene and 25-35 vol.% naphthalene.    USE - Phase-stabilizing agent is used for modified alcohol-gasoline (claimed).    ADVANTAGE - The phase-stabilizing agent has excellent solubilizing effect, anti-aqueous phase separation property and gas barrier property at high temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of phase-stabilizing agent, which involves preparing liquid (A) by mixing toluene, xylene and naphthalene, and preparing liquid (B) by mixing dioctyl phthalate, methyl decanoate and methyl octanoate; and    (2) usage method of phase-stabilizing agent for modified alcohol-gasoline, which contains 5-60 vol.% methanol, 30-85 vol.% straight-run gasoline and 8-20 vol.% liquid (A).
NOVELTY - A biogas is processed by performing biogas wet desulfurization to obtain mixture of gas and calcium hydroxide solution, performing decarburization treatment to obtain gas and suspension, drying to obtain natural biogas, and standing suspension to obtain precipitate which is calcium carbonate.    USE - Processing of biogas (claimed).    ADVANTAGE - Process recycles carbon dioxide and is low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of overall process of processing biogas by biogas treatment system. (Drawing includes non-English language text).
NOVELTY - Reducing acidic value of biodiesel involves dissolving fatty acid of biological diesel oil in methanol and strong inorganic base for performing heterogeneous reaction to obtain a reaction product. The methanol is removed from biodiesel under reduced pressure.    USE - Method for reducing acidic value of biodiesel (claimed).    ADVANTAGE - The method enables reducing acidic value of biodiesel in an efficient manner.
NOVELTY - A micro-algae light biological reactor for waste water depth processing comprises transparent illumination plane serpentine tube (3); liquid circulation pump (2); water inlet end of transparent illumination plane serpentine tube through liquid circulation pump water outlet; circulation pump water inlet through algae liquid collecting tank (1); and water outlet end of transparent illumination plane serpentine tube through algae liquid collecting tank water inlet to form one closed circulation loop.    USE - For waste water depth processing (claimed) to remove sewage nitrogen and phosphorus.    ADVANTAGE - The reactor efficiently removes sewage nitrogen and phosphorus (especially phosphate) from waste water. The reactor has a simple structure; and convenient manufacturing and mounting. The reactor provides simple artificial operation and low energy consumption during operation. Collecting the photosynthesis area and a separate structure, and using the serpentine tube-shaped structure in the photosynthetic area greatly reduces the illumination path, and increases the light photosynthesis efficiency. The collecting tank has a water storage, water, and liquid deposition which reduce the cost of partition construction. The reactor provides small floor area, and high water dissolve oxygen content. The reactor provides fast and accurate control on important operation parameter of process e.g. pH, temperature, CO2/O2 gas balance, stir, sterilizing and dust-removing, which promotes the algae of a light in photosynthesis, and increases water treatment capacity of system.    DESCRIPTION OF DRAWING(S) - The figure shows a micro-algae light biological reactor.    Algae liquid collecting tank (1)    Liquid circulation pump (2)    Transparent illumination plane serpentine tube (3)    Heat exchange device (4)    Valve (5)
NOVELTY - Stirring device with digester system for producing biogas comprises methane tank; and digester that can produce biogas comprising a tank body, where the tank is hinged on the body at the upper part of tank cover and a tube. The tank body is inner set with electric heating tube, a connecting tube of one end passes through the tank cover that is connected with the tank body. The connecting tube of one storage device is connected with the tank body that is further set with the inner tank body. The storage device comprise base and gas storage cavity.    USE - The stirring device with digester system is useful for producing biogas (claimed).    ADVANTAGE - The device has high efficiency for collecting gas. The gas storage device can occupy small space.
NOVELTY - A Devriesia sp. DSE strain 24L-4 (CGMCC No. 9098), is new.    USE - The Devriesia sp. DSE strain 24L-4 is useful for promoting growth of tissue-cultured sugarcane plantlets and potted sugarcane seedlings (all claimed), in production/cultivation of sugarcane, or as microbial agent for preparation of biofertilizer.    ADVANTAGE - The Devriesia sp. DSE strain 24L-4 increases biomass of the tissue-cultured sugarcane plantlets by 57.44% after 30 days and potted sugarcane seedlings by 24.69% after 120 days of application, plant height by 14.44%, stem diameter by 3.53% and fresh weight by 26.26% when compared to control, is environmentally-friendly and has wide application prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the above-mentioned Devriesia sp. DSE strain 24L-4 for promoting growth of tissue-cultured sugarcane plantlets and potted sugarcane seedlings.
NOVELTY - A dark septate endophyte (DSE) strain 24L-4 (CGMCC 9098), is new.    USE - The DSE strain 24L-4 (CGMCC 9098) is useful for promoting growth of tissue-cultured D.candidum plantlets and potted D.candidum seedlings (all claimed), and in preparation of biofertilizer and cultivation of D.candidum.    ADVANTAGE - The DSE strain increases biomass of the plantlets to 19.4%, after 45 days and 18.5%, after 180 days, height of the plantlets to 15.3%, height of the stem to 6.8%, and bud number to 22.1%, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the above-mentioned DSE strain 24L-4 for promoting growth of tissue-cultured Dendrobium candidum plantlets and potted D.candidum seedlings.
NOVELTY - A bacterial strain, specifically Pseudomonas stutzeri, deposited under CGMCC NO. 8646, for efficiently degrading oil sludge in petroleum, is new.    USE - The Pseudomonas stutzeri is useful for efficiently degrading oil sludge in petroleum; and useful as sludge purifying agent (all claimed).    ADVANTAGE - By using the Pseudomonas stutzeri, the degradation rate of aromatic hydrocarbon is 8.08%; and the oil sludge degradation rate of total petroleum hydrocarbons is 53.29%. The bacterial group has strong degradation capacity for n-12-34C hydrocarbon, naphthalene, acenaphthene, and benzo (b) fluoranthene with respective percentage of 44.39%, 27.79%, 30.78% and 39.43% (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a bacterial group for efficiently degrading oil sludge in petroleum, comprising Pseudomonas stutzeri, deposited under CGMCC NO. 8646; and Corynebacterium glutamicum deposited under CGMCC NO. 8647.
NOVELTY - A microbial inoculum is prepared by culturing Bacillus brevis strain 50 L-3a, short soil Bacillus, and Bacillus amyloliquefaciens solid strain to obtain 3 suspensions, inoculating suspension at 3-7 vol.% inoculum size in 1st-stage seed culture medium to obtain cultured suspension, mixing same volumes of suspensions, inoculating at 2-3 vol.% inoculum size in 2nd stage seed culture medium to obtain 2nd level mixed suspension, and fermenting in microbial fermentation culture medium at inoculum size until spore concentration is 2-5x 1012 to obtain fermenting liquid.    USE - Preparation of microbial inoculum for organic fertilizer of municipal domestic garbage and kitchen garbage, and deodorizing and fermenting in livestock (all claimed).    ADVANTAGE - The preparation has low cost, short time, and obtains product which has good deodorization effect and protects environment.    DETAILED DESCRIPTION - A microbial inoculum is prepared by culturing B. brevis strain 50 L-3a, short soil Bacillus, and B. amyloliquefaciens solid strain to obtain 3 suspensions each having 1-3x 108 CFU/ml, inoculating suspension at 3-7 vol.% inoculum size in 1st-stage seed culture medium to obtain cultured suspension having 1-4x 108 CFU/ml, mixing same volumes of suspensions, inoculating at 2-3 vol.% inoculum size in 2nd stage seed culture medium to obtain 2nd level mixed suspension having 2-5x 1011 CFU/ml, and fermenting in microbial fermentation culture medium at 2-6 vol.% inoculum size until spore concentration is 2-5x 1012 to obtain fermenting liquid having greater than or equal to 85% Bacillus.
NOVELTY - Restoration of broth involves mixing refluxed precipitated sludge and high-concentration organic wastewater, adding chromium slag and waste gypsum, stirring, adding resultant mixture to a digestion reactor, performing digestion process, adding 1/2-2/3 digestive liquid to a sedimentation tank, precipitating, adding precipitated sludge to another sedimentation tank, discharging precipitated sludge into the digestion reactor, mixing chromium(IV)-contaminated waste and high-concentration organic wastewater, and performing above process.    USE - Restoration of chromium(IV)-contaminated waste (claimed) e.g. soil.    ADVANTAGE - The chromium(IV)-contaminated waste is efficiently and quickly restored.    DETAILED DESCRIPTION - Restoration of broth involves mixing refluxed precipitated sludge and high-concentration organic wastewater in the ratio of 1:10-15, adding 3-5% chromium slag and 1-2% waste gypsum, stirring uniformly, adding resultant mixture to a digestion reactor, performing digestion process for 2-3 days, adding 1/2-2/3 digestive liquid to a sedimentation tank, precipitating for 5-15 minutes, discharging precipitated sludge, adding remaining digestive liquid containing reduced chromium(VI) ion to broth or its metabolite, adding precipitated sludge to an another sedimentation tank, maintaining for 3-5 minutes, discharging precipitated sludge into the digestion reactor, mixing chromium(IV)-contaminated waste and high-concentration organic wastewater in the ratio of 1:10-15, and performing above process.
NOVELTY - Catalytic electrode includes a three-layer structure composite light electrode, wide gap semiconductor or noble metal nano-particle narrow band semiconductor.    USE - Catalytic electrode used in photo-catalysis of hydrogen.    ADVANTAGE - The semiconductor nano-structure increases the surface area contact interface, thus increasing light energy utilization efficiency, improving the hydrogen production amount and enhancing the corrosion resistance property of electrode.    DESCRIPTION OF DRAWING(S) - The drawing is a flowchart of the preparation of the catalytic electrode (Drawing includes non-English language text).
NOVELTY - This utility new type relates to a one electrolytic groove, belonging to the water electrolysis hydrogen preparing field. Inner lower shell are set with a uniform interval of a clapboard dividing the inner lower shell form several independent of a, open a small electrolytic room, upper end of a plate I through the top fixed bolt and a fixed connecting plate, two adjacent electrode plate I are mounting buckle, a plate I of two side edge a through electrode plate II and the anode and cathode of a lower shell connecting terminal. Advantages: increase electrolytic water making efficiency of hydrogen and reduce the energy consumption. The traditional electrolytic water in hydrogen making device to increase the hydrogen quantity to use multi-groove body connecting a module, only the a multi-groove body connecting a single a groove body structure change of effect, and the way of connecting the electrode plate upper saves the use of lead, which not only increase the hydrogen efficiency and simplifies the whole structure. The practicability is strong.
NOVELTY - Influent wastewater treatment involves setting wastewater inlet proportion with inner reactor and wastewater inlet, where the inner reactor is provided for controlling concentration of microorganism in the influent wastewater.    USE - Method for treating influent wastewater (claimed).    ADVANTAGE - The method enables to treat influent wastewater continuously.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the influent wastewater treatment method. (Drawing includes non-English language text).
NOVELTY - This utility new type claims a biomass gasification and directly one active carbon of the multi-joint device. Device with two large part is composed of upper semi-part is one table biomass gasification furnace, lower half part is furnace activate one of a biomass carbon. A waste heat steam using biomass gasification furnace cooling water as activator, a activate the furnace structure, the traditional steam overheating room and activate a heating room are integrated, small floor space and convenient control, a material, using high temperature resistant alloy steel to replace non-metal refractory material, the heat transfer effect increased greatly, component type a, using efficient heat transfer fin tube, using the waste heat discharge a earlier stage, later using gasification furnace of a gas heating, a directly activated carbon. The whole process is compact and reasonable, economic and practical, and it can save energy and protect environment.
NOVELTY - Cultivating Agrocybe cylindracea, by weighing cotton seed hulls, wheat bran, and auxiliary materials, mixing weighed materials, adding water to mixture, stirring mixture uniformly, sealing with film, fermenting mixture, stirring fermented product, packaging fermented product in bag, sterilizing bag, cooling sterilized bag, inoculating mushroom into bag, placing bag in dry and ventilated place, transferring bag to greenhouse after formation of mycelium, and maintaining 16-20 degrees C temperature and 90-94% humidity.    USE - The method is useful for cultivating A.cylindracea (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly cultivation of A.cylindracea using widely available raw materials and without using chemical fertilizers, pesticides, disinfectants and other chemicals. The cultivated A.cylindracea has increased nutritive value.    DETAILED DESCRIPTION - Method for cultivating Agrocybe cylindracea, involves (a) weighing 50-85 pts. wt. cotton seed hulls, 10-30 pts. wt. wheat bran, and 10-25 pts. wt. auxiliary materials, mixing the weighed materials, adding 65-70 pts. wt. water to the mixture, stirring the mixture uniformly, sealing with film, fermenting the mixture, stirring the fermented product, packaging the fermented product in bag, sterilizing the bag at 120-130 degrees C for 2-3 hours, and cooling the sterilized bag to 20-30 degrees C, (b) inoculating mushroom into the bag, and placing the bag in dry and ventilated place at 20-25 degrees C, and (c) transferring the bag to greenhouse after formation of mycelium, and maintaining 16-20 degrees C temperature and 90-94% humidity.
NOVELTY - Above this utility new type claims a biomass pneuma in one furnace ash discharge slag device, it comprise hearth (3) and a feeding channel (11), wherein a hearth (3) and a feeding channel (11) is around set with a ash-type, said rotary ash-discharge device comprise the ash discharge disk (9) and turntable, inner turntable set with plate (10), a turntable is set in the ash discharge disk (9) rotating connect inner, ash disk (9) set with several ash discharging hole and ash hole through with the hearth (3) inner chamber connected, ash disk (9) set with dust outlet (20) and through (20) and the ash discharging tube (19) connecting, ash disk (9) one side set with the driven wheel and the transmission connecting plate, the driven wheel and the power wheel or power shaft connecting. This utility new type using type ash ash-scraping slag and ash slag, clinker entering into rear ash disk, by scraping the furnace clinker ash discharge port through the inner outer scraper ash discharging tube, and then entering into the box. The whole sealed, ash slag effect is better.
NOVELTY - A downhole fluid comprises a base fluid, and a gelling agent containing an aromatic core having one or more aromatic rings. The gelling agent contains 2 or more amide branches distributed in the aromatic core. The amide branches have one or more organic groups.    USE - Downhole fluid is used as drilling fluid used for treatment of downhole formation (all claimed).    ADVANTAGE - The downhole fluid has excellent gelling properties, and enables efficient treatment of downhole formation, by simple process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) downhole formation treatment method, which involves introducing the downhole fluid into a downhole formation;    (2) preparation of downhole fluid, which involves mixing the base fluid and the gelling agent; and    (3) composition for gelling downhole fluid, which contains the gelling agent and a wetting agent.
NOVELTY - Manufacture of biodiesel involves adding organic solvent, alcohol and catalyst in microalgae, heating, and carrying out simultaneous lipid extraction and transesterification reaction.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The method economically enables manufacture of biodiesel with high conversion efficiency.
NOVELTY - An adsorbent (1000) for adsorbing gas comprises carbon nanotube assembly (100) provided with carbon nanotubes (10) in which shear adhesive force of adsorbent with respect to glass surface at room temperature is greater than or equal to 10 N/cm2.    USE - An adsorbent for adsorbing gas (claimed) used in analysis.    ADVANTAGE - The adsorbent can adsorb multiple types of gas and can be easily fixed to arbitrary parts.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of the adsorbent.    Carbon nanotube (10)    One end of carbon nanotube (10a)    Base material (30)    Carbon nanotube assembly (100)    Adsorbent (1000)
NOVELTY - The method involves determining optical characteristic of color of a carbonized-material and grindability of the carbonized-material. Carbonization condition corresponding to the carbonized-material provided with desired grindability is specified from a profile. Another carbonization condition corresponding to the optical characteristic of the carbonized-material is specified from the profile. A carbonizing machine is controlled such that the latter carbonization condition is correspond to the former carbonization condition.    USE - Method for manufacturing a carbonized-material from biomass by utilizing a carbonizing machine.    ADVANTAGE - The method enables controlling the carbonizing machine such that carbonization conditions are correspond with each other, so that carbonized-material can be manufactured at low-cost with desired property, property of the carbonized-material can be simply determined, running cost of the carbonized-material can be reduced and utilization of biomass can be stimulated.    DETAILED DESCRIPTION - The carbonization condition is carbonization temperature. An INDEPENDENT CLAIM is also included for a carbonized-material quality inspection method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a carbonizing machine.'(Drawing includes non-English language text)'
NOVELTY - An electrode is obtained by forming porous plating film containing nickel on base material containing electroconductive material. The hole diameter of porous plating layer is 5-500 mu m in an area weighted-mean value.    USE - Electrode is used as cathode in hydrogen production by electrolysis (claimed).    ADVANTAGE - The electrode is manufactured by economical process with reduced energy consumption.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of electrode; and    (2) electrolysis method.
NOVELTY - Producing hydrogen involves: a) producing a low pressure synthesis gas mixture from a process selected from steam or carbon dioxide reforming of hydrocarbons, autothermal reforming of hydrocarbons and partial oxidation of hydrocarbons; b) feeding the low pressure synthesis gas mixture to an electro-chemical cell where hydrogen is separated from the low pressure synthesis gas mixture; and c) recovering the hydrogen.    USE - For producing hydrogen (claimed); or for producing high purity, high pressure hydrogen from a low pressure synthesis gas production process.    ADVANTAGE - The method provides use of low cost construction materials, resulting in significant cost savings; provides the production of high purity, high pressure hydrogen while avoiding the need to pressurize the entire synthesis gas mixture. Thus a more cost effective means for hydrogen production results compared to conventional steam methane reforming, dry reforming or partial oxidation processes.
NOVELTY - The system (5) has a riser (15) containing a catalyst (50), where a biological feed (35) comprises biomass-derived liquid for the riser and a hydrocarbon feed (40) comprises hydrocarbons for the riser. The biological feed and the hydrocarbons react in the riser in the presence of the catalyst to convert a portion of the biological feed and the hydrocarbons to hydrocarbon products, where the hydrocarbon products comprise concentration of oxygen of about 0.005 wt. % to 6 wt. %. The biological feed and the hydrocarbon feed are mixed to provide a riser feed.    USE - Fluid catalytic cracking system for producing a hydrocarbon product from biomass. Uses include but are not limited to petrol, ethylene, propylene and butylene.    ADVANTAGE - The system is provided with the riser and/or reactor such that the riser and/or reactor are operated at suitable temperature and pressure, thus providing desired cracking. The biological feed and the hydrocarbon feed are fed to a mixer such that the mixer mixes the biological feed and the hydrocarbon feed, thus providing sonication to the biological feed and the hydrocarbon feed for agitation.    DETAILED DESCRIPTION - The riser feed comprises biological feed of about 0.1 wt. % to 99.9 wt. % and hydrocarbon feed of about 99.1 wt. % to 0.1 wt. %. An INDEPENDENT CLAIM is also included for a method for producing a hydrocarbon product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fluid catalytic cracking system.    Fluid catalytic cracking system (5)    Riser (15)    Biological feed (35)    Hydrocarbon feed (40)    Catalysts (50, 55)
NOVELTY - The method comprises cutting waste wood, old clothes and waste synthetic resin into pieces having a length of 10 cm and then crushing to obtain crushed waste, adding 30 wt.% of food waste, crushed bone and hair and manure into the crushed waste and then stirring at 80 degrees C, adding 50 pts. wt. asphalt into the waste and then stirring at 100 degrees C to obtain a first mixture, adding 10 pts. wt. red clay into the first mixture and then stirring to obtain a second mixture, adding graphite into the mixture and then extruding using a extruder, and adding deasphalted oil into extruded mixture.    USE - The method is useful for manufacturing a pellet using biomass (claimed), where the pellet is useful as a solid fuel.    ADVANTAGE - The method is capable of manufacturing the pellet with excellent combustion efficiency and thermal efficiency.    DETAILED DESCRIPTION - The method comprises cutting waste wood, old clothes and waste synthetic resin into pieces having a length of 10 cm and then crushing to obtain crushed waste, adding 30 wt.% of food waste, crushed bone and hair and manure into the crushed waste and then stirring at 80 degrees C, adding 50 pts. wt. asphalt into the waste and then stirring at 100 degrees C to obtain a first mixture, adding 10 pts. wt. red clay into the first mixture and then stirring to obtain a second mixture, adding graphite into the mixture and then extruding using a extruder, adding deasphalted oil into extruded mixture, and solidifying the mixture to obtain a solid product and then cutting into small pieces.
NOVELTY - Biogas plant comprises a fermenter feed device for the supply of biomass in a fermentation container of the biogas plant. The fermenter feed device comprises a cell disintegration extruder comprising at least one screw shaft (14), which is provided in an extruder housing (16), with a raised screw coil. The cell disintegration extruder comprises at least one supply device for biomass, which is to be extruded, and at least one outlet opening (18) for extruded biomass. At least one raking device with at least one raking prong is arranged in the interior of the extruder housing.    USE - Used as a biogas plant.    DETAILED DESCRIPTION - Biogas plant comprises a fermenter feed device for the supply of biomass in a fermentation container of the biogas plant. The fermenter feed device comprises a cell disintegration extruder comprising at least one screw shaft (14), which is provided in an extruder housing (16), with a raised screw coil. The cell disintegration extruder comprises at least one supply device for biomass, which is to be extruded, and at least one outlet opening (18) for extruded biomass. At least one raking device with at least one raking prong is arranged in the interior of the extruder housing. At least one raking prong with its free prong end is associated with the screw shaft. The raised screw coil exhibits prong recess in each passage area of raking prong. The prong recess is penetrated through the respectively associated raking prong during screw shaft rotation such that biomass solids are scraped and/or removable from the screw shaft.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of the cell disintegration extruder.    Screw shaft (14)    Electric motor (15)    Extruder housing (16)    Outlet opening (18)    Insertion opening (34)
NOVELTY - The fermentation tank has the tank housing (1) that is connected with a coiled water tube (4). The coiled water tube and the tank housing are provided to form a closed loop. The tank housing is connected with a connected tube. The connected tube is connected to a switch valve. The two ends of the coiled water tube and the tank housing are connected to the switch valve. The coiled water tube is connected with an insulating layer (2). A micro water pump is extended out of the tank housing.    USE - Straw fertilizer fermentation tank.    ADVANTAGE - Since the tank housing is connected with the coiled water tube, the inner temperature of the tank is uniform. The tank is heated, without adding supplemental initial heat. The fuel consumption of the tank is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw fertilizer fermentation tank.    Tank housing (1)    Insulating layer (2)    Insulating cover (3)    Coiled water tube (4)
NOVELTY - The device has a hydrogen storage device provided with a storing bottle for storing hydrogen. Average diameter of granule is about 20-200 microns. The storage bottle is fixed with a porous wall surrounding a hollow cavity. The hollow cavity is matched with a pneumatic hole formed in an end of the bottle. An inner part of the hole is matched with a filter. The bottle comprises a shell that comprises an iron-based alloy inner bag and a carbon fiber enhance layer. A power generating device unit is overlapped with a polymer electrolyte film by a porous hydrogen fuel electrode and an air electrode.    USE - Solid state hydrogen power generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - The generating device has a hydrogen storage device provided with a storing bottle. An inner part of the storing bottle is fixed with a hydrogen storing unit. Average diameter of granule is about 20-200 microns. A porous wall is surrounded on a hollow cavity. An end of the storing bottle is formed with a pneumatic hole. An inner part of the pneumatic hole is fixed with a filter. A generating device main body is covered with a polymer electrolyte film that is provided with a porous hydrogen fuel electrode and an air electrode. The storing bottle is made of stainless steel.    USE - Solid state hydrogen power generating device.    DETAILED DESCRIPTION - The hydrogen storage unit is made of nanometer carbon tube, nano-glass ball, nano ceramic, zeolite and nano-fiber material. The stainless steel contains 0.025 mass percent of carbon, 1.00 mass percent of silicon, nickel and manganese, 0.040 mass percent of phosphorus, 0.030 mass percent of sulfur, 0.035 mass percent of nitrogen. The storing bottle is made of fluoropolymer that is PTFE.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - Aerobic microbiological heating of pourable moist organic solids, preferably partially dewatered liquid manure, comprises (i) introducing the solid into a drum (2), (ii) rotating the drum around a rotational axis and simultaneously conveying the solid into the drum, and (iii) introducing oxygen, preferably atmospheric oxygen into the solid via at least one perforated pipe. The pipe extends in the drum and rotates with the drum. The solid is introduced into the drum and/or the solid is discharged from the drum during the rotation of the drum.    USE - The method is useful for aerobic microbiological heating of pourable moist organic solids, preferably partially dewatered liquid manure.    ADVANTAGE - The method is carried out in a safe, cost efficient and energy efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device (1) for carrying out the above mentioned method, comprising the rotatably arranged drum, an insertion device (8) on the drum for entering the solid, a discharge device (9) to the drum for discharging the solid, at least one perforated pipe for introducing oxygen, preferably atmospheric oxygen in the solid, where the tube extends in the drum, and is rotationally fixedly connected to the drum.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic isometric view of the device.    Device (1)    Drum (2)    Insertion device (8)    Discharge device (9)    Supply air connection (22)
NOVELTY - The manufacturing method involves forming the hollow fiber at a nozzle of a spinneret. The polymer resin is mixed with the co-solvent at eighty to one fifty degree centigrade. The polymer resin is made of the polysulfone, the polyethersulfone, the polyimide, the polyether imide, the polyamide, the poly acrylonitrile, the cellulose acetate and cellulose triacetate. The co-solvent includes the N-methylpyrolidone, the dimethylacetamide dimethylformamide, and the dimethyl sulfoxide and gamma-butyrolactone. The polydimethylsiloxane is coated on the surface of the hollow fiber.    USE - Manufacturing method for an asymmetry hollow fiber membrane (Claimed) used in separation of the oxygen or nitrogen from the air.    ADVANTAGE - The polydimethylsiloxane is coated on the surface of the hollow fiber, and thus enhances the precision efficiency of the manufacturing method, improves the gas transmittance and selectivity about the asymmetry hollow fiber membrane, and hence efficiently provides the excellent mechanical property about the asymmetry hollow fiber membrane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an asymmetry hollow fiber membrane made of oxygen, nitrogen, the carbon dioxide, hydrogen and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional schematic view of an asymmetry hollow fiber membrane. (Drawing includes non-English language text).
NOVELTY - Nutrients condensing method involves applying olive oil mills wastewater to organic waste such as animal manure and drying by sun drying based process.    USE - The method is useful for condensing nutrients from the olive oil mills wastewater, and the end product is used by fertilizer distributing machinery (all claimed).    ADVANTAGE - The method enables to condense nutrients from wastewater using energy source of the sun, which is highly cost-effective and renewable.
NOVELTY - Processing method of palm trunk involves crushing palm trunk, squeezing, separating into solid and liquid, distilling liquid component to produce liquid fuel, producing fertilizer from the fraction which remains after distillation of liquid component, compressing solid component and molding to form fuel pellets. During liquid fuel production process, the liquid component is fermented. Squeezing process is carried out until moisture content of solid component is 35% or less.    USE - Processing method of palm trunk (claimed).    ADVANTAGE - The liquid fuel, fertilizer, and fuel pellet are efficiently formed during processing of palm trunk.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the squeezing machine used during processing of palm trunk.    Squeezing machine (2)    Ring roll (21)    Internal roll (22)    Insertion opening (23)    Cylinder (25)
NOVELTY - Manufacture of biomass-derived organic compound involves pulverizing biomass, manufacturing biomass-derived raw material, mixing biomass-derived raw material, catalyst component and pH control component, performing reaction at 373-673K, hydrogen pressure of 0.1-10 MPa and pH of 7-14 for 0.1 to 10 hours, and collecting biomass-derived organic compounds from the obtained reaction liquid.    USE - Manufacture of biomass-derived organic compound e.g. 2-methoxy-phenol, phenol, 2,3,4-methyl phenol, 2,3,4-ethyl phenol, 3,5-dimethyl phenol, 4-ethyl-2-methoxyphenol, 2-methoxy-4-methyl phenol, 2-methoxy-4-propyl phenol, 2,6-di-ethoxy phenol, methoxy benzene, 1,2-dimethoxybenzene, 2-methylnaphthalene, aromatic heterocyclic compounds including furans, (tetra-hydroxy-furan-2-yl) methanol(sic), tetrahydro-2H-pyran, 2-vinyl furan, 2-methyltetrahydrofuran, hexane, propane and naphtha.    ADVANTAGE - The method is economical, and enables manufacture of highly selective biomass-derived organic compound.
NOVELTY - The present invention relates to an eraser and a manufacturing method thereof. The eraser contains: a biomass plastic material of 5-50 wt%, a thermoplastic elastomer of 10-40 wt%, a filler of 5-65 wt% and a softener of 5-40 wt%. Owing to the raw material of eraser in the present invention is made by fermentation and polymerization of biomass raw material, this method can achieve low energy consumption and low carbon emission in the manufacturing process and have lower CO2 emission than the eraser manufacturing method using general petrochemical products.
NOVELTY - The present invention relates to a method of using Botryococcus braunii as biomass gasoline, including: placing Botryococcus braunii in a container, separating algal oil from algal water in said container, and then distilling the algal oil by a fractionation method to obtain biomass gasoline. By this way, the present invention can make Botryococcus braunii directly secrete algal oil into culture medium (i.e. extracellular) and then can convert the algal oil into biomass gasoline by a fast and low-cost manner, such that vehicles can directly utilize biomass gasoline as a fuel without modifying the engine.
NOVELTY - The electrolysis system (1) has a lid that is provided with an inner surface opposite to a housing inside of which a solution containing an electrolyte held at a cell is formed. A controller (3) controls voltage applied to an electrolyzer (2), supplies electric power of a battery (4) to the electrolyzer, and detects the electric current of the electrolyzer. A voltage reduction unit reduces the voltage applied to the electrolyzer when the electric current becomes larger than a setting value.    USE - Electrolysis system for generating hydrogen gas and oxygen gas supplied to internal combustion engine mounted in motor vehicle. Can also be used in boiler apparatus, construction machine and large sized motor vehicle such as truck.    ADVANTAGE - Since the voltage reduction unit reduces the voltage applied to the electrolyzer when the electric current becomes larger than a setting value, and by supplying the voltage reduced by the voltage reduction unit to the electrolyzer, the electric current value of the electrolyzer is reduced, raise of the temperature of the electrolyzer is prevented, and the size reduction of the electrolysis system is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the electrolysis system.(Drawing includes non-English language text)    Electrolysis system (1)    Electrolyzer (2)    Controller (3)    Battery (4)
NOVELTY - The system has a gasification reactor (50) which carries out the gasification process of biomass by supercritical water and nonmetallic type catalyst. The gas, ash content, and nonmetalic type catalyst suspended in water are generated with gasification reactor. The heat of mixture discharged from gasification reactor is utilized, and a double-pipe heat exchanger (40) is provided to preheat hydrous biomass after gasification process. The pressure in the system is adjusted to 27-35 Mpa.    USE - Biomass gasification system for gasification of hydrous biomass such as shochu-liquor residue and hen droppings.    ADVANTAGE - Generation of tar is suppressed when heating the slurry of hydrous biomass or biomass gasified by supercritical water. The clogging in the pipe is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification system. (Drawing includes non-English language text)    Adjustment tank (10)    Crusher (20)    Feed pump (30)    Double-pipe heat exchanger (40)    Gasification reactor (50)
NOVELTY - The method involves starting liquid feeding of the gasification raw material which suspends the activated carbon which is a gasification catalyst to supercritical water gasification system. The water which suspends activated carbon is supplied before supplying the suspension to each apparatus in the supercritical water gasification system.    USE - Method for operating supercritical water gasification system.    ADVANTAGE - The supercritical water gasification of the biomass by activated carbon is performed efficiently, while preventing obstruction of the apparatus by a tar.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the supercritical water gasification system. (Drawing includes non-English language text)    Heat exchanger (30)    Preheater (40)    Reactor (50)    Splitter (60)    Supercritical water gasification system (100)
NOVELTY - The method involves decomposing the to-be-processed water which flows in into processing tanks (2-4) by microorganisms. The support (8) for microorganisms immobilization is injected to any one processing tanks with anaerobic species sludge (7), and the anaerobic treatment of the to-be-processed water is carried out by the microorganisms supported by each support at the time of a stop of the diffuser.    USE - Operation method of sewage treatment unit.    ADVANTAGE - The treated water quality of waste-water on a predetermined level is maintained, even when the aeration to aerobic tank is stopped by certain cause and early restoration is not expected.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the operation process of sewage treatment unit. (Drawing includes non-English language text)    Primary sedimentation basin (1)    Processing tanks (2-4)    Final sedimentation tank (5)    Sludge (7)    Support (8)
NOVELTY - A downhole fluid comprises a base fluid and a gelling agent with an aromatic core of one or more aromatic rings, the gelling agent having two or more amide branches distributed about the aromatic core, each of two or more amide branches having one or more organic groups.    USE - The downhole fluid is useful as a drilling fluid, and as a downhole treatment fluid (all claimed) used for fracturing treatment or for treating downhole formation.    ADVANTAGE - The wetting agent may be used to help wet the surface of the solid amide branched aromatic and pyromellitamide gels, thus speeding up the dissolution of the solid and improving time to gel. The gelling agent may be provided with increased aromatic character in order to improve solvation with aromatic solvents. It can improve the gel stability of water and organic solvent based systems. The gelling agents may be used in oil recovery enhancement techniques.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method which involves introducing the fluid into a downhole formation;    (2) a method of making a fluid which involves combining the base fluid and gelling agent; and    (3) a composition for gelling a fluid, comprising the gelling agent and a wetting agent.
NOVELTY - Feeding a biocide particulate slurry into a treating system, comprises (a) providing a biocide in the form of a dry particulate biocide, (b) combining the dry particulate biocide with water in the absence of organic solvent to provide a biocide particulate slurry, and (c) introducing the biocide particulate slurry into the treating system.    USE - The method is useful for feeding biocide particulate slurry into treating system.    ADVANTAGE - The method: is cost effective due to lower transportation costs and elimination of use of organic solvents, acids, bases or freeze protection additives; improves storage and logistics efficiencies; is environmentally-friendly; and utilizes dry biocides, which are easy to clean and containment in case of an accidental spill.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system (100) for feeding a biocide treatment composition into a treating system, comprising a pump (110), a hopper (120) for providing a biocide in the form of a dry particulate, an auger (130) with a screw feeder for feeding the dry particulate biocide, a conical wetting mechanism (140) for combining the dry particulate biocide with water in the absence of organic solvent to provide a biocide particulate slurry, an eductor for combining the biocide particulate slurry with a pressurized water stream to provide a biocide treatment composition and an outlet line for conveying the biocide treatment composition into the treating system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of a system for feeding a biocide treatment composition into a treating system.    System for feeding biocide particulate (100)    Pump (110)    Hopper (120)    Auger (130)    Conical wetting mechanism (140)
NOVELTY - The biomass gasifier stove (100) has drum (10) which is filled with biomass (50) e.g. sawdust. A pipe (30) is concentrically placed in cavity of the drum. A conical hollow element (20) has bottom portion that is secured to bottom center of the drum and several holes (24) are formed for providing secondary air for combustion. An inlet pipe is horizontally attached to the hollow element. The pipe is set to draw primary air from bottom of the drum due to heating of primary air, to ignite the biomass in the drum. The pipe, hollow element and holes are act as an air preheater device.    USE - Biomass gasifier stove used in cooking or industrial application and community scale cooking application.    ADVANTAGE - Since pipe, conical hollow element and holes are act as air preheater device, efficiency of the biomass gasifier stove is improved. The carbon monoxide emission from the stove is reduced and fuel consumption of the stove is reduced. The power output is made stable. The cost of the stove is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasifier stove.    Drum (10)    Conical hollow element (20)    Hole (24)    Pipe (30)    Biomass (50)    Biomass gasifier stove (100)
NOVELTY - Preparation of artemisinin involves organic solvent extracting artemisinic acid and dihydroartemisinic acid from a residue obtained by extracting Artemisia annua, reducing artemisinic acid with hydrazine hydrate to give dihydroartemisinic acid crude product, dissolving the crude product in organic solvent, adding a photosensitizer and acid catalyst, using a light source to oxidize dihydroartemisinic acid into artemisinin crude product and carrying out column chromatography and recrystallization purification on the artemisinin crude product.    USE - Preparation of artemisinin (claimed).    ADVANTAGE - The method efficiently provides artemisinin having improved conversion rate without polluting the environment.    DETAILED DESCRIPTION - Preparation of artemisinin comprises organic solvent extracting artemisinic acid and dihydroartemisinic acid from a residue obtained by extracting Artemisia annua, reducing artemisinic acid with hydrazine hydrate, followed by slow addition of hydrogen peroxide for 2-4 hours to give dihydroartemisinic acid crude product, dissolving the crude product in organic solvent, adding a photosensitizer and acid catalyst for 1-3 hours, stirring, using a light source to oxidize dihydroartemisinic acid with oxygen at -50 to 50degrees C for 3-30 hours, then at room temperature for 1-3 hours, to give crude artemisinin product, or dissolving the crude product in organic solvent, adding a photosensitizer, stirring, adding to a photo-oxidation reactor with an oxygen or air source at -50 to 50degrees C for 3-30 hours for oxidation, adding acid catalyst at room temperature for 1-3 hours, washing with aqueous sodium bicarbonate, drying the organic phase and concentrating to give crude artemisinin product, and carrying out column chromatography and recrystallization purification on the artemisinin crude product.
NOVELTY - A compound (c) (104) comprising carbon, oxygen and hydrogen, is mixed with water, to obtain wet compound. The wet compound is transferred to reaction processing chamber (102) and heated such that water in the wet compound is dissociated from compound and reacted with compound by non-oxidation reaction, to obtain hydrogen gas.    USE - Method for generating hydrogen gas from compound comprising carbon, oxygen and hydrogen used for producing electrical power and used as replacement of gasoline to run automobile.    ADVANTAGE - The method economically enables generation of hydrogen gas from compound comprising carbon, oxygen and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system for generating hydrogen gas.    System (100A)    Reaction processing chamber (102)    Compound (104)    Heating system (110)    Gas separator (120)
NOVELTY - Producing an organic substance by simultaneous saccharification and fermentation comprises: combining, in the absence of a supplemental nitrogen source, a cellulosic substrate, a whole fermentation broth and a fermenting microorganism; and incubating the cellulosic substrate, whole fermentation broth and fermenting microorganism under conditions conducive both to hydrolysis of cellulose to glucose and/or xylose and to conversion of glucose and/or xylose to organic substance.    USE - The method is useful for producing an organic substance by simultaneous saccharification and fermentation, where the organic substance is alcohol, preferably ethanol (all claimed) which is useful as fuel ethanol, drinking ethanol or as industrial ethanol.    ADVANTAGE - The method: increases the production of the organic substance; and utilizes the reactive composition which is substantially free of supplemental nitrogen source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reactive composition for production of an organic substance comprising a mixture of a cellulosic substrate, whole fermentation broth and fermenting microorganism, where the reactive composition is substantially free of supplemental nitrogen source.
NOVELTY - Producing biodiesel fuel comprises (a) propagating a Desmodesmus strain characterized as having a fatty acid methyl ester content of 2.6% as determined by nuclear magnetic resonance analysis, a nitrogen content of 11.3% and a carbon content of 46.3% to obtain a biomass source, and (b) subjecting the biomass source to transesterification so that biodiesel fuel is produced.    USE - The method is used for producing biodiesel fuel (claimed).    ADVANTAGE - The method for producing biodiesel fuel is simple and low cost. The method produces biodiesel fuel at high yield.
NOVELTY - Vilazodone hydrochloride crystalline polymorphic form B and form A having X-ray diffraction patterns with peaks as given in the specification, are new.    USE - The vilazodone hydrochloride crystalline polymorphic form B and form A are useful as serotonergic antidepressants.    ADVANTAGE - The vilazodone hydrochloride crystalline polymorphic form B and form A: exhibit enhanced storage stability and purity; and can be obtained at high yields and high quality or purity, in a simple, easy, economical, precise, reproducible, environment friendly and industrially scalable manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for preparing the vilazodone hydrochloride crystalline polymorphic form B and form A.
NOVELTY - Feedstock (60) is placed in kiln (10). Fuel is burned in an oxidizer (70) and resultant heated gas from the oxidizer is directed to the feedstock to reduce the moisture content of the feedstock and to pyrolyze the feedstock. Pyrolytic gases released from the feedstock are removed to the oxidizer for burning. Portion(s) of partially inert gases obtained from the burning of the pyrolytic gases are directed to the kiln to controllably continue pyrolysis to the feedstock, to obtain biochar.    USE - Production of biochar used as soil improver.    ADVANTAGE - The method provides biochar by an efficient and economical process. The generation of gases including methane during the production process is reduced. The efficiency of heat recovery during the production process is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biochar manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of production of biochar.    Kiln (10)    Lid (20)    Side walls (30)    Feedstock (60)    Oxidizer (70)
NOVELTY - The apparatus (100) has a first driving roller (111) provided in a conveyance path. A tension sensor (125) detects tension that is provided between a second driving roller (121) and a third driving roller. A driving roller control part controls rotational speed of the second driving roller by feeding back control amount according to deviation of detected tension and target tension to the second driving roller. Another driving roller control part (114) controls speed of the first driving roller based on rotational speed ratio between the first driving roller and the second driving roller.    USE - Apparatus for joining a gas diffusion layer with respect to a strip-shaped membrane electrode assembly during manufacturing of a fuel cell (claimed) i.e. polymer electrolyte fuel cell. Can also be used for manufacturing a phosphoric acid fuel cell, a molten carbonate fuel cell and a solid oxide fuel cell.    ADVANTAGE - The apparatus allows moving average of control amount to be taken such that draw ratio is calculated and the draw ratio can be changed smoothly, so that fluctuation of the tension of a strip shaped unit in a tension area between the second driving roller and the joining roller can be suppressed when a gas diffusion layer of a sheet and disturbance like generated pulse can be injected in tension of a strip-shaped unit and shift of a joining position of the gas diffusion layer can be suppressed with respect to the strip-shaped unit, thus performing cutting with high precision.    DETAILED DESCRIPTION - The third driving roller is a joining roller (152). An INDEPENDENT CLAIM is also included for a joining method.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram of a joining apparatus.'(Drawing includes non-English language text)'    Joining apparatus (100)    Driving rollers (111, 121)    Driving roller control part (114)    Tension sensor (125)    Joining roller (152)
NOVELTY - Adsorbent material, is claimed. The adsorbent material has carbon dioxide adsorption capacity of more than 50 cm3 carbon dioxide/g adsorbent at 273 K and 1 bar pressure, and methane adsorption capacity of less than 35 cm3 methane/g adsorbent at 21 degrees C and 1 bar pressure. The adsorbent material has bulk density of more than 0.55 g/cubic centimeter volume.    USE - The adsorbent material, preferably carbon pyrolyzate adsorbent is useful in apparatus or method for removing carbon dioxide from gas mixture comprising carbon dioxide and methane (all claimed), purifying biogas, natural gas and coalbed methane, and refining oil.    ADVANTAGE - The adsorbent material is selective with carbon dioxide, and has total ash content of less than 1%, bulk density of 0.55-1.25 g/cc, carbon dioxide heats of adsorption and desorption of 5-50 kJ/mole, and radial crush strength of greater than 7 kP.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for manufacturing carbon pyrolyzate adsorbent, involves pyrolyzing polymer or copolymer of polyvinylidene fluoride or polyvinylidene chloride to form pyrolyzate, and activating the pyrolyzate under sufficient conditions of environment, pressure, temperature and time to obtain the carbon pyrolyzate adsorbent;    (2) apparatus having at least one adsorbent bed of carbon pyrolyzate adsorbent that is selective for carbon dioxide when contacted with gas mixture, where the at least one adsorbent bed is arranged (i) for contacting with the gas mixture during first period of time to adsorb carbon dioxide on the carbon pyrolyzate adsorbent in the bed, and discharge from the bed carbon dioxide-reduced methane gas, and (ii) for desorbing previously adsorbed carbon dioxide from the carbon pyrolyzate adsorbent in the bed during second period of time; and    (3) method for removing carbon dioxide from gas mixture, involves contacting the gas mixture with the carbon pyrolyzate adsorbent.
NOVELTY - A solid recovered fuel composition comprises a co-mingled mix of carpet tiles, waste carpets and other waste textiles.    USE - As solid recovered fuel composition useful for reducing the amount of fossil fuel used to power a coal powered generator or cement kiln (claimed).    ADVANTAGE - The solid recovered fuel provides a viable alternative disposal route for carpet tiles that due to their poor combustion properties are currently disposed of mainly in landfill, which incurs a fee. Use of solid recovered fuel composition provides a replacement for coal, reduction in emissions of a range of undesirable gases and heavy metals. In addition to the reducing harmful emissions the use of the waste of carpet made from natural fibers such as wool, provides a further benefit due to the carbon neutral status of biomass. This provides a reduction in carbon dioxide emissions, which provides obvious benefits to operators working to strict emissions levels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing the composition involving providing a first waste stream of carpet tiles; providing a second waste stream of post-consumer carpet waste; processing the first and second waste streams to reduce the size of the waste and produce particles of the waste; co-mingling the first and second waste streams; and    (2) reducing the amount of fossil fuel used to power a coal powered generator or cement kiln involving supplementing or replacing the coal with the solid recovered fuel composition.
NOVELTY - A biodiesel crystallization depressant composition comprises triacylglycerol comprising unsaturated fatty acid(s) (a) in sn-1 position and/or sn-3 position and saturated fatty acid(s) (b) in sn-2 position.    USE - Composition is used for suppressing crystallization of diesel fuel, and biodiesel fuel e.g. fatty acid ester of natural oil. Uses include but are not limited to canola oil, rapeseed oil, coconut oil, corn oil, cottonseed oil, olive oil, palm oil, peanut oil, safflower seed oil, sesame seed oil, etc,.    ADVANTAGE - The composition provides biodiesel fuel having low temperature characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following    (1) A biodiesel crystallization depressant composition comprising a triacylglycerol comprising (a) at least one saturated fatty acid or at least one trans-unsaturated fatty acid in the sn-1 position, and (b) at least one unsaturated fatty acid in the sn-2 and sn-3 position.    (2) A biodiesel crystallization depressant composition comprising a triacylglycerol comprising (a) at least one saturated fatty acid in the sn-3 position, and (b) at least one saturated fatty acid, or at least one trans-unsaturated fatty acid in the sn-1 and sn-2 position.
NOVELTY - The method involves laminating polyimide films, including thermoplastic polyimide films alternating with non-thermoplastic polyimide films. The polyimide films are adhered by applying heat such that the ports (A1,A6,A7,A8) of films communicate with channels (B1,B2) of films.    USE - Method for producing fluid channel device used for distributing fluid containing biological samples (claimed), such as physiological saline, as well as for chemical synthesis including any reaction or fuel cell.    ADVANTAGE - The non-thermoplastic polyimide films suppress deformation of thermoplastic polyimide films, forming the flow channels with high precision. As fluid flow rate can be increased, sample having low flowability can be transported through flow channels at high pressure. Since adhesive to adhere the films are unnecessary, biological samples are not damaged by the adhesive even if the fluid containing the samples flow through the flow control device. Since the flow channel device has high chemical resistance and heat resistance, the device can also use alcohols, organic solvents, and acids. Since adhesives are not used, manufacturing process is simplified and manufacturing costs are decreased, allowing a flow channel device with electrodes to be mass produced with reduced inspection and reaction costs. Since the films are laminated, a flexible flow channel device is realized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a flow channel device.    DESCRIPTION OF DRAWING(S) - The drawing shows the plan view of a flow channel device.    Flow channel device (50)    Holes (51)    Ports (A1,A6,A7,A8)    Channels (B1,B2)
NOVELTY - Anaerobic treatment system comprises an anaerobic treatment tank that anaerobically treats organic wastewater by sludge which is acclimated to a low temperature condition, a state evaluation unit that evaluates a state of the organic wastewater with respect to the anaerobic treatment tank, and a heating unit that heats the organic wastewater which flows into the anaerobic treatment tank, where when the state evaluation unit determines that heating is necessary, a temperature of the organic wastewater is increased by the heating unit.    USE - The apparatus or method is useful for performing anaerobic treatment of organic wastewater (all claimed).    ADVANTAGE - The apparatus performs anaerobic treatment easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic treatment method.
NOVELTY - Converting wet algae biomass to biodiesel, involves reacting the wet algae biomass with a non-catalytic supercritical methanol.    USE - The method is useful for converting wet algae biomass to biodiesel (claimed).    ADVANTAGE - The single-step method operates at modest temperatures and has a lower energy requirement compared to conventional extraction and transesterification methods.
NOVELTY - Pellets comprise 50% lignin having moisture of 40-75 wt.%.    USE - Pellets are used in polymer application and carbon fiber application.    ADVANTAGE - The pellets are efficiently manufactured with high productivity.
NOVELTY - The apparatus has a support plate which is located within an interior volume (9), attached to an electrode (60) and to a core (14), supports the core within interior volume. A non-conducting bushing (64) defines a bushing opening (65) within which electrode is placed. The non-conductive bushing placed between support plate and inside of a case (6), has a configuration that prevents escape of an electrolyte or HHO through an electrode penetration (7) and prevents contact between electrode and liquid electrolyte when liquid electrolyte contained within case and core generates HHO.    USE - Apparatus for generating mixture of hydrogen and oxygen (HHO) used in internal combustion engine, moving motor vehicle, stationary engine and torch.    ADVANTAGE - The combustion of fossil fuels such as gasoline or diesel fuel in engine is improved. The problems such as lack of generation capacity, thermal stability, compactness, efficiency, chemical stability, robustness due to vibrations, shock, rain, wind, freezing and heat, flow control, electric source generator loading and vehicle or structure mounting are eliminated. The overheating of the electrolyte is avoided thus the failure of the hydrogen generator is eliminated. Leakage of hydrogen gas and electrical power is reduced. By using non-conductive fasteners and spacers, the separation between plates is assured thus the arcing and the attendant problems of combustion of HHO in the generator caused by the spark are avoided. The HHO bubble formation and release of bubble from the surface of the plate are improved. The minimal inductive kick back is maintained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of generating HHO.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrode and core mounting.    Case (6)    Electrode penetration (7)    Interior volume (9)    Core (14)    Electrode (60)    Non-conducting bushing (64)    Bushing opening (65)
NOVELTY - Fuel gel comprises alcohol, water and thickening agent.    USE - The gel-type fuel is used in chafers as flowable refilling fuel and for igniting charcoal in food service applications involving grilling and barbecuing. The classic gel-type fuel is used in food preparation or warming; pourable product for use in refilling existing containers or dedicated receptacles; and as igniter which may be squirted on wood or charcoal to produce fire.    ADVANTAGE - The formulation performs in superior fashion in all the basic requirements for superior gel-type fuel. The constituents used are few, with flexibility in the ability to provide variations in the gel-type fuel. By varying the viscosity of the fuel with differing percentage of the gelling agent, three distinctly functioning fuels are produced as a gel, a pourable refilling fuel and a less viscous fire lighting fuel, without the latent smell or taste to affect the taste of the food product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing improved gel-type fuel involving pumping approximately 50% of alcohol into mixing vessel; slowly adding gelling agent with moderate agitation; continuing agitation for 30 minutes; allowing the mixture to rest for 45 minutes to an hour; adding the entirety of water with moderate to vigorous agitation; determine whether the mixture has achieved pH of at least 8-9; adding NaOH to the mixture to achieve pH level of at least 8; adding the balance of the alcohol volume as the mixture gels and continuing with moderate agitation until the mixture achieves the desired smoothness (at least 25000 cPs viscosity).
NOVELTY - Treating organic waste material (10) comprises (a) adding 10-40 gallons of methyl isothiocyanate (MITC)-generating compound (11) per dry ton of organic waste material to organic waste material, (b) combining the MITC-generating compound with the organic waste material, and (c) incubating the combination of the MITC-generating compound and the organic waste material.    USE - The method is useful for treating organic waste material for vector attraction reduction (claimed), where the organic waste material is useful as a soil amendments and fertilizers.    ADVANTAGE - The method allows for reducing the vector attraction effectively and economically, without affecting the beneficial nutrient content of the waste material, and capable of preventing hazards to human health and environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for treating organic waste material, comprising a means for dewatering organic waste material, means for adding MITC-generating compound to the organic waste material after dewatering, means for mixing the MITC-generating compound with the organic waste material, means for conveying the organic waste mixed with the MITC-generating compound to a means for incubating the organic waste material, incubating the organic waste material mixed with the MITC-generating compound for a period of time at a temperature, and means for conveying the organic waste material from the means for incubation to a means for transporting the organic waste material.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart for treating a waste organic material.    Organic waste material (10)    Methyl isothiocyanate generating compound (11)    Mixer (12)    Incubator. (13)
NOVELTY - Ethanol is carbonylated to propanoic acid. Propanoic acid is dehydrated to methyl ketene. Methyl ketene is converted to self addition product. The self addition product is hydrogenated using a catalyst, to obtain 6C alcohol-containing composition.    USE - Preparation of alcohol-containing composition used for manufacturing chemical and fuel for automotive applications.    ADVANTAGE - The alcohol-containing composition enables economical and environmentally-friendly manufacture of high-energy fuel compatible with automotive and transportation infrastructure, from non-petroleum sources such as biomass, coal and natural gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of 3-pentanol, which involves carbonylating ethanol to propanoic acid, ketonizing propanoic acid to 3-pentanone, and hydrogenating 3-pentanone; and    (2) preparation of butanol fuel mixture, which involves carbonylation ethanol to propionic acid, reducing propanoic acid to propanol, carbonylating propanol to butyric acid, and reducing butyric acid to butanol.
NOVELTY - A recombinant yeast host cell capable of producing isobutanol, comprises mitochondria substantially devoid of threonine deaminase activity and pyruvate dehydrogenase activity, is new.    USE - The recombinant yeast host cell is useful for producing isobutanol (claimed) which is used as fuel or fuel additive.    ADVANTAGE - The recombinant yeast host cell produces isobutanol to reduce demand of fossil fuels.
NOVELTY - Thermal energy recovery system has boiler comprising burner configured to produce thermal gases comprising steam and exhaust, cooker configured to cook biomaterial in liquid, a bioreactor comprising anaerobic fermenter component and an aerobic composter component, a thermal gas conduit extending from the boiler through the cooker and the bioreactor, and thermal liquid conduit configured to recover liquid by-products from the boiler and the thermal gas conduit.    USE - The system is useful for recovering thermal energy which is used for processing biomaterial.    ADVANTAGE - The system improves boilers operation, reduces emission of certain regulated compounds, recycles thermal energy.    DETAILED DESCRIPTION - Thermal energy recovery system has boiler comprising burner configured to produce thermal gases comprising steam and exhaust, cooker configured to cook biomaterial in liquid, a bioreactor comprising anaerobic fermenter component and an aerobic composter component, a thermal gas conduit extending from the boiler through the cooker and the bioreactor, and a thermal liquid conduit configured to recover liquid by-products from the boiler and the thermal gas conduit, where the burner has an inlet configured to supply air to the burner, the thermal liquid conduit is configured to direct an acidic portion of the liquid by-products to the cooker and direct a basic portion of the liquid by-products to the bioreactor.
NOVELTY - A modified host cell comprising a heterologous pinene synthase (PS), or its fragment or variant, and optionally a geranyl pyrophosphate synthase (GPPS), or its fragment or variant, or a fusion protein, is new.    USE - The modified host cell is useful for producing pinene or pinene dimer which is used as fuel (claimed).    ADVANTAGE - The modified host cell produces pinene or pinene dimer cost-effectively in large quantities and is suitable for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fusion protein comprising (a) PS or its fragment or variant, and (b) GPPS, or its fragment or variant, where (a) and (b) are linked by a linker; and    (2) method for culturing or growing the modified host cell, involves (a) providing the modified host cell in a solution, (b) culturing or growing the modified host cell, (c) optionally isolating or separating pinene expressed in the solution, (d) optionally chemically catalyzing the pinene to produce a pinene dimer, and (e) optionally using the pinene or pinene dimer as a fuel.
NOVELTY - Inhibiting the growth or reducing the growth rate of one or more rotifers, or inhibiting or preventing a rotifer infestation of an algae culture, comprises contacting the rotifers or the algae culture with an isolated antimicrobial peptide (AMP), where the growth or growth rate of the rotifers is inhibited by the AMP compared to the growth of the rotifers absent in the AMP, or the concentration of the AMP in the algae culture is sufficient to inhibit the growth of and/or reduce the rate of growth of a rotifer in the algae culture.    USE - The method is useful for inhibiting the growth or reducing the growth rate of rotifers in the algae culture (all claimed), where the algae culture is useful for biofuel production.    ADVANTAGE - The method is capable of efficiently controlling and/or preventing rotifer contaminations in algae cultivations thus improving biomass production systems, preferably large-scale systems.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a transgenic algae comprising an expression vector, where the expression vector comprises a heterologous promoter operatively linked to a nucleotide sequence encoding an AMP; and    (2) an expression vector comprising a promoter operatively linked to a nucleotide sequence encoding an AMP, where the nucleotide sequence is codon-optimized for expression in algae.
NOVELTY - Method for generating resources from organic feedstocks, involves receiving an organic feedstock and an isolated rumen in a fermenter, fermenting the organic feedstock with the isolated rumen to produce continuous managed ecosystem fermentation (MEF) to generate a resource comprising biomass, separating the biomass through particulate separation, and dewatering the separated biomass.    USE - The method is useful for generating resources from organic feedstocks. The resources comprise high protein animal feed, fertilizer, lipids, chemicals e.g. volatile fatty acids, preferably acetic acid, biomass, and biogas (all claimed).    DETAILED DESCRIPTION - Method for generating resources from organic feedstocks, involves (a) receiving an organic feedstock and an isolated rumen in a fermenter, fermenting the organic feedstock with the isolated rumen to produce continuous managed ecosystem fermentation (MEF) to generate a resource comprising biomass, separating the biomass through particulate separation, and dewatering the separated biomass, or (b) receiving an organic feedstock and an isolated rumen in a fermenter, fermenting the organic feedstock with the isolated rumen to produce a continuous MEF to generate lipids, chemicals, biomass, and biogas, separating through particulate separation the lipids, chemicals, biomass, and biogas, and separating the chemicals through ion exchange technology to generate one or more volatile fatty acids.
NOVELTY - The electrochemical cell comprises an anode that comprises an electrochemically oxidizable material and is formed as a hydrogen generating electrode, a cathode that comprises an electrochemically oxidizable material and is formed as an oxygen generating electrode, a housing enclosing an interior space in which a separator (105) is arranged, a button cell, a cell cover (102), and a seal (103). The anode and cathode is separated by the separator. The housing has an opening, which is covered by a thin polymer or metal layer.    USE - The electrochemical cell is useful for generating hydrogen or oxygen (claimed).    ADVANTAGE - The electrochemical cell has improved storage stability.    DETAILED DESCRIPTION - The electrochemical cell comprises an anode that comprises an electrochemically oxidizable material and is formed as a hydrogen generating electrode, a cathode that comprises an electrochemically oxidizable material and is formed as an oxygen generating electrode, a housing enclosing an interior space in which a separator (105) is arranged, a button cell, a cell cover (102), and a seal (103). The anode and cathode is separated by the separator. The housing has an opening, which is covered by a thin polymer or metal layer. The thin polymer or metal layer is impermeable to gases consisting of hydrogen, oxygen and carbon dioxide, is provided in the form of a film or a lacquer layer, and has a thickness of less than 40 microns. The electrochemical cell has an opening with a diameter of less than 1.5 mm.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of an electrochemical cell.    Cell cover (102)    Seal (103)    Catalyst electrode (104)    Separator (105)    Polymer or metal layer. (108)
NOVELTY - The embedded biological electrolytic hydrogen production device has an anode room (1) which is communicated to lower portion of cathode room (6). The inner cavity and outer cavity is formed in anode room and cathode room. The anode room is connected with the water inlet. A gas storage tank (8) is connected to upper portion of cathode room, and anode room. The closed cathode (2), diaphragm (3), current collecting network (4) and anode (5) are provided in inner portion of anaerobic oxidation reactor (9).    USE - Embedded biological electrolytic hydrogen production device used in petroleum industry, pharmacy, and chemical industry.    ADVANTAGE - The cost of the embedded biological electrolytic hydrogen production device is reduced. The waste water is treated efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for embedded biological electrolytic hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the embedded biological electrolytic hydrogen production device.    Anode room (1)    Closed cathode (2)    Diaphragm (3)    Current collecting network (4)    Anode (5)    Cathode room (6)    Gas storage tank (8)    Anaerobic oxidation reactor (9)
NOVELTY - Preparing highly purified biological L-tert-leucine involves cloning and expressing leucine dehydrogenase gene and formate dehydrogenase gene in Escherichia coli&gt;. The obtained recombinant Escherichia coli cells are then cultured in a seed culture medium, where the obtained growth of recombinant Escherichia coli cells are then mixed with fermentation culture medium. The obtained fermentation broth is centrifuged to obtain a pellet of recombinant Escherichia coli cells, which is then dissolved in a buffer solution to obtain a cell suspension.    USE - Method for preparing highly purified biological L-tert-leucine (claimed).    ADVANTAGE - The method enables to prepare highly purified biological L-tert-leucine using enzyme that is highly efficient and selective in nature in a simple, specific, eco-friendly, and cost-effective manner.    DETAILED DESCRIPTION - Preparing highly purified biological L-tert-leucine involves cloning and expressing leucine dehydrogenase gene and formate dehydrogenase gene in Escherichia coli&gt;. The obtained recombinant Escherichia coli cells are then cultured in a seed culture medium, where the obtained growth of recombinant Escherichia coli cells are then mixed with fermentation culture medium. The obtained fermentation broth is centrifuged to obtain a pellet of recombinant Escherichia coli cells, which is then dissolved in a buffer solution to obtain a cell suspension. A biocatalytic reaction is performed by mixing reaction substrate with trimethylammonium formate solution with dissolved recombinant Escherichia coli cell suspension in presence of pyruvate formate- lyase to obtain catalyzed L-tert-leucine in the solution. The catalyzed L-tert-leucine found in the solution is then centrifuged to obtain L-tert-leucine solution, which is then passed through column chromatography. The obtained analyte is then dried to obtain concentrated highly purified biological L-tert-leucine as desired product.
NOVELTY - The device has a device body provided with a storing bottle. Average diameter of granule is about 20-200 microns. A porous wall is formed with a hollow cavity that is matched with a pneumatic hole. The pneumatic hole is formed at an end of the storing bottle. A filter is formed with an inner hole. A shell of the storing bottle is made of iron-based porous metal material. The shell is connected with an inner bag and a carbon fiber enhance layer. The device body is made of nano-meter carbon tube, nano glass ball, nano ceramic, zeolite and nano-fiber materials.    USE - Iron-based porous metal composite material solid state hydrogen generation device.    DETAILED DESCRIPTION - The filter is made of metal powder sintering molding part, stainless steel micro net and metal palladium materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an iron-based porous metal composite material solid state hydrogen generation device.
NOVELTY - The device has a hydrogen storage device connected with a hydrogen supply device that is connected with a power generation unit. The hydrogen storage device is provided with a storing bottle that stores hydrogen granule with average diameter of 20 to 200 microns. A porous wall of the storing bottle surrounds a hollow cavity that is formed with a pneuma hole at an end of the storage bottle. An inner hole storing bottle is arranged with a filter that is made of non-metal material. The storage bottle is provided with an inner container that is made of silver cadmium oxide material.    USE - Solid state hydrogen power generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - The device has a device main body provided with a storing bottle. Average diameter of granule is about as 20 to 200 microns. A porous wall of the device main body is formed with a hollow cavity that is matched with a pneumatic hole. The pneumatic hole is matched with the bottle. A filter is formed with an inner hole. A shell of the storage bottle is made of iron-based porous metal material. The shell is connected with a titanium-nickel alloy inner bag and a carbon fiber enhance layer. The main body is made from nano-meter carbon tube, nano glass ball, nano-ceramic, zeolite and nano-fiber.    USE - Titanium-nickel alloy composite material solid state hydrogen generating device.    DETAILED DESCRIPTION - The filter is made of metal powder sintering molding part, stainless steel micro net and metal palladium.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a titanium-nickel alloy composite material solid state hydrogen generating device.
NOVELTY - The generating device has a hydrogen storage device provided with a storing bottle. An inner part of the storing bottle is fixed with a hydrogen storing unit. Average diameter of granule is about 20-200 microns. A porous wall is surrounded on a hollow cavity. An end of the storing bottle is formed with a pneumatic hole. An inner part of the pneumatic hole is fixed with a filter. The storing bottle is made of titanium-nickel alloy. The hydrogen storage unit is made of nanometer carbon tube, nano-glass ball, nano ceramic, zeolite and nano-fiber material.    USE - Solid state hydrogen power generating device.    DETAILED DESCRIPTION - The filter is made of stainless steel micro net, metal palladium or metal powder sintering molding material. The titanium nickel alloy contains 43 to 52 parts of titanium and 48 to 57 parts of nickel.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - The generating device has a hydrogen storage device provided with a storing bottle. An inner part of the storing bottle is fixed with a hydrogen storing unit. Diameter of granule is about 20-200 microns. The hydrogen storing unit is formed with a porous wall that is surrounded on a hollow cavity. An end of the storing bottle is formed with a pneumatic hole. An inner part of the pneumatic hole is fixed with a filter. The storing bottle is made of copper base alloy. The hydrogen storage unit is made of nanometer carbon tube, nano-glass ball, nano ceramic, zeolite, and nano-fiber material.    USE - Solid state hydrogen power generating device.    DETAILED DESCRIPTION - The filter is made of stainless steel micro net, metal palladium or metal powder sintering molding material. The copper base alloy is made of 0-20 parts of beryllium and 0.5-1.5 parts of copper.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - The generating device has a hydrogen storage device provided with a storing bottle. An inner part of the storing bottle is fixed with a hydrogen storing unit. Average diameter of granule is about 20-200 microns. A porous wall is surrounded on a hollow cavity. An end of the storing bottle is formed with a pneumatic hole. An inner part of the pneumatic hole is fixed with a filter. The storing bottle is made of titanium-nickel alloy. The hydrogen storage unit is made of nanometer carbon tube, nano-glass ball, nano ceramic, zeolite and nano-fiber material.    USE - Solid state hydrogen power generating device.    DETAILED DESCRIPTION - The filter is made of stainless steel micro net, metal palladium or metal powder sintering molding material. The titanium-nickel alloy contains 48- 57 parts of titanium and 43-52 parts of nickel.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a solid state hydrogen power generating device.
NOVELTY - This utility new type relates to a one organic waste treatment device, especially relates to a biological fermentation process one device, the crushing device, the fermentation treatment device, sterilizing device and drying device a small computer and a process control management, at the same time, set a bone sieve at the end exit of a bottom of a set with a conveying belt. Through the device for a large animal cultivation field afterbirth, died of livestock carrying out harmless treatment, so as to realize the zero discharge without pollution. Rear afterbirth, died livestock through the crushing device, makes full use of rear crushed straw, wheat straw and other crop by-product as fermentation substrate, a special biological strain, fully stir a rear produce high fermenting it at high temperature, killing pathogenic microorganism, rear all decomposed into high-quality organic fertilizer, a change waste into treasure, it not only ecological environment-friendly and promotes the agriculture production benign circulation, but also solves the burning straw, wheat straw and crop waste caused by a pollution problem.
NOVELTY - Hydroxyl group of 4-(4-((5R)-5-(hydroxymethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (V) is converted to highly active leaving group, to obtain leaving group-containing compound (IV). The resultant product is reacted with nucleophilic reagent (VI) in the presence of base (b1), and nitrogen ions are provided to obtain 4-(4-(2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one derivative (III). The resultant product is deprotected, to obtain 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (II) or its salt.    USE - Preparation of aminomethyl-2-oxo-1,3-oxazolidin-3-yl-phenyl morpholin-3-one (claimed).    ADVANTAGE - The aminomethyl-2-oxo-1,3-oxazolidin-3-yl-phenyl morpholin-3-one is prepared by simple, economical and environmentally-friendly method under mild reaction conditions using simple purification techniques.    DETAILED DESCRIPTION - Hydroxyl group of 4-(4-((5R)-5-(hydroxymethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one of formula (V) is converted to highly active leaving group, to obtain leaving group-containing compound of formula (IV). The resultant product is reacted with nucleophilic reagent of formula: W1-NH-W2 (VI) in the presence of base (b1), and nitrogen ions are provided to obtain 4-(4-(2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one derivative of formula (III). The resultant product is deprotected, to obtain 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one of formula (II) or its salt.    L=leaving group chosen from halo, preferably chloro, bromo or iodo, or -OSO2R;    R=1-6C alkyl or optionally substituted aryl;and    W1,W2=carbonyl, alkoxycarbonyl, trialkylsilyl or dialkoxy phosphoryl.    An INDEPENDENT CLAIM is included for 4-(4-(2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one derivative (III).
NOVELTY - Microbial agent comprises Bacillus sp. EBW4 (KACC91749P) culture product having organic matter decomposition function of protein, carbohydrate, lipid or surfactant, and esterase activity and salinity tolerance, where the Bacillus sp. is identified from lugworm.    USE - The microbial agent is useful for fish farm wastewater purification (claimed).    ADVANTAGE - The microbial agent recycles breeding water and protects environment, and purifies water contaminated with organic matter.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) fish farm wastewater purification process, comprises spraying the microbial agent comprising Bacillus sp. EBW4 culture to breeding water for decomposing organic matter including protein, carbohydrate, lipid or surfactant; and (2) preparing the microbial agent by inoculating Bacillus sp. EBW4 (KACC91749P) identified from lugworm in a culture medium, and culturing at 25-30 degrees C for 1-2 days.
NOVELTY - Antioxidant composition comprises hydroquinone based antioxidant, and basic additives including triethylenetetramine and/or triethylenepentamine.    USE - The antioxidant composition is useful for biodiesel fuel (claimed).    ADVANTAGE - The composition exhibits improved oxidation stability.
NOVELTY - Biofertilizer product based on non-symbiotic nitrogen-free fixing bacteria comprises Azospirillum sp., 0.01-0.5% of carboxy methylcellulose, 2-5% of preserving and stabilizing agent, and sterile water.    USE - The biofertilizer product is useful as an agricultural fertilizing product for biological fixation of atmospheric nitrogen in the soil and for the stimulation of plant growth (claimed). No biological data given.    ADVANTAGE - The biofertilizer product exhibits improved agricultural soil fertility and good bacterial strain stability for a long time, stimulates the assimilation of nutritional elements, and increases the crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing biofertilizer product, comprising adding a stabilizing agent before the stationary phase and just before the end phase exponential growth of both two bacterial strains.
NOVELTY - A Bacillus amyloliquefaciens strain LMS 1207 (KCCM 11341P), is new.    USE - The B.amyloliquefaciens strain LMS 1207 is useful in composition and as deodorant for treating sewage or wastewater, and removing bad odor caused by decomposition of sulfur compounds and ammonia compounds (all claimed).    ADVANTAGE - The B.amyloliquefaciens strain LMS 1207 enables to remove bad odor without chemical treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition or deodorant, which comprises B.amyloliquefaciens strain LMS 1207, culture material of the B.amyloliquefaciens strain LMS 1207, or condensed products of the culture material as active ingredient.
NOVELTY - Method for producing saccharified solution of wood-based biomass having toxicity reduced or removed, involves hydrolyzing wood-based biomass, preparing saccharified solution in which wood-based biomass has been pretreated by hydrolysis, and removing or reducing toxicity of the saccharified liquid by electrochemical treatment method.    USE - The method is useful for producing saccharified solution of wood-based biomass having toxicity reduced or removed, which is used for producing bio-chemical or bio-fuel (all claimed).    ADVANTAGE - The method reduces phenolic compound to 50 wt.%, polychlorinated dibenzofuran to 90 wt.%, coumaric acid to 70 wt.%, ferulic acid to 25 wt.%, vanillin to 45 wt.%, syringaldehyde to 70 wt.%, and 5-HMF to 90 wt.%, usage of microorganism and cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing bio-chemical or bio-fuel, involves fermenting the saccharified solution of wood-based biomass; and    (2) saccharified solution of wood-based biomass.