NOVELTY - Preparing iron pyrite cinder concentrate comprises (1) leaching pyrite cinders in a nitric acid and hydrochloric acid mixed solution solid to obtain a nitrate leaching slag phase and hydrochloric acid residue, dissolving the residue in ferric chloride solution and then filtering and roasting to obtain iron ore, spraying acid hydrolysis slag on the iron ore and then adding supplemental nitrogen, phosphorus and potassium into a nitro slag compound and (2) introducing the pyrite cinders into nitric acid to obtain iron ore leaching slag and then acid infusion through the iron ore.    USE - The method is useful for preparing iron pyrite cinder concentrate (claimed).    ADVANTAGE - The method is capable of preparing iron pyrite cinder concentrate with high iron resource utilization rate and without pollution.    DETAILED DESCRIPTION - Preparing iron pyrite cinder concentrate comprises (1) leaching pyrite cinders containing sulfur, arsenic and other impurities in a nitric acid and hydrochloric acid mixed solution to obtain a nitrate leaching slag phase and hydrochloric acid residue, dissolving the residue in ferric chloride solution and then filtering and roasting to obtain iron ore, spraying acid hydrolysis slag having cement additives or construction materials on the iron ore and then adding supplemental nitrogen, phosphorus and potassium into a nitro slag compound to remove arsenic, and (2) introducing the pyrite cinders having sulfur, arsenic and other impurities into nitric acid to obtain iron ore leaching slag and then acid infusion through the iron ore to remove arsenic after adding supplemental nitrogen, phosphorus and potassium, where the nitric acid and hydrochloric acid is carried out when the pyrite cinder contains silicon dioxide content of 10%, and nitric acid treatment is carried out when the pyrite cinder contains silicon dioxide content of less than 10%.
NOVELTY - A dimethyl malonate is prepared by reacting sodium chloroacetate and sodium cyanide to obtain sodium cyanoacetate solution, acidifying by adding dilute hydrochloric or by introducing sodium cyanoacetate solution in hydrogen chloride gas, performing solid-liquid separation to obtain acetic acid-hydrochloric acid solution and sodium chloride, concentrating acetic acid-hydrochloric acid solution by performing vacuum distillation to obtain cyanoacetic acid-hydrochloric acid solution, and esterifying sulfuric acid by catalytic esterification reaction to obtain cyanoacetic acid and methanol.    USE - Preparation of dimethyl malonate for medicine e.g repaglinide, pesticides, dyes, and synthetic polyphthalamides.    ADVANTAGE - The method reduces desalination and wastewater generation, is low cost, simple, environment-friendly, and has high yield.    DETAILED DESCRIPTION - A dimethyl malonate is prepared by reacting sodium chloroacetate and sodium cyanide by cyanide reaction to obtain sodium cyanoacetate solution, acidifying by adding dilute hydrochloric acid to generate hydrogen chloride gas, acetic acid and sodium cyanide, or by introducing sodium cyanoacetate solution in hydrogen chloride gas to generate cyanoacetate and sodium chloride, desalting by performing solid-liquid separation to obtain acetic acid-hydrochloric acid solution and solid sodium chloride, concentrating acetic acid-hydrochloric acid solution by performing vacuum distillation to obtain cyanoacetic acid-hydrochloric acid solution, and esterifying sulfuric acid by catalytic esterification reaction to obtain cyanoacetic acid and methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the preparation of dimethyl malonate. (Drawing includes non-English language text).
NOVELTY - The waste gas processing apparatus has fuel cell which is provided with a membrane electrode assembly, and a fuel-supply unit which supplies the hydrazine to anode of fuel cell. An air supply unit supplies air to the cathode of fuel cell, and an exhaust pipe (108) discharges the gas discharged from the fuel cell to air. A muffler (109) is provided in the middle of exhaust pipe, and a space surrounded by the ammonia-removal sheet (152), water absorption unit (153), and inlet opening of muffler main body (151) is provided inside the muffler main body.    USE - Waste gas processing apparatus for fuel cell system.    ADVANTAGE - Reduces the quantity of aqueous ammonia discharged to the exterior of fuel cell system, and suppresses the quantity of moisture content since the water absorption units function as a heat insulating material when distributing inside the muffler.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the muffler of the waste gas processing apparatus.    Exhaust pipe (108)    Muffler (109)    Muffler main body (151)    Ammonia-removal sheet (152)    Water absorption unit (153)
NOVELTY - Organic liquid fertilizer comprises 45-55 wt.% of chicken manure, 22.5-27.5 wt.% of rice bran, and 22.5-27.5 wt.% of soybean cake. The fertilizer is produced by mixing chicken manure, rice bran and soybean cake, diluting the mixture and then performing anaerobic fermentation for 40-60 days.    USE - The organic liquid fertilizer is useful for fruit cultivation (claimed). No biological data given.    ADVANTAGE - The organic liquid fertilizer is eco-friendly, and improves the quality of the fruit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the organic liquid fertilizer comprising mixing chicken manure, rice bran and soybean cake, diluting the mixture for 71-15 times, and then performing anaerobic fermentation for 40-60 days.
NOVELTY - Producing environmentally-friendly liquid fertilizer using enzyme, involves decomposing organic matter using microbes, performing catalyze degradation of molecule using an enzyme-producing environment-friendly manure, and breaking carbohydrate molecules using amylase, breaking protein molecules using protease, and breaking fat molecules using lipase.    USE - The method is useful for producing the environmentally-friendly liquid fertilizer using enzyme (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - Preparation of 3-chloro-4-fluoro-aniline hydrochloride involves 1) taking 3,4-dichloro-nitrobenzene in a reaction vessel, adding fluorinated salt and dissolving in a solvent, reacting at reflux for 5 hours, steam distillation to give 3-chloro-4-fluoro-nitrobenzene, where salt is selected from potassium fluoride and cesium fluoride; 2) reducing 3-chloro-4-fluoro-nitrobenzene in presence of palladium-carbon, and methanol at room temperature, cooling; 3) dissolving 3-chloro-4-fluoro-aniline in a solvent, to which passing hydrogen chloride gas, introducing tail gas into alkali solution.    USE - For preparation of 3-chloro-4-fluoro-aniline hydrochloride (claimed).    ADVANTAGE - The process allows little byproduct, stable product property, reduction of the nitro group with hydrogen and Pd-C at room temperature, reaction carried out only on less demanding reaction equipment and solvents, and Pd-C can be recycled, excess hydrogen chloride (HCl) gas in the alkali liquid, and avoids the environmental pollution.    DETAILED DESCRIPTION - Preparation of 3-chloro-4-fluoro-aniline hydrochloride involves 1) fluorine substitution: taking 3,4-dichloro-nitrobenzene in a reaction vessel, adding fluorinated salt and dissolving in a solvent, reacting at reflux for 5 hours, steam distillation to give 3-chloro-4-fluoro-nitrobenzene, where the fluoride salt is selected from potassium fluoride and cesium fluoride; 2) hydrogenation: reducing 3-chloro-4-fluoro-nitrobenzene in presence of palladium-carbon (Pd-C), and methanol at room temperature for 6 hours, recycling solvent and Pd-C, cooling to give 3-chloro-4- fluoro-aniline; 3) forming salt: dissolving 3-chloro-4-fluoro-aniline in a solvent, to which passing hydrogen chloride gas, introducing tail gas into alkali solution, filtering, and drying to give 3-chloro-4-fluoro-aniline hydrochloride.
NOVELTY - Cultivating Hypsizygus marmoreus, comprises preparing nutrient solution by mixing glucose, corn starch, bean powder, heat resisting amylase, gellan gum, and water, sterilizing the nutrient solution, transferring the solution to a bottle, and then sterilizing the bottle, cooling the bottle, separating Hypsizygus marmoreus JB06 from liquid strain, and then inoculating into the nutrient solution, transferring the bottle containing inoculated Hypsizygus marmoreus JB06 to a cultivating chamber, and cultivating.    USE - The method is useful for cultivating Hypsizygus marmoreus (claimed).    ADVANTAGE - The method rapidly cultivates edible and ornamental Hypsizygus marmoreus in a simple and environmental friendly manner.    DETAILED DESCRIPTION - Cultivating Hypsizygus marmoreus comprises preparing nutrient solution by mixing 2% of glucose, 1-10%of corn starch, 1-4% of bean powder, 1-1000 units of heat resisting amylase, 0.01-0.1% of gellan gum, and water, sterilizing the nutrient solution at a temperature of 121 degrees C and a pressure of 150 kPa for 20 minutes, transferring the 100 ml of solution to a 250 ml of bottle with a height of 3 cm, and then sterilizing the bottle at a temperature of 121 degrees C and a pressure of 150 kPa for 20 minutes, cooling the sterilized bottle at 20 plus minus 2 degrees C, separating Hypsizygus marmoreus JB06 from 5 ml of liquid strain, and then inoculating into the nutrient solution, transferring the bottle containing inoculated Hypsizygus marmoreus JB06 to a cultivating chamber having a culture temperature of 23 plus minus 1 degrees C and humidity of 75 plus minus 5%, harvesting at a temperature of 25 plus minus 2 degrees C and a humidity of 95% for 10 days, and controlling the illumination intensity at 70 lx for 1-5 days and then at 500 lx for 6-10 days.
NOVELTY - Method of planting grass, involves using sand mixed material comprising 1000 kg crop straw, 300 kg dairy manure and 1 kg composite ferment bacteria, raising the temperature to 50 degrees C for 3-5 days, fermenting the mixed material at 50-60 degrees C for 3-4 days, reducing the temperature to normal temperature, obtaining the sand mixed material bag, then adding 200-300 kg sand mixed material, 1-5 kg plant seed and 1-5 kg paper swelling agent, stirring for 5 minutes, and spraying the mixture.    USE - The method is useful for planting grass (claimed).    ADVANTAGE - The method replaces petroleum byproduct mixed material for natural gel material and sand-fixing material, prevents sand surface compaction, and improves plant seed germination, normal growth and development. The method is cost-effective and simple.
NOVELTY - This utility model claims a kind of sulphate recycling method of desulfurized waste liquid of a system, comprising a reaction kettle, a centrifuge, a the upper part of the reaction kettle is set flue gas inlet, a flue gas outlet, a cooling water inlet, a cooling water outlet, a centrifuge and a the bottom of the reaction kettle are connected by a pipeline. This utility model has the advantages of using flue gas waste heat as the heat source of waste water for treating and recovering ammonia desulphurization waste liquid is ammonium sulphate or magnesium oxide method desulfuration of magnesium sulphate, a desulfurizing system in the waste liquid without waste liquid discharge and protects the environment, recycling the obtained ammonium sulphate, magnesium sulphate can be used as fertilizer to improve comprehensive utilization value of the waste liquid, a system is featured with simple structure and less investment.
NOVELTY - This new type utility claims one from a hot cross lug boss array alcohol reformer. From upper to lower in turn hydrogen plate and catalytic combustion plate composed of a hydrogen purifying part. Reforming the hydrogen in a reforming hydrogen production cavity plate, a load limiting catalyst for producing hydrogen for alcohol reforming produce hydrogen catalytic combustion plate in catalytic combustion chamber is loaded with combustion catalyst, alcohol used for combustion. Through alcohol combustion reforming hydrogen production provide heat, it can realize the alcohol of from hot reformer. Hydrogen reforming and catalytic combustion chamber inner cavity there is an error - dummy club matrix structure, large specific surface area, hot transfer mass transfer efficiency is high. And alcohol reformer containing hydrogen purifying part, which can improve the reforming hydrogen cavity of the fuel conversion efficiency, at the same time, hydrogen can exit directly for hydrogen fuel battery use. This utility new type structure is compact, catalyst loading is convenient, the whole structure is easy to assemble, can be used for in small flow amount alcohol reforming hydrogen production.
NOVELTY - This utility new type relates to a one a synthetic ammonia tail pneuma system. Parallel rear. the methane recovery device of water seal fire retardant device A and water-sealing fire. B, pneuma. rear cabinet on the water-sealing fire. B, before water seal fire retardant device A and water seal fire retardant device B of a methane recovery device in parallel using a connecting pipeline, a boiler, a pneuma cabinet, a water seal fire. B, water seal fire retardant device A and methane recovery device after all. with valve. This utility new type is added by using a system of synthetic ammonia tail pneuma, directly putting the original tail pneuma of air in a using process, it not only saves the resource, reduces the production cost, but also greatly reduces the process for production of the environment pollution, the comprehensive utilization of.
NOVELTY - This utility new type provide a one ammonia oxidizing furnace ignition device, include head, an ignition box, an ignition cable and hydrogen tube, ignition head is composed of a spark plug, an ignition connecting pole and insulation tube, steel pipe and seal device is composed of a lighting box four sides of steel plate is composed of a lighting head through first connecting flange with the ignition box connecting the ignition cable through cable gland head extending to the ignition box, ignition connecting pole of ignition head connect with the ignition cable in the ignition box, hydrogen tube outlet is located spark plug ignition electrode. This utility new type structure is simple, the manufacture is convenient, it can reduce the production cost is valid.
NOVELTY - The biological film processing device has a main casing (1) that is provided with active bio-film filling layer in bottom portion. The air blowing holes are formed on the top portion of main casing. An annular portion (3) is set with lower end section and upper end guidance portion. The water flow accelerating surface is connected with horizontal air outlet joint. The active biological film sub-layer is set with semi-spherical framework weaved polycarbonate wire. The biological active component is composed of amidogen silicon ball and sodium alginate.    USE - Industrial sewage biological film processing device.    ADVANTAGE - The organic pollutant degradation reaction area can be provided. The principle of fluid mechanics is used to reduce the pump drives for sewage flow. The energy can be saved. The wastewater amount can be driven though air outlet. The outlet water flow speed is fifteen times more than the normal flow speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the industrial sewage biological film processing device.    Main casing (1)    Annular portion (3)
NOVELTY - The method involves providing a kettle comprising constant temperature chamber in biological generator. The constant temperature chamber is connected with liquid inlet through liquid inlet overflow joint. An overflow tube is connected with lower portion air inlet. M-level bio-generating system (3) is arranged for simulating water temperature, climate and water quality.    USE - Method for treating sewage.    ADVANTAGE - The sewage can be treated efficiently at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-generating system.    Bio-generating systems (1-9)
NOVELTY - Preparation of cement rotary kiln process mixed fuel involves crushing stored rice hull into less than 0.8 mm, crushing stored anthracite as raw coal, introducing the crushed product into discharge tube of coal mill system, providing the resultant product into exhaust suction bag-type dust collector, then providing the resultant product into spiral conveyor machine, introducing the resultant product into mixed fuel compartment, measuring the resultant product, carrying out material pumping process, collecting the resultant product and purifying exhaust gas through chimney.    USE - Preparation of cement rotary kiln process mixed fuel (claimed).    ADVANTAGE - The cement rotary kiln is processed using the mixed fuel with reduced fuel consumption.    DETAILED DESCRIPTION - Preparation of cement rotary kiln process mixed fuel involves crushing stored rice hull through a belt metering scale into less than 0.8 mm fine rice hull powder, then crushing stored anthracite as raw coal into 0.08 mm through square hole sieve of less than 1%, introducing the crushed product into discharge tube of coal mill system, providing the resultant product into exhaust suction bag-type dust collector, then providing the resultant product into spiral conveyor machine or rigid impeller feeding machine, then introducing the resultant product into mixed fuel compartment, measuring the resultant product using two rotor measuring scale, then providing the resultant product into double air lock impeller, then introducing the resultant product into decomposing furnace, carrying out material pumping process, collecting the resultant product and purifying exhaust gas through chimney.
NOVELTY - The utility model claims a one vacuum-heated high temperature high pressure method animal corpse treatment device, comprise the high temperature high pressure tank, heating system, the material vehicle, vacuum device, a condensing recovery system, gas filtering system, a drain system, extruding and crushing device, automatic control system, the rear device is in an animal body, for animal corpse automatic organization set a harmless treatment, at the same time, the device further comprises a high efficiency, environment-friendly, energy-saving, convenient to use and so on.
NOVELTY - This utility new type relates to organic waste treatment technology field, especially relates to a waste organic bio-safety one, upper upper comprise upper feeding device, sieving device, a material pre-heating device, sterilizing and deodorizing device and temperature mix device, sterilizing and deodorizing device in turn connecting of seal set with heating device, cooling mix device set with steam exit, a steam exit seal connected material pre-heating device, reducing the mix device set with strain accessories entrance. This utility new type by using afterheat of cooling time for a pre-heating material, saves energy source and improves efficiency, and the whole processing process is proceeding in a closed device is not in contact with the outside, which will not cause new environmental pollution of waste organic matter by high temperature sterilizing and deodorizing process, a strain for fermentation to form organic fertilizer, and small volume, it is movable, not limited by the limit, compare is suitable for domestic cultivation base of dispersion.
NOVELTY - A one pyrogenation gastification furnace for life garbage preheating device, comprise driving device, a screw pole and an outer cylinder, a driving device and a driving connecting rod, a screw rod is rotatably set in the interior of said outer cylinder, and a screw and the seal assembly at the connecting of said outer cylinder, wherein the outer cylinder of the inner wall a. with a hot layer and heat preservation layer, a heat preservation layer on the inner wall of a. the outer cylinder and a heating layer, a screw and a heating layer form pre-heating room. One hand, it can make the bacteria of garbage, the more important is to the lower one of waste high temperature cracking step as preparation, or else, directly entering into from the feeding high temperature cracking to produce other side, does not reach to the expected effect of the patent is suitable for pyrogenation gastification furnace for life garbage, the valid device in oxygen-deficient environment, seal property is good, the pre-heating effect is good, the hot energy consumption is low, the structure is simple, the use is convenient to safety of use.
NOVELTY - One a garbage hot cracking machine, include feeding device further comprise a pre-heating device, high temperature cracking device and controller, pre-heating device of a first driving device with the first driving connecting rod, the first screw is rotatably set inside of first cylinder, the inner wall of first cylinder. first heating layer and a first insulating layer, high temperature cracking device of second driving device and the second driving connecting rod, second screw rod can be rotatably set in the inner of second charging barrel, the inner wall of second charging barrel a. second hot layer and the second insulating layer, the second insulating layer on the inner wall. second material cylinder and the second of the hot layer, second screw and the second emitting layer forming hot cracking area, first driving device, second driving device, first heating layer and second luminous layer a hot electric connect with the controller. This utility new type has high leak tightness, good heating effect, environmental protection and no discharge, continuous operation and working efficiency is high and so on.
NOVELTY - This utility new type claims a preventing and controlling one second dioxin discharge of pyrogenation gastification furnace for life garbage pyrolysis gasifying a municipal system, comprise the hot dry pneuma in furnace, a gas purification system, an air storage tank, a pneuma unit using tail pneuma and purification device, a hot dry pneuma for furnace up from upper to lower in turn with upper section pneuma. exit, entrance and lower section pneuma exit, hot pyrolysis gasifying furnace of upper section pneuma exit and lower section pneuma exit with the gas purification system of entrance connecting, a gas purification system of exit with the pneuma of entrance connecting tank, exit of pneuma storage tank is connected with the fuel gas entrance of pneuma unit using connecting, using tail pneuma entrance of tail pneuma exit and the tail pneuma purification device of pneuma connecting unit, and finally by the tail pneuma exit discharge of tail pneuma purification device. This utility new type through a gas purification system and. tail pneuma purification device is composed of multi-level purification structure for the pyrolysis pneuma and tail pneuma purification process, to the utmost extent in pyrolysis pneuma and removing tail pneuma of dioxin, pneuma tail discharge of the content in a level of dioxin is better than current European standard is more than 70%.
NOVELTY - This utility new type relates to a one pressure coupling type biomass pyrolysis system, furnace top high temperature synthesis pneuma. exit, the middle. two side feeding opening, the lower part. multi-microwave entrance and plasma torch interface at the bottom with a slag discharging port., microwave entrance and plasma torch interface of pyrolysis furnace are using multi-layer annular uniformity intervals, plasma torch in a microwave entrance interface, pulse feeding system with the pyrolysis furnace feed port and. feeding controller is connected with a switch control, pyrolysis furnace top synthesis pneuma exit is connected with the cyclone separator, the pyrolysis furnace bottom slag with the slag lock is connected with cyclone separator and ash lock is connected with the cyclone separator and the cooling device, the cooling device and the purification device. Pyrolysis furnace using pressing operation, a single large ability and the subsequent compressor without adding in the process and greatly saves compression ', reduces system energy consumption. Generating a synthetic pneuma tar-free in the subsequent purification process is simple and has no environment pollution.
NOVELTY - Movable coal synthesis pneuma methanation catalyst test platform, which can include the container in the transportation of a conversion and purification of gas and gas methanation section, a conversion gas purification part and include sulphur-resisting water coal conversion device, temperature in zinc oxide desulfurizing device, pneuma water separating device and NaOH and 5A molecular sieve column decarburization device, gas methanation is triple-section methanation reactor device, the working flow is as follows: 1. water coal sulphur conversion device in the coal hydrogen to carbon monoxide ratio is proper value, 2, in temperature zinc oxide desulfurization device the sulphur content is less than 0.2 ppm, 3, pneuma water separating device of separated water in coal, 4, NaOH and 5A molecular sieve column removing device removing less than 20 ppm, 5, triple-section methanation reactor a coal methanation reaction, the platform for testing the pneuma source condition of a best methanation reaction condition is suitable for different raw material pneuma components, different operation condition, test of different catalyst can test methanation process, operation parameter and catalyst property.
NOVELTY - Removing natural gas drier belongs to natural gas purifying device, comprise tank body, dryer, as technology plan of this utility new type, a drier in the top of the tank body, a dryer set with outer cover, the bottom of dryer set with natural gas pipeline, gas pipeline and two end lower part inside tank body set with a hot tracing device, tank body front end set with a human hole, the bottom set with a drain outlet. This utility new type through said technology solution, the beneficial effects: a carboxylic acid the purification drying process of natural gas, which simplifies the purification drying device, saves the production cost, so as to simplify the production process, the production efficiency, reduces the production cost.
NOVELTY - This utility new type claims a one energy-saving marsh gas fermentation tank, comprise inner layer body and the outer layer body is composed of fermentation tank, the inner tank body of middle part is a cylindrical tank body, the top part is the top and the bottom of the conical tank bottom form a sealed tank body, upper layer semi-sphere top in rotating connecting with one foldable and rotatable tank cover, semi-spherical tank top body extending to the inner bottom of the tank body with one three-level machinery stirring mechanism, the inner layer body and the outer layer tank body set with a heat preservation material layer and multi-level constant temperature heating tube, the inner conical tank bottom tank body and the outer tank body lower part is composed of a space set with circulation jet auxiliary stirring device, jet circulation auxiliary stirring device with the marsh gas circulation mechanism is connected, the bottom of the fermentation tank body set with sludge outlet, side wall of the fermentation tank body set with a biogas outlet and gas exit. This utility new type makes full use of solar energy and marsh gas self-heating, which greatly reduces the energy consumption to realize constant temperature, is suitable for large-scale popularization and use.
NOVELTY - This utility new type claims a one interlayer marsh gas tank, include with an inner cavity of tank body and tank body of adjacent water pressure, a tank body upper part of the inner cavity of lower part of the inner cavity of the pneuma room, the tank body of fermentation room, the tank body set with upper wall of the feeding tube, a discharge hole and gas-guide tube, tank body and water pressure room connected with the fermentation is composed of the inner wall and the outer wall of anti-leaking layer. the two layer wall. This utility new type of marsh gas tank. three-layer interlayer wall, plastic thin film or polypropylene fibre waterproof cloth. in the interlayer of the inner and outer wall of the middle can prevent the produce, use and gas storage marsh gas in process and improves the air tightness and use life of the marsh gas tank, and the solution is simple, it is easy to carry out.
NOVELTY - This utility new type movable top cover of marsh gas pool, upper pool body and comprise a top cover, a tank body set with a feeding tube and a discharging tube, a tank body side inner wall. sliding device, said sliding top cover and seal connecting device. A sliding device comprise vertical. limit the upward of the maximum displacement of upper inner wall and can slide along the sliding groove of the sliding block, a lifting block through the inner wall of tank body. upper end of limiting block. Said top cover is soft bag. A soft bag of multi-layer plastic film. This utility new type marsh gas tank of top cover by multiple layers of thin film, and the top cover and the upper lower moving of sliding seal connecting device, the top cover can pool with biogas pneuma amount to move up and down, made of movable top cover sealing is good, and the structure is simple, the manufacturing cost is low, the weight is light, wide adaptability.
NOVELTY - A basic fertilizer comprises mixing Selenastrum, trotters, animal bones, fish guts, fish belly, poultry manure, fish intestines, animal meat, fish bone, fish scales, crab scales, shrimp scales, animal hair, animal nails, and animal horn into cylinder, adding water and fermentation agent, maintaining humidity at 60-70%, sealing, and fermenting.    USE - Method for preparing basic fertilizer (claimed).    ADVANTAGE - The method is simple.
NOVELTY - Processing method of kitchen waste comprises collecting kitchen waste and microbial culture, mixing, fermenting and standing. Microbial culture includes yeast.    USE - Method for processing kitchen waste used in preparing organic fertilizer (claimed).    ADVANTAGE - The method improves chlorophyll content and crop yield.
NOVELTY - Preparation of pigeon dung organic manure comprises taking 1 kg pigeon manure, diluting with water, placing in heating tank, heating to 40 degrees C, stirring for 30 minutes, and standing for 15 to 20 days while stirring for 10 minutes/day.    USE - Method for preparing pigeon dung organic manure (claimed).
NOVELTY - An organic fertilizer product is produced by anaerobically fermenting livestock excrement and anaerobic microbial inoculum in marsh gas tank at 60-75 degrees C and 1.4-1.6 atm for 15-20 days.    USE - Method for producing organic fertilizer product (claimed).
NOVELTY - This utility new type claims a one grading pneumatic stirring and fermenting device, include fermentation and multi-level fermentation device, biogas residue and biogas liquid tank, fermenting control system, gas circulation system and material circulation system, fermentation tank upper body set with an air outlet, a drain outlet and a slag, each level fermentation device both comprise bracket, the heater part and is set on the heater of the top part of the fermentation container top bracket, upper container set with biogas fermentation vents, in the fermentation container set with bottom blowing compressed gas nozzle and connecting the compression of upper gas nozzle and the stirring blade bottom, upper side wall of the fermentation tank body is connected with a bottom blowing compressed gas conveying branch pipeline, the raw material conveying branch pipeline and material circulation pipeline, upper circulation pipeline is connected with the raw material raw material circulation pump, fermentation control system include fermentation controller, operation button, a display screen, a pressure gauge and temperature sensor. The utility model uses the valid space of the fermentation tank, the heating uniformity, the raw material reaction completely, the fermentation efficiency is high, energy-saving and environment-friendly, the practicability is strong.
NOVELTY - Preparation of double-seaweed fertilizer comprises separately squeezing and dehydrating green algae and brown algae, cutting, crushing, sieving, adding water, soaking and thawing to obtain paste; adding into reaction kettle, adding water and complex enzyme, performing enzymolysis, adding seaweed polysaccharide-degrading enzyme, adjusting pH, filtering and centrifugally separating to obtain enzymolysis liquid and seaweed residue; and drying and granulating seaweed residue to obtain fertilizer, performing ultrafiltration of enzymolysis liquid and freeze-drying to obtain fertilizer additive.    USE - Method for preparing double-seaweed fertilizer (claimed).    ADVANTAGE - The method improves seaweed extraction and degradation rate, and fully uses resources.    DETAILED DESCRIPTION - Preparation of double-seaweed fertilizer comprises:    (A) separately squeezing and dehydrating green algae and brown algae until water content is 50-60%, thawing for 2-3 times, cutting to 2-3 cm, crushing, sieving, adding 5-8 times water, soaking and thawing 2-3 times to obtain green algae paste and brown algae paste;    (B) adding green algae paste and brown algae paste into reaction kettle at mass ratio of 1:2-2:1, adding 10-15 times by weight water and 2-3 wt.% complex enzyme, performing enzymolysis at 40-55 degrees C and pH of 3.5-4.5 for 1.5-2 hours, adding 1-2 wt.% seaweed polysaccharide-degrading enzyme, adjusting pH to 5.5-6.5, filtering and centrifugally separating to obtain enzymolysis liquid and seaweed residue; and    (C) drying and granulating seaweed residue to obtain organic fertilizer, performing ultrafiltration of enzymolysis liquid and freeze-drying to obtain polysaccharide fertilizer additive.
NOVELTY - Cultivation of Chinese medicine residue comprises piling first stack of Chinese medicine residue, spraying with water to maintain humidity at 40-50%, covering with plastic film, carrying out fermentation, piling second stack of Chinese medicine residue, maintaining humidity at 40-50%, mixing fermentation strains and second pile of Chinese medicine residue at weight ratio of 800-1200:1, covering with plastic film, turning dregs and fermenting for 2 months.    USE - Method for cultivating Chinese medicine residue (claimed) for nursery stock.    ADVANTAGE - The method is energy-saving.
NOVELTY - Organic flower fertilizer comprises crop straw or husk, cassava residue and microbial fermentation agent at weight ratio of 20-30:70-80:0.1-1 where microbial fermentation agent is thermophilic bacteria and crop straw is rice straw, wheat straw, maize straw, canola straw, cotton straw, tobacco straw or sugar beet straw.    USE - Organic flower fertilizer.    ADVANTAGE - The product is stable and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic flower fertilizer comprising mixing crop straw or husk with particle diameter of three quarters mm, cassava residue and microbial fermentation agent, adjusting humidity to 50-60% and carrying out solid-state fermentation for 24 hours.
NOVELTY - Preparation of green manure comprises placing bone meal and plant ash into cylinder or tank, adding 2.5 kg water, soaking, adding 1 kg vegetable leaf or leaves and grass, heating at 35 degrees C and decomposing for 20-30 days.    USE - Method for preparing green manure (claimed).
NOVELTY - Preparation of nitrogen fertilizer comprises placing mycophenolate borers, unedible beans, peanuts, melon seeds, castor, vegetable leaves, hulls, fruit peel, pigeon droppings and expired milk in small jar, filling with water, sealing, fermenting, heating at 45 degrees C for 3-6 months and decomposing.    USE - Method for preparing nitrogen fertilizer (claimed).
NOVELTY - Preparation of organic fertilizer comprises mixing mushroom, manure and organic solid waste, adding compound fertilizer and aerobic fermenting.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The method is eco-friendly and inexpensive.
NOVELTY - Preparation of humic acid ammonium phosphate by mixing 1 kg biogas sludge compost and 0.05 kg phosphate rock, piling at thickness of 3-5 cm, applying paste and soil, sealing for 40 days, adding 1 kg humic acid fertilizer and 0.05 kg ammonia and sealing for 8-10 days.    USE - Method for preparing humic acid ammonium phosphate (claimed).
NOVELTY - Preparation of high temperature organic fertilizer comprises mixing manure and fresh grass weeds at mass ratio of 2:1, adding water, stirring, piling, heating at 30-45 degrees C, and sealing with plastic film for 20-25 days.    USE - Method for preparing high temperature organic fertilizer (claimed).
NOVELTY - Preparing fruit organic fertilizer comprises soil covering cement/tile compost tank, rotting fruit, seed, bark, flower, and fertilizer more than 50 cm, where the layer of organic material is not more than 10-15 cm intervals, covering soil with organic material, composting for greater than or equal to 12-24 months before the end of maturity, adding a small amount of ferrous sulfate and superphosphate, and keeping the soil moist without overdoing the watering to prevent nutrient loss.    USE - Method for preparing fruit organic fertilizer (claimed).
NOVELTY - Manufacturing plant nutrient soil includes spreading sludge, naturally drying and draining on the surface; polishing slag and sludge, spraying and grinding up the sludge, and mixing and aerating; spraying quicklime on the mixture; fermenting a bacteria decay of the mixture to produce rot compound, stirring, and aerating; covering a plastic thin film layer, a mineral wool layer and a plastic film layer; composting, mixing and aerating; and further composting, mixing, and aerating; and continuing composting to obtain the plant nutrient soil.    USE - Method for manufacturing plant nutrient soil (claimed).    DETAILED DESCRIPTION - Manufacturing plant nutrient soil comprises:    (A) spreading sludge with 60-80% water content, then throwing mud on each 1.5 kg sludge per kg polyacrylamide, naturally drying for one week and draining on the surface;    (B) polishing slag and sludge, spraying and grinding up the sludge, and then mixing and aerating;    (C) spraying quicklime on the mixture of 1-4 kg/m2 lime;    (D) fermenting a bacteria decay of the mixture to produce rot compound, stirring, and aerating;    (E) covering plastic thin film layer, a mineral wool layer and a plastic film layer at 60-65 degrees C;    (F) composting at 25-42 degrees C for 50-35 days, or at 10-25 degrees C for 75-50 days, mixing and aerating;    (G) further composting at 25-42 degrees C needs 50-35 days, and at 10-25 degrees C for 75-50 days, and mixing, and aerating; and    (H) continuing composting to obtain the plant nutrient soil.
NOVELTY - Preparation of potash fertilizer comprises mixing residual tea, rice water and swill at ratio of 1:1:1, mixing with water or milk, washing bottles of water, quickly warming at 40-45 degrees C, stirring, heating for 30 minutes, and fermenting for 2-5 days.    USE - Method of potash fertilizer preparation (claimed).
NOVELTY - Preparation of organic fertilizer comprises in cement/ceramic tile composting tank, composting fallen leaves, covering soil of more than 40 cm, aging for 6-12 months, decomposing, adding ferrous sulfate and calcium superphosphate, and maintaining wet soil.    USE - Method of preparation of organic fertilizer (claimed).
NOVELTY - Producing organic fertilizer comprises mixing uniformly 25 kg calcium superphosphate, 25 kg ammonium sulfate, 1.25 kg zinc sulfate, 7.5 kg potassium chloride, 500 kg human excreta, 250 kg pig manure, and 1000 kg fine dry soil, stacking, sealing with plastic film, and administering after 25-30 days.    USE - Method for producing organic fertilizer (claimed).
NOVELTY - A nanocow manure is prepared by mixing cattle manure and cattle manure fermented bacteria at a mass ratio of 1:1 to obtain mixed fertilizer, placing the mixed fertilizer in fermenting tank, and fermenting for 40 hours; adjusting water content in mixed fertilizer, drying, and grinding into granule; ultrasonically vibrating mixed fertilizer, and adding nanocalcium carbonate, nanotitanium dioxide, and nanocarbon; and mixing with corn, clear water, fructus momordicae powder and earthworm.    USE - Method for preparation of nanocow manure (claimed).    DETAILED DESCRIPTION - Preparation of nanocow manure comprises (A) mixing cattle manure and cattle manure fermented bacteria at a mass ratio of 1:1 to obtain mixed fertilizer (a), placing the mixed fertilizer (a) in fermenting tank, and fermenting for 40 hours; (B) adjusting water content in mixed fertilizer (a) to less than 2%; (C) drying the mixed fertilizer (a), grinding into granule, and mixing mixed fertilizer (a) powder and water at a ratio of 1:2 to obtain mixed fertilizer (b); (D) ultrasonically vibrating mixed fertilizer (b), adding nanocalcium carbonate, nanotitanium dioxide, and nanocarbon to obtain mixed fertilizer (c); (E) mixing with corn, clear water, fructus momordicae powder and earthworm to obtain mixed fertilizer (d); (F) drying mixed fertilizer (d) at 30-35 degrees C for 45-50 hours, and removing earthworm compost in (d) to obtain final fertilizer.
NOVELTY - A composite microorganism fertilizer comprises neomycin R, mixture of slag and ash, Bacillus subtilis HL259, and B. megaterium.    USE - Composite microorganism fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer.
NOVELTY - A tobacco seedling fertilizer formulation comprises 20 mass% inorganic phosphorus, 10 mass% inorganic potassium, 25 mass% organic nitrogen, 20 mass% biological strain, 0.1 mass% alcohol, and 1 mass% trace element.    USE - Tobacco seedling fertilizer formulation used for loosening soil and preventing soil insect pests.    ADVANTAGE - The fertilizer has long-term fertilizing effect and improved utilization rate, eliminates soil compaction, and contains inorganic elements that are easily absorbed by crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the tobacco seedling fertilizer, comprising:    (A) adding inorganic phosphorus and inorganic potassium and uniformly mixing to obtain inorganic fertilizer;    (B) adding organic nitrogen into the inorganic fertilizer and mixing;    (C) adding fertilizer mixture with biological strain, then adding alcohol and trace elements, mixing and agitating to obtain nutrient-rich composite fertilizer; and    (D) granulating the composite fertilizer and packaging.
NOVELTY - Human excrement is composted to prepare fertilizer by adjusting water content of human excrement to 65-68%, then mixing with auxiliary material to obtain compost, and performing rapid high temperature fermentation at 120-130 degrees C with stirring for 2 hours to obtain harmless excrement; adding harmless excrement with high temperature fermentation strain and composite enzyme and fermenting at 95-98 degrees C for 5-8 days; and adding liquid film modifier into the fermented material at 80-90 degrees C and curing for 1-2 days to obtain solid fertilizer.    USE - Process for composting human excrement to prepare fertilizer (claimed).    ADVANTAGE - The method requires small floor area and has short composting period (6-8 days). The production period is shortened by 66%. The obtained fertilizer product conforms to People's Republic of China Agricultural Industry standard for Organic Fertilizer NY525-2012 and Biological Organic Fertilizer NY884-2012 Standard.    DETAILED DESCRIPTION - Composting human excrement to prepare fertilizer comprises:    (A) adjusting water content of human excrement to 65-68%, then mixing with auxiliary material to obtain compost, and performing rapid high temperature fermentation at 120-130 degrees C with stirring for 2 hours to obtain harmless excrement;    (B) adding harmless excrement with high temperature fermentation strain and composite enzyme, and fermenting at 95-98 degrees C for 5-8 days;    (C) adding liquid film modifier into the fermented material at 80-90 degrees C, uniformly stirring for 3-5 minutes, and curing for 1-2 days to obtain solid fertilizer, where the liquid film modifier is 0.001 mol/L acetic acid, propionic acid, hydrochloric acid, sulfuric acid, nitric acid, or phosphoric acid; and    (D) crushing solid fertilizer, sieving and packaging to obtain the finished product fertilizer.
NOVELTY - An onion planting fertilizer comprises organic fertilizer, fermented tobacco stems, urea, diamine, and potassium sulfate.    USE - Onion planting fertilizer.    ADVANTAGE - The fertilizer provides adequate nutrients for onions which improves yield and increases its pest-resistant capacity, and has 1.59% nitrogen content, 2.68% phosphorus content, 2.76% potassium content, 60% organic matter content and 23% moisture content in its organic fertilizer raw material, and 46% urea nitrogen content, 18% diammonium nitrogen content, 46% phosphorus content, 50% potassium content and 20% sulfur content in its fermented tobacco stems raw material.
NOVELTY - Fertilizer comprises organic fertilizer, urea, diammonium, potassium sulfate, and fermented tobacco stalk; prepared by uniformly mixing.    USE - Fertilizer used for planting leeks (claimed).    ADVANTAGE - The fertilizer provides adequate nutrients, repels maggots, increase resistance to pests and diseases, and improves yield.
NOVELTY - A special organic fertilizer comprises organic solid waste, gypsum and desulfurized gypsum pulverized coal ash.    USE - Special organic fertilizer used for saline alkali soil (claimed).    ADVANTAGE - The fertilizer is environment-friendly and utilizes waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special organic fertilizer comprising mixing organic solid waste, gypsum and desulfurized gypsum pulverized coal ash.
NOVELTY - An alkyl salicylate (I) is reacted with carboxylic acid or carboxylic acid salt (II) in presence of base and solvent, to obtain carboxylate (III) and salicylate (IV).    USE - Preparation of carboxylate (claimed).    ADVANTAGE - The method economically and environmentally-friendly enables preparation of carboxylate having reduced toxicity using readily available reagents.    DETAILED DESCRIPTION - An alkyl salicylate of formula (I) is reacted with carboxylic acid or carboxylic acid salt of formula (II) in presence of base and solvent, to obtain carboxylate of formula (III) and salicylate of formula (IV).    M=H or metal ion;    R1=1-20C alkyl;and    R2=6-20C aryl or 1-20C alkyl.
NOVELTY - Preparation of meclizine comprises reacting piperazine and chlorobenzhydryl chloride and Methyl benzyl chloride to obtain meclozine.    USE - Method for preparing meclozine (claimed).    ADVANTAGE - The method is non-toxic, environmental-friendly, and reduces waste discharge.
NOVELTY - Benfotiamine (I) is synthesized by taking vitamin B1 (II) and polyphosphoric acid, hydrolyzing, extracting, precipitating in organic solvent, pulping with water, adding alkali to adjust pH, adding benzoyl chloride, reacting, filtering, adjusting pH value to 3.5-4.0 to precipitate, separating, and drying.    USE - Method for synthesizing benfotiamine (claimed).    ADVANTAGE - The environment-friendly synthesis has high yield, high product purity and simple operation.    DETAILED DESCRIPTION - Benfotiamine of formula (I) is synthesized by taking vitamin B1 of formula (II) and polyphosphoric acid, reacting, hydrolyzing, extracting, precipitating in organic solvent, pulping with water, adding alkali to adjust pH value, adding benzoyl chloride, reacting, filtering, adjusting pH value to 3.5-4.0 to precipitate, separating, and drying.
NOVELTY - The device has a tail pneuma purification system, a tail pneuma combustion system, and a baking treatment intervention system that comprises hoppers (1,7), a packing auger (2), drying cylinders (3,4), and tail pneuma combustion device (26). A continuous carbonization system is provided with carbonizing furnace (11), a carbon bucket (13), a tail pneuma purification system, water box (9), a spray tower (17), a cooling tower (18), dehumidifying tower (19) and air storage tank (21). The dehumidifying tower is made to enter into the air storage tank.    USE - Combined multi-joint fast biomass carbonization device.    ADVANTAGE - The pneuma liquid separation and gas-solid separation can be realized effectively. The structure of the combined multi-joint fast biomass carbonization device is simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combined multi-joint fast biomass carbonization device.    Hoppers (1,7)    Packing auger (2)    Drying cylinders (3,4)    Water box (9)    Carbonizing furnace (11)    Carbon bucket (13)    Spray tower (17)    Cooling tower (18)    Dehumidifying tower (19)    Air storage tank (21)    Tail pneuma combustion device (26)
NOVELTY - Desulfurization of industrial wastewater or domestic sewage involves adding desulfurizing agent in industrial wastewater or domestic sewage with a mass ratio of 1:2 in a coal furnace, stirring, spraying water from the spraying device to the top portion of the furnace, evenly spraying water to the surface of the furnace, heating and evaporating low-boiling point material, absorbing desulfurizing agent on the surface of coal, and desulfurizing with coal gas.    USE - Desulfurization of industrial wastewater or domestic sewage (claimed).
NOVELTY - The furnace has a furnace body installed on a bracket. A furnace cover is covered on a top part of the furnace body through a rotary engaging device. A compactor is fixed in the furnace body. A pull rod is connected with an upper end of the furnace cover. A lower part of the furnace body is connected with a fan. The top part of the furnace body is connected with a gas passage. An air inlet pipe is connected with a dust filter screen. The rotary engaging device is equipped with an upper part of a sealed gasket.    USE - Straw gasification furnace.    ADVANTAGE - The furnace has better gasification furnace sealing effect and prolonged service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification furnace.
NOVELTY - The device has a gas tube connected with a gasification furnace. An end of the gas tube is connected with an air mix device body. Another end of the gas tube is connected with a fan. An included angle is formed in the gas tube for about 20 to 70 degrees.    USE - Straw gasification furnace air mixing device.    ADVANTAGE - The device has high stability and better burning effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification furnace air mixing device.
NOVELTY - The furnace has a furnace body fixed with a bracket. A furnace cover is covered on a top part of the furnace body. A lower part of the furnace body is formed with ash ignition ports. An upper part of the furnace body is formed with a gas channel. A compactor is fixed with the furnace body and provided with a base plate and a pull rod. The base plate is horizontally placed on the furnace body. The pull rod is fixed to an upper part of the furnace cover. A pressing device is fixed on the base plate. Upper and lower parts of the base plate are movably fixed to the furnace body.    USE - Straw gasification furnace.    ADVANTAGE - The furnace body realizes complete straw combustion operation. The furnace has prolonged service life, and improves user experience degree and reduces combustion time consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace.
NOVELTY - The furnace has a furnace cover covered on a top part of a furnace body. A compactor is fixed at a lower part of the furnace body. An upper part of the furnace body is connected with a gas tube. The top part of the furnace body is connected with a heating jacket. An upper part of the heating jacket is provided with a hot tube. A lower part of the heating jacket is connected with a water tube and an indoor radiator.    USE - Straw gasification furnace.    ADVANTAGE - The furnace is environment-friendly, and has better heat preservation and gasification effect, and reduces coal resource wastage and coal resource stress defects.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a straw gasification furnace.
NOVELTY - The generator has a furnace body (1) whose inner wall is connected with a container (2). An upper part of the container is fixed with a storage hopper (5). A lower part of a cracking room (6) is fixed with an upper part of another cracking room (11). A lower part of the latter cracking room is fixed with an ash bucket (13). An upper side of the ash bucket is connected with a fuel gas exit (7). The former cracking room is connected with a water jacket (3) and an inner part of the container. The water jacket is connected with the furnace body.    USE - Biomass double-section type pneumatic generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass double-section type pneumatic generator.    Furnace body (1)    Container (2)    Water jacket (3)    Storage hopper (5)    Cracking rooms (6, 11)    Fuel gas exit (7)    Ash bucket (13)
NOVELTY - The furnace has a processor connected with an information feedback unit, a distributor controller, a gasification flow controller, an air flow controller and an ignition device controller. A controller is connected with a flame lighter that is connected with the gasification flow controller. The gasification flow controller is connected with a gasification fan. The air flow controller is connected with a combustion-supporting air blower. The information feedback unit is connected with a biomass gasification system, a biomass gas burner and an application system.    USE - Double-cracking integrated biomass furnace.    ADVANTAGE - The furnace realizes gasifying and burning operations in a complete manner so as to increase thermal range for improving energy utilization rate. The furnace improves pneumatic waste water discharging efficiency so as to ensure better cleaning effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a double-cracking integrated biomass furnace.'(Drawing includes non-English language text)'
NOVELTY - Energy saving gas oil comprises methanol, water and triethanolamine.    USE - Used as gas oil.    ADVANTAGE - The gas oil is smoke-free, coke-deposition-free and does not produce toxic gases when burnt.
NOVELTY - Methanol diesel additive comprises 10-15% methyl tertiary butyl ether, 5-10% n-octane, 15-20% isopropanol, 25-30% n-butanol, and 10-35% methyl cyclopentane.    USE - Used as methanol diesel additive.    ADVANTAGE - The additive solves the problem of corrosion, swellability, starting under cold condition, heat resistance, decreased power, fluidity, emulsification and other technical problems.
NOVELTY - Methanol-straight-run gasoline cosolvent comprises first liquid comprising 20-35 wt.% toluene, 35-55 wt.% xylene and 25-35 wt.% naphthalene, and second liquid comprising 20-50 wt.% lauryl alcohol, 20-50 wt.% n-octanol, 0-30 wt.% glyceryl monostearate, 0-40 wt.% oleic acid and 0-20 wt.% biodiesel.    USE - The cosolvent is useful in methanol-straight-run gasoline system (claimed).    ADVANTAGE - The cosolvent has good dissolving effect, resistance to aqueous phase separation and has good performance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the methanol-straight-run gasoline cosolvent, comprising mixing toluene, xylene and naphthalene to obtain first liquid, and mixing lauryl alcohol, n-octanol, glyceryl monostearate, oleic acid and biodiesel to obtain second liquid; and    (2) use of the cosolvent in methanol-straight-run gasoline system.    .
NOVELTY - Methanol-gasoline additive is prepared by mixing 0-34 wt.% lower alcohol, 0-22 wt.% soluble ester, 0-43 wt.% alkyl ether, and 0-1 wt.% benzotriazole.    USE - As methanol-gasoline additive.    ADVANTAGE - The methanol-gasoline additive is suitable for large scale production, cleans and starts the vehicle fast, has e.g. no carbon, strong power, latent heat of vaporization, catalytic combustion speed, high auto-ignition temperature, and high octane, and protects the vehicle's rubber and metal parts.
NOVELTY - Synthesis of straw fuel block comprises collecting crop straw; screening and classifying; removing impurity; pulverizing to obtain crop straw powder; carbonizing; granulating to obtain granular charcoal; mixing with millet mixture; extruding via spiral continuous extrusion machine; molding at certain pressure and temperature to obtain fuel block; packaging; and drying to obtain synthetic straw fuel block with straw carbon powder content of more than 80% and millet mixture content of 20%.    USE - Synthesis of straw fuel block.    ADVANTAGE - The method solves problem of large-scale storage and transportation of crop straw, and produces straw fuel block that is easy to use, has high thermal efficiency and high flammability, can replace coal, and enable farmers to increase economic efficiency while increasing farmers' income. The straw fuel block is non-polluting, renewable, and environment friendly.
NOVELTY - Fuel composition comprises 65-75 pts. wt. straw briquetting fuel, 8-21.7 pts. wt. dry sludge organic cellulose, and 7-13.3 pts. wt. dry sludge ash. The straw briquetting fuel is prepared by subjecting crop straw, sugar crops, starch crops, oil crops waste, forestry, and wood processing wastes into urban garbage classification processing.    USE - Fuel composition.    ADVANTAGE - The fuel composition solves problem that renewable coal may not be enough to overcome existing biomass pellet fuel requirement. It increases productivity, reduces cost, and is easy to produce, safe, energy saving, and environment friendly.
NOVELTY - Pulverized coal boiler bio-particle matches are prepared by subjecting sulfated tungsten oxide zirconia (SWZ) catalyst and biomass into endothermic reaction and flameout time, and waterproof coating.    USE - Pulverized coal boiler bio-particle matches.    ADVANTAGE - The pulverized coal boiler bio-particle matches can be ignited at 0 degrees C, have high calorific value, and produce strong flame that can quickly ignite pulverized coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for preparing pulverized coal boiler bio-particle matches (Drawing includes non-English language text).
NOVELTY - Biofuel comprises 70-80 pts. wt. biomass fuel briquettes, 10-15 pts. wt. coal, 6-7 pts. wt. hexamethylene tetramine, 3-5 pts. wt. ethanol, and 1-3 pts. wt. stearic acid.    USE - Biofuel.    ADVANTAGE - The biofuel is environment-friendly and energy-saving. It has high carbon content and oxygen content, thus improving combustion heat value of fuel. It has adjustable composition to effectively reduce volatiles generated by initial combustion, thus providing environmental protection.
NOVELTY - Method for brewing technology of vegetable liquid, involves taking vegetable from stacking field or storehouse, air heat-preservation of vegetable, fermenting the vegetable, crushing, stirring, filtering, heating and sterilizing, cleaning, drying the vegetable, adding vegetable to spice, then adding clove, star anise, and mint and crushing into fine slurry, drying, fermenting, adding slurry raw material, yeast, and water, processing, stirring, fermenting, adding mash raw materials, and heating and distilling the mash raw materials, and filtering mash liquid.    USE - The method is useful for brewing technology of vegetable liquid used as feed or biogas raw material, and for producing ethanol and fuel (all claimed).    ADVANTAGE - The method is energy-saving and environment-friendly.    DETAILED DESCRIPTION - Method for brewing technology of vegetable liquid, involves taking vegetable from stacking field or storehouse, air heat-preservation of vegetable, fermenting the vegetable, crushing, stirring, filtering, heating and sterilizing, cleaning, drying the vegetable, adding vegetable to spice in ratio of 5-4:0.2-0.1, then adding clove, star anise, and mint, crushing components into fine slurry, drying, fermenting, adding slurry raw material, yeast, and water in ratio of 100:0.8-1:280-260, processing at temperature of more than 30 degrees C, stirring, fermenting for 9 days, adding mash raw materials, and heating and distilling the mash raw materials to obtain mash residues and mash liquid, and filtering mash liquid.
NOVELTY - Method for producing anaerobic methane with improved efficiency involves using short chain fatty acid as donor, and magnetite as carrier, performing anaerobic fermentation under culture condition, rapidly degrading short chain fatty acid so as to improve production of oxidized methane.    USE - The method is useful for producing anaerobic methane with improved efficiency (claimed).
NOVELTY - Peat activation involves drying peat at 140-190 degrees C for 4-20 minutes under pressure of 0.6-1.6megapascal in the steam explosion tank to obtain activated blast instant peat. Anaerobic fermentation of obtained product is carried out by adding 10-90wt.% of anaerobic activated sludge at 30-50 degrees C for 7-30 days to obtain methane gas and then the content of methane in biogas is determined, where pH of solution is adjusted to 6.5-7.5 and solid-liquid ratio is adjusted to 1:(5-20)g/mL.    USE - Method for activating peat (claimed).    ADVANTAGE - The method enables activation of peat in an economic manner.
NOVELTY - Pre-treating corn at low temperature to produce fuel ethanol, involves (a) crushing corn into powder, and sieving crushed corn through 40 mesh sieve, (b) formulating the crushed corn into slurry after grinding, (c) adding protease, amylase, and antibacterial agent to the slurry, adjusting pH of mixture to 4.5, and pretreating the mixture, and (d) rapid cooling the mixture, adding glucoamylase, yeast, and nutrients into the mixture, and fermenting the mixture.    USE - The method is useful for pre-treating corn at low temperature to produce fuel ethanol (claimed).    ADVANTAGE - The method is carried at low temperature, and saves 35% of steam.
NOVELTY - Ethanol fuel preparation involves mixing raw material, lime and water in ratio of 5-7:0.5-0.7:7-9 and then soaking obtained product in alkali solution for 10-12 days. The obtained product is crushed and then crushed product is added to pulping machine to obtain pulp. The obtained product is mixed with alcohol and water in ratio of 100:0.9-1.1:280-300. The obtained product is added to anaerobic fermentation tank for 11-13 days and then tank is sealed. The product is stirred once after 3 days. Pale or dark brown fermentation product is obtained.    USE - Method for preparing ethanol fuel (claimed).    ADVANTAGE - The method enables preparation of ethanol fuel of high quality in energy-saving and eco-friendly manner.    DETAILED DESCRIPTION - Ethanol fuel preparation involves mixing raw material, lime and water in ratio of 5-7:0.5-0.7:7-9 and then soaking obtained product in alkali solution for 10-12 days. The obtained product is crushed and then crushed product is added to pulping machine to obtain pulp. The obtained product is mixed with alcohol and water in ratio of 100:0.9-1.1:280-300. The obtained product is added to anaerobic fermentation tank for 11-13 days and then tank is sealed. The product is stirred once after 3 days. Pale or dark brown fermentation product is obtained. Distillation of obtained product is carried out. The obtained product is filtered and the remaining residue is refermented to obtain biogas. The obtained product is redistilled to obtain ethanol fermentation liquid. The obtained product is blended with fuel, oxidizer and inert gas in proportion of 2-3:1-2:0.4-0.5:0.01-0.02 and then obtained product is pumped into standard bottles to obtain desired product.
NOVELTY - This utility new type provided straw gasification cooking heating system, belonging to the family of small cooking heating device technology field, mainly solves the problem that the existing technology high tar content, the multi-water, waste gas can not remove the cooker and boiler ignition failure or the problem that the phenomenon of breaking. Include gasification furnace, a purifier, a cooker, hot water boiler, fuel gas supply pipeline system and air distribution system, wherein it further comprise the. the gas tube up to the gasification furnace of a pipeline between the waste discharge tube of waste pneuma pneuma valve and the small gas storage barrel and the discharging water purifier is equipped with condensed water of condensed water of drain valve. This utility new type ignition easy, without tar, it is not easy to cut.
NOVELTY - This utility new type relates to a new biomass pneuma by one guide pneuma furnace combustion device, comprise air inlet tube (1), the oil water outlet (2), gas-guide tube (4), a gas distribution box (5), wherein the air inlet tube (1) is connected with the gas distribution tank (5) connect through screw thread, a cooking range (3) is installed on the guide pneuma tube (4) upper, gas-guide tube (4) is installed on the gas distribution tank (5) one side of upper gas distribution tank (5) bottom part set with upper oil water outlet (2). With the existing technology, the device can be valid problem of water vapour and tar problem in combustion pneuma, preventing gas channel clogging biomass gasification furnace to influence the normal working. This utility new type is the best assorted device of multi-stove biomass gasification furnace.
NOVELTY - The furnace has a gas tube (6) connected with a gasification chamber (3) that is matched with a fuel gas furnace body (28). A mix gas filtering system is provided with a smoke exhaust system. An upper part of the smoke exhaust system is fixed with the fuel gas furnace body that is fixed with a heating system. An upper part of the fuel gas furnace body is connected with the gas tube that is fixed with the mix gas filtering system. A mix filter device (15) is connected with a mix device (7) that is connected with a storage device (12) and a mix gas filtering device (13).    USE - Energy-saving waste straw, firewood, edible fungi waste utilizing gasification furnace for use in a rural area.    ADVANTAGE - The furnace is inexpensive, environment-friendly and sanitary to use, and has high burning stability, better utilization rate and low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy-saving waste straw, firewood, edible fungi waste utilizing gasification furnace.    Gasification room (3)    Gas tube (6)    Mix device (7)    Storage device (12)    Mix gas filtering device (13)    Mix filter device (15)    Fuel gas furnace body (28)
NOVELTY - The battery has an anode plate (1) and a cathode plate (2) connected with each other by a proton exchange film (3). The anode plate and the proton exchange film are formed with a hydrogen channel. The cathode plate and the proton exchange film are formed with an oxygen channel. An upper part of a hydrogen inlet is connected with the anode plate and a gas exit. An oxygen inlet is provided with the cathode plate and an oxygen exit. An electro-catalyst layer (8) is formed on the anode plate. The cathode plate is connected with a battery anode end by a lead.    USE - Proton exchange fuel battery.    ADVANTAGE - The battery has better energy conversion effect, quick starting function, reliable operation, pollution-free effect and low noise.    DETAILED DESCRIPTION - The anode plate and the cathode plate are made of carbon fiber cloth and PTFE. The proton exchange film is a full-fluorine sulfonic acid type proton exchange film. The electro-catalyst layer is made of carbon-supported platinum alloy catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional perspective view of a proton exchange fuel battery.    Anode plate (1)    Cathode plate (2)    Proton exchange film (3)    Electro-catalyst layers (8, 9)    Trapezoidal flow channel (10)
NOVELTY - Decomposing fish dejection and food residue of device. No matter the current aquarium or aquarium cannot treat waste and food residue of fish, long before the fish excrement of food residue and serious pollution and aquarium fish, the fish pond and aquarium of water quality is bad, the fish is easy to sick and death. A decomposing one fish dejection and food residue of device, the comprise of the fish tank (1), upper connecting frame (2), a fish tank of said upper frame through slide way orderly connecting yeast cavity (3), cavity (4) nitrifying bacteria, lactic acid bacteria cavity (5), wherein the yeast chamber connecting one number spraying device (6), said nitrobacteria cavity connect the second spraying device (7), wherein the lactic acid bacteria cavity connecting the third spraying device (8). This utility new type used for decomposing fish dejection and food debris and water purification.
NOVELTY - Preparing fermented chicken manure comprises mixing 60% of fresh chicken manure, and 40% of rice straw powder or rice bran and wheat bran, blending into a mixed material, adding the mixed material, effective microorganism (EM) probiotic multi effect active liquid and brown sugar in a ratio of 500:1:1, diluting the obtained product with 30-40% of water, washing and spraying the diluted material into a container, adding 500 times of EM probiotic multi effect active liquid for one time and each 10 spraying, covering with a plastic film, sealing and fermenting for 1 month.    USE - The method is useful for preparing fermented chicken manure (claimed).
NOVELTY - Preparing fermented rabbit manure, comprises drying healthy fresh rabbit manure, crushing, then adding rabbit manure, effective microorganism (EM) probiotic pleiotropic active solution and brown sugar in the ratio of 200:1:1 into water, mixing, cleaning a container by spraying 500 times diluted EM probiotic pleiotropic active solution, adding the mixture into the container, once again spraying EM probiotic pleiotropic active solution until 10 cm of the container is filled, covering with a plastic film, and sealing.    USE - The method is useful for preparing fermented rabbit manure (claimed).
NOVELTY - A one garbage pyrolysis processing system, first crusher comprise in turn flows of garbage, squeezing and de-watering machine, separator, a sieving, second crusher, drying and hot cracking machine, wherein the hot cracking machine comprise in turn connected of feeding device, a pre-heating device, high temperature cracking device and discharging and cooling device. Compared with the existing technology, this utility new type of waste cracking processing system not only has simple structure, reasonable and arrange device of use easy to buy, the price is cheap, processing cost is low.
NOVELTY - This utility new type relates to one used for a continuous vertical magnetization pyrolyzer of municipal sludge, include the hopper, spiral conveying machine, a vertical pyrolyzer magnetizer, air blower and spiral ash conveying machine, a vertical top part is set with a pyrolyzer, side is provided with a decomposing gas exit, the bottom set with discharging device, a spiral material conveying machine feeding end connecting the hopper, a discharge end connecting cloth, said air blower is connected with the gas pipeline through the air magnetizer, a magnetizer rear magnetization of the combustion-supporting air into the vertical type pyrolyzer; a spiral ash conveying machine feeding end connecting outlet of discharging device. This utility new type using pyrolysis principle for sludge not only can realize high-efficient processing, and the utility model is new type structure and concise, valid to realize continuous feeding continuous discharging, the operation cost is low, processing efficiency is high.
NOVELTY - This utility new type claims a one carbon straw recovery device, a motor fixed to one end part of the top of the supporting body, a gear fixing device is connecting inside, a gear device with the motor of support body, a rotor body fixed to the other end part of the top support of the inner rotor box body is set with a rotor and high temperature carbonization device, rotor of inner rotor box body through the device with the gear connecting device feeding opening fixed on the top part of the rotor box body, a discharging rotor box body is located at the right lower part of the rotor of said rotor box body is conical rotor, ratio is 1: 20, the upper rotor is further provided with a reverse spiral rotary groove. This utility new type of straw carbon recovery device using of taper ratio is 1: 20 of conical rotor, and with a reverse spiral rotary groove. up the rotor so that the straw can be extrusion uniformity so that the prepared straw carbon powder, uniformity, and can according to need into the needed length of, at the same time, solves the problem that the farmers can not burning straw and no accumulation of.
NOVELTY - A one biomass microwave hot de-decoking device, comprise in turn connecting of microwave cracking furnace, a cyclone separator, a condensing system and alkali washing tank, an air inlet, the discharging port of the cyclone separator of the air outlet cyclone separator connecting microwave cracking furnace of connecting tar and particulate matter; the liquid outlet condensing system of cyclone separator of the air outlet connecting the condensing system of the air inlet, connecting oil tank, alkaline cleaning tank air outlet of air outlet of the condensation system connecting alkali cleaning tank of the air inlet, connecting air storage tank or gas pipeline. Using the production device of the biomass microwave cracking obtained liquid product-bio-oil ratio of improved, at the same time, bio-oil with the petroleum refining technology, the device processing the raw material does not need the fine crushing, so as to solve the biomass in large scale by high cost and economic;
NOVELTY - This utility new type claims a one biomass cracking gasification furnace, the structure include furnace body (1), furnace bar (3), a feeding port (8), a fuel gas nozzle (9), an air inlet (10), ash room (5), wherein the feeding port and gas nozzle is composed of inner container (11). and (12) interlayer structure, inner and outer liner connected at the bottom of the furnace in the upper part of the furnace body, a furnace body, feed inlet (8) and gas nozzle (9) is connected with the inner wall of the furnace liner (11) is connected, the air inlet (10) and the outer container (12) connected, furnace grid (3) is set on the bottom of the liner in the furnace body. This utility new type of biomass cracking gasification furnace from up down counter thermal cracking, feeding can be one continuous number for thermally cracking and gasifying, complete combustion, hot efficiency is high, no smoke dust, continuous stable produce, safety steady operation.
NOVELTY - This utility new type is a device containing hydrogen sulphide of natural gas, especially suitable for the oil extraction well, metering stations use, which can solve the oil field gas containing sulfureted hydrogen gas can not use of. The device comprise a reaction tank body and medicine is equipped with air outlet pipeline, a pressure meter and a sampling port on the top end of reaction tank body, feeder connecting the upper part of reaction tank body, in part of reaction tank body connecting liquid level meter, the bottom of reaction tank body is installed with an air inlet pipeline and a sewage outlet, the air inlet pipeline is connected with the distributor of reaction tank body, upper air inlet pipeline and the air outlet pipeline are set with control valve. This utility new type has small volume, light weight, strong commonality, is suitable for natural gas containing a small amount of hydrogen sulphide use. The device is simple, operation is convenient, hydrogen sulphide gas rear treatment reaches standard use, improves the utilization rate of natural gas and ensures production safety.
NOVELTY - Purification of crude biodiesel byproduct glycerin comprises acidifying with dilute acid at 45-50 degrees C for 30-60 minutes, recycling upper oil to biodiesel feed, reacting lower glycerol solution, adjusting pH with dilute alkali, standing, removing precipitate, feeding glycerin dilute solution to ion exchange column, removing impurities and evaporating.    USE - Method for purifying crude biodiesel byproduct glycerin.    ADVANTAGE - The simple and highly efficient method has reduced refining cost.
NOVELTY - Preparing micro-ecological fertilizer, comprises mixing Bacillus subtilis, Aspergillus niger, and Lactobacillus plantarum agent according to the ratio and pelleting to obtain the product.    USE - The method is useful for preparing micro-ecological fertilizer (claimed).    ADVANTAGE - The fertilizer is composed of composite microorganism, and rich in nutrition and high organic matter content; can satisfy organic food production requirement; can improve the micro-ecological environment of soil; provides favorable conditions for the growth of crops; and can enhance crop resistance to pests and diseases.
NOVELTY - Method for preparing ethanol fuel using sweet Sorghum involves pressing the sweet Sorghum and separating the juice and residues, concentrating the sweet Sorghum juice to obtain molasses, drying and soaking the Sorghum residues in diluted acid solution, performing steam explosion preprocessing on the diluted Sorghum residues, and adding alkali, adding 5-35 wt.% cellulase to the mixture and performing enzymolysis, adding 0-30 wt.% molasses to the enzymolyzed liquid, performing fermentation, and separating ethanol.    USE - The method is useful for preparing ethanol fuel using sweet Sorghum (claimed).    ADVANTAGE - The method enables to prepare product environmentally-friendly, which consumes less energy, and can be stored for long period of time.
NOVELTY - A 1,3 propanediol wastewater is treated by electrodialyzing to generate high concentration salt containing wastewater, entering heat exchanger and multi effect evaporator, evaporating to obtain liquid, concentrating, drying, cooling, mixing with discharge wastewater, entering into reactor, methanating under anaerobic fermentation bacteria, recovering methane gas, first stage aerobic biochemical treating, adding oxidant into ozone oxidation device, second stage aerobic biochemical treating, and discharging or recycling.    USE - Method for treating 1,3 propanediol wastewater (claimed).    ADVANTAGE - The method has high concentration salt content wastewater, comprehensive resource utilization, and is environment-friendly.
NOVELTY - Method for processing wastewater of cellulosic ethanol, involves (a) preprocessing and fermenting the iron in wastewater, (b) performing high pressure anaerobic treatment of the wastewater containing scrap iron, (c) performing Fenton oxidation of the processed wastewater, (d) adding organic flocculating agent to the wastewater and performing flocculation, and (e) filtering the product obtained in the step (d).    USE - The method is useful for processing wastewater of cellulosic ethanol (claimed).    ADVANTAGE - The method processes wastewater having high salt content, utilizes biodegradable organic matter of wastewater and hence saves subsequent aerobic biochemical process, and is cost-effective.    DETAILED DESCRIPTION - Method for processing wastewater of cellulosic ethanol, involves (a) preprocessing and fermenting the iron in wastewater preprocessing tank to generate large amount of ferrous and ferric ions, (b) passing the wastewater containing scrap iron after fermentation to the high pressure anaerobic reactor, performing high pressure anaerobic treatment of the wastewater containing scrap iron at the bottom of the reactor, and maintaining the reactor internal pressure at 0.1-1 MPa, (c) passing the processed wastewater of the step (b) from the lower portion of the anaerobic reactor to top portion of the Fenton oxidization reactor, and performing Fenton oxidation, (d) adjusting pH of the wastewater to 7-8, adding organic flocculating agent to the wastewater and performing flocculation, and (e) filtering the product obtained in the step (d).
NOVELTY - Method for processing potato straws, involves mixing bacteria and fermenting the potato straws for 2-3 weeks, obtaining probiotics comprising 108 colony-forming unit/g or more, enhancing straw utilization rate to 100%, and exploring dynamics model potato straw as main matrix of solid fermentation, where the straw is expected to be an environment conducive to high-value processing mode.    USE - The method is useful for processing potato straws (claimed).    ADVANTAGE - The method is environmentally-friendly and natural, and utilizes potato straw waste.
NOVELTY - High-activity bioorganic fertilizer comprises 30-70 wt.% poultry and livestock manure, 5-15 wt.% Eucalyptus powder, 5-15 wt.% mushroom powder, 5-15 wt.% straw powder, 5-15 wt.% distiller's grain, 0.1-0.5 wt.% trehalose, 0.1-0.2 wt.% effective microorganisms (EM) original liquid, 0.2-0.5 wt.% brown sugar, 0.2-0.5 wt.% elements zinc, magnesium, calcium, manganese, ferrous and sodium, and balance water.    USE - High-activity bioorganic fertilizer used as microbial inoculum and soil modifier.    ADVANTAGE - The bioorganic fertilizer has nitrogen-phosphorus-potassium content of greater than or equal to 7 wt.%, organic material content of greater than or equal to 60 wt.%, and plant growth promoting rhizobacteria (PGPR) viable count of greater than or equal to 2.7x 109-4x 109/g. Raw materials are inexpensive and easy to obtain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bioorganic fertilizer preparation by: (A) dissolving zinc, magnesium, calcium, manganese, ferrous and sodium in water to prepare 5 kg first mixture; (B) sequentially adding trehalose, EM original liquid, brown sugar, 10 kg water and 2 kg first mixture to a mixer, uniformly stirring, standing at 30-40 degrees C for 3-4 days, and discharging while maintaining normal pressure to obtain second mixture; (C) adding distiller's grain, Eucalyptus powder, mushroom powder, straw powder and second mixture to a blender, uniformly stirring for 30 minutes, standing at 50-60 degrees C for 3-4 days, and turning to permeate oxygen to obtain third mixture; and (D) adding chicken manure and 3 kg first and second mixtures to a mixer, uniformly stirring, stacking stirred mixture into a heap with width of 1.5-2 m and height of 0.8-1 m, covering with sack, aerobically composting at 60-70 degrees C for 3 days, heating to 55-65 degrees C, turning after 5-7 days, fermenting for 7-10 days, drying until water content of less than 30 wt.%, and packaging.
NOVELTY - Preparation of biological organic fertilizer comprises crushing traditional Chinese medicine dregs; mixing with livestock excrement, fermenting bacteria and water at ratio of 55-70:15-25:2-4:10-30 and stirring; fermenting at 60-90 degrees C for 2-15 hours; ventilating and aging at 60-70 degrees C and secondary fermenting for 3-6 days; adding nitrogen, phosphorus, and potassium at ratio of 25-40:30-45:10-20:10-20, stirring and crushing; granulating at 50-60 degrees C and maintaining water content at 8-15%; drying at 100-120 degrees C for 20-40 minutes until water content is 3-5%; cooling; and sieving.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The fertilizer solves environment pollution problem, reduces investment of inorganic nitrogen, phosphate and potassium fertilizer, reduces loss of nitrogen and potassium, prolongs fertilizer effect, improves phosphorus activity, and reduces soil fixation of phosphorus element.
NOVELTY - Wet production of basic zinc carbonate during wastewater treatment, comprises (i) adding calcium hydroxide into basic zinc carbonate wastewater, and adjusting the pH to produce ammonia gas; (ii) dividing ammonia gas into two portions, (a) passing carbon dioxide into part of ammonia gas, absorbing water to produce ammonium bicarbonate, and (b) adding zinc sulfate solution into another part of ammonia gas, to obtain a mixed solution; and (iii) mixing ammonium bicarbonate and mixed solution, controlling the pH to obtain basic zinc carbonate precipitate and ammonium sulfate solution.    USE - The method is useful for wet production of basic zinc carbonate during wastewater treatment.    ADVANTAGE - The method has high wastewater recovery efficiency, can reduce environment pollution, and saves energy consumption.    DETAILED DESCRIPTION - Wet production of basic zinc carbonate during wastewater treatment, comprises (i) adding calcium hydroxide into basic zinc carbonate wastewater, and adjusting the pH to 10-11 to produce ammonia gas; (ii) dividing the generated ammonia gas into two portions, (a) passing carbon dioxide into part of ammonia gas, absorbing water to produce ammonium bicarbonate, and (b) adding zinc sulfate solution into another part of ammonia gas, and controlling ammonia amount, to obtain a mixed solution; and (iii) mixing ammonium bicarbonate and mixed solution, controlling the pH of mixture to 6-7, to obtain basic zinc carbonate precipitate and ammonium sulfate solution.
NOVELTY - Biogas slurry composite comprises 99.5-99.8 wt.% biogas slurry, and 0.2-0.5 wt.% fungicidal agent comprising thiophene, thiazole, and copper acetate in a ratio of 1:1:8.    USE - The biogas slurry composite in the form of emulsion or powder is useful as farm chemical for promoting growth of crops, and preventing soft rot in vegetables and fruits.    ADVANTAGE - The biogas slurry does not leave any residue, has excellent antibiosis, reduces usage of farm chemical, is rich in nutrition, environmentally-friendly and directly absorbed by vegetable crops, enhances disease resistance ability, and exhibits bactericidal effect to more than 85%.
NOVELTY - Mushroom nutrient bag comprises 70-76 pts. wt. sawdust, 12-15 pts. wt. rice bran, 4-5 pts. wt. wheat bran, 1.5-2 pts. wt. gypsum powder, 1-1.5 pts. wt. sucrose, 0.8-1 pts. wt. calcium superphosphate and 100-110 pts. wt. water. The mushroom nutritional bag is a polypropylene bag having a bending range of 15X55 cm. The mushroom nutrient bag is cylindrical in shape, where the weight of each mushroom nutritional bag is 1600-1700 g.    USE - Used as a mushroom nutrient bag.    ADVANTAGE - The mushroom nutrient bag is maintained in a sterilizing room scale. The method has automatic production of edible fungi in the nutritious bag, and facilitates the culturing of bacterial fruiting body with stable production until there is cultivation of mushroom spawn.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing mushroom nutrient bag, comprising (i) mixing, and stirring sawdust, rice bran, wheat branand gypsum powder, to obtain dry material A, and adding sucrose and calcium superphosphate into the dry material A, and adding water into to obtain culture material having water content of 58-62%; (ii) adding the culture material into polypropylene bag to obtain mushroom nutrition bag; and (iii) sterilizing the obtained mushroom nutrient bag at room temperature by adding edible fungi into the bag, and performing high temperature steam sterilization.
NOVELTY - Microalgae is cleaned, dried and crushed. Cleaned algae, methanol and catalyst are added into a three-neck bottle, and spirulina powder is added. Three-mouth flask is set in ultrasonic device, under constant temperature water bath for 3-5 hours, and reaction is terminated and maintained. Algae powder is filtered, and petroleum ether is added and maintained to separate the petroleum ether phase. Resultant mixture is repeatedly extracted, and petroleum ether is evaporated, to obtain transparent biological preservative.    USE - Preparation of transparent biological preservative for aquatic diesel product.    ADVANTAGE - The method efficiently and economically provides transparent biological preservative with reduced consumption of energy.    DETAILED DESCRIPTION - Microalgae is cleaned, dried after removing impurities, and crushed. Cleaned algae, methanol and catalyst are added into a three-neck bottle, and spirulina powder is added. The content of catalyst is 4-5 %mass with respect to algae. The three-mouth flask is set in an ultrasonic device at 50-60 degrees C, under constant temperature water bath for 3-5 hours, and reaction is terminated and maintained. The algae powder is filtered, and 15-20 mL petroleum ether is added and maintained to separate the petroleum ether phase. The resultant mixture is repeatedly extracted, and petroleum ether is evaporated by a rotary evaporator, to obtain transparent biological preservative.
NOVELTY - Removing glycerol in biodiesel comprises according to oil to alcohol ratio of 1:5-1:8, adding cooking oil and methanol three-necked flask equipped with a stirrer motor and reflux condenser, heating to 60-65 degrees C, adjusting stirring rate at 400-500 revolutions per minute, reacting by constant stirring for 60-90 minutes, stratifying the obtained product, taking upper methyl ester solution, and evaporating methanol to obtained crude biodiesel; and washing crude biodiesel at 45-50 degrees C, for more than 4 times, stirring in an electric mixer at speed of 300-350 revolutions per minute, for 10-20 minutes.    USE - The method is useful for removing glycerol in biodiesel (claimed).    ADVANTAGE - The method is carried out under mild condition, requires fewer devices, has high removing efficiency, and simple operation.
NOVELTY - High-performance chemical liquid fuel comprises 5-15 pts. wt. ethanol, 3-8 pts. wt. potassium nitrate, 1-5 pts. wt. butyl butyrate and 90-100 pts. wt. methanol.    USE - The chemical liquid fuel is useful in suitable for municipal catering industry.    ADVANTAGE - The chemical liquid fuel can replace liquefied petroleum gas as hot pot; utilizes barbecue fuel, organic matter as raw materials, and easily available raw materials; is economical, and less volatile; has simple process procedures, and good and storage and transportation safety, easy application procedure, and high calorific value of 6000 kcal/kg; does not require hydroelectric machinery production process; utilized in direct artificial synthesis, and in iron bucket and plastic bucket; combustion is complete; does not produce carbon, and easily explode; and meets the environment protection requirements.
NOVELTY - A regenerative chemical liquid fuel comprises 50-75 pts. wt. crude methanol, 20-25 pts. wt. water, 1-5 pts. wt. catalyst, 1-2 pts. wt. potassium permanganate solution, and 5-10 pts. wt. fatty alcohol polyoxyethylene ether.    USE - Regenerative chemical liquid fuel.    ADVANTAGE - The fuel is smoke-free, nontoxic, non-explosive and convenient to use, greatly reduces pressure on supply and demand of petroleum products and its costs, lowers exhaust gas after combustion, and has readily available raw materials, simple process, and fuel heat value of 7500-10000 kcal/kg.
NOVELTY - The method involves pouring animal oil and hydrogen mix into a hydrogenation isomerization reactor and a hydrogenation refining and isomeric dewaxing reaction. Pneumatic liquid is mixed in a hot high pressure separator. Hot high liquid phase of catalytic cracking diesel is obtained. Hydrogenation refining diesel is poured into a mixing tank. A liquid phase hydrogenation reactor is placed in the hydrogenation refining and isomeric dewaxing reaction. A pressure reducing valve is connected with a decompression outflow device. Mixed hydrogen is stored in a storage tank.    USE - Animal, vegetable oil and diesel catalytic hydrogenation method.    ADVANTAGE - The method enables expanding refinery diesel production and raw material source, pouring animal and plant oil in the hydrogenation heterogeneous reactor and improving dissolved hydrogen amount in the liquid phase hydrogenation reactor and quality of diesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view illustrating an animal, vegetable oil and diesel catalytic hydrogenation method.
NOVELTY - Animal and vegetable oil and diesel feedstock are hydrogenated by mixing animal and vegetable oil in hydroisomerization reactor (3), hydrorefining, hydroisomerizing-dewaxing to obtain reaction effluent, introducing hot polymer gas (4), gas-liquid separating to obtain hot high liquid phase of diesel feedstock, entering into mixing tank (7) to mix with hydrogen, entering into liquid phase hydrogenation reactor (10) for hydrogenation refining reaction, and pressure-reducing reaction effluent via pressure reducing valve decompression flow device.    USE - Combined hydrogenation of animal and vegetable oil and diesel feedstock for producing ultra-low sulfur diesel.    ADVANTAGE - Amount of dissolved hydrogen in liquid-phase hydrogenation reactor is improved, animal and vegetable oils have higher cetane number, appropriate pour point, and almost zero sulfur content after isomerization, resulting in high quality clean fuel, and hydrogenation consumption is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the combined hydrogenation of animal and vegetable oil and diesel feedstock.    Animal and vegetable oil pipeline (1)    Hydroisomerization reactor (3)    Hot polymer gas (4)    Mixing tank (7)    Liquid phase hydrogenation reactor (10)
NOVELTY - The method involves pouring animal and vegetable oils and hydrogen mix into a rear hydrogenation isomerization reactor. A hydro-refining catalyst bed layer is formed by hydrogenation refining reaction process. A hot high pressure separator reaction effluent is entered into a pneuma liquid separator. Hot high liquid phase of a catalytic cracking diesel mix is obtained. Mixing hydrogen is entered into a mixing hydrogen storage tank. A hydrogenation reaction effluent part is obtained by a pressure reducing valve decompression rear outflow device.    USE - Animal and vegetable oil and catalytic diesel combined hydrogenation method.    ADVANTAGE - The method enables improving catalytic diesel quality.    DETAILED DESCRIPTION - The animal is selected from plant oil, animal oil, vegetable fat and animal fat. The vegetable oil is selected from in soybean oil, sunflower oil, rapeseed oil, palm oil, olive oil, linseed oil, cotton seed oil, castor oil, fish oil or cattle oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating of an animal and vegetable oil and catalytic diesel combined hydrogenation method.'(Drawing includes non-English language text)'
NOVELTY - The biomass solid fuel forming machine has propeller (1) that is inserted into mold structure (3) whose feeding end is set with anti-blocking mold (2). The anti-blocking mold is provided with circular tube whose inner structure is divided into four equal sized portions.    USE - Biomass solid fuel forming machine.    ADVANTAGE - The biomass solid fuel forming machine is provided with simple structure, convenient operational efficiency, improved production efficiency and long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass solid fuel forming machine.    Propeller (1)    Anti-blocking mold (2)    Mold structure (3)
NOVELTY - Preparation of antifouling coating comprises mixing cured resin, antistatic agent, photoinitiator and plasticizer at mass ratio of 10:1-5:0.2-2:0.5-3, stirring at 150-300 degrees C for 1-3 hours, adding stabilizer and toughener at mass ratio of 10:1-2:0.1-1, refining for 0.5-2 hours and heating for 1 hour.    USE - Method for preparing antifouling coating.    ADVANTAGE - The method is simple, inexpensive and environment-friendly.
NOVELTY - Straw and Eupatorium are crushed, stirred, and dried to moisture content of 5-10%. The resulted product is pressed in a mold into rod having cylinder, hexahedron cylinder or square column shape. The resulted rod is supplied into intermediate-pressure carbonization furnace, heated, maintained, air is introduced into the carbonization furnace, heated at 900 degrees C at rate of 60-80 degrees C/hour, air is stopped, and maintained, and carbon is removed. Thus, carbonization of Eupatorium is performed.    USE - Carbonization of Eupatorium (claimed).    ADVANTAGE - The carbonization of Eupatorium is performed by simple and economical method.    DETAILED DESCRIPTION - Straw and Eupatorium are crushed to diameter of l-5 mm. The resulted product is stirred, and dried to moisture content of 5-10%. The resulted product is pressed in a mold into rod having cylinder, hexahedron cylinder or square column shape. The resulted rod is supplied into intermediate-pressure carbonization furnace, heated at 130-180 degrees C for 2.5-3.5 hours, heated at 250-350 degrees C, maintained for 5-6 hours, air is introduced into the carbonization furnace, heated at 900 degrees C at rate of 60-80 degrees C/hour, air is stopped, and maintained for 70-80 hours, and carbon is removed. Thus, carbonization of Eupatorium is performed. The content of straw and Eupatorium in mixture is 55-65 wt.% and 35-45 wt.%, respectively.
NOVELTY - Synthesis gas is methanated by connecting not less than 2 methanation reactors in series, charging synthesis gas containing hydrogen (H2), carbon monoxide (CO), carbon dioxide (CO2) and water, performing high-temperature methanation, compressing, and carrying out low-temperature methanation to produce substitute natural gas.    USE - Method for methanating synthesis gas used for preparing substitute natural gas (claimed).
NOVELTY - A horizontal biomass granulator includes a chassis frame (1) set with a motor (2) and a distribution box (3), a main shaft transmission mechanism (4), a discharging channel (6), an upper disk card set with a machine head, and a scraping support mechanism. An upper scraper support mechanism can be set with a scraping mechanism (11). An upper chassis frame is set with a scraper transmission mechanism (12). A head disk through upper seal lock (13) is provided with a shell.    USE - A horizontal biomass granulator.    ADVANTAGE - The horizontal biomass granulator saves resource, improves production efficiency, has prolonged use life, and saves time.    DETAILED DESCRIPTION - A horizontal biomass granulator comprises a chassis frame (1) set with a motor (2) and a distribution box (3). A bottom end of the chassis frame is set with a main shaft transmission mechanism (4). An upper end of the discharging head disk is connected with a discharging channel (6). The discharging end of the machine head is set with leaking openings disk. An upper disk card is set with a machine head. A machine head disk through bearing is provided with a rotation of the main shaft mechanism. The upper grinding disc is set with a scraping support mechanism. An upper scraper support mechanism can be set with a scraping mechanism (11). An upper chassis frame is set with a scraper transmission mechanism (12). A head disk through upper seal lock (13) is provided with a shell. The top of the shell through end seal ring is provided with a machine cover. The machine upper cover is set with a feeding port. The upper machine covers one side of a feeding port set with oil hole. An oil hole is set with upper oil cover.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the horizontal biomass granulator.    Chassis frame (1)    Motor (2)    Distribution box (3)    Main shaft transmission mechanism (4)    Discharging channel (6)    Leaking openings (8)
NOVELTY - A biomass solid fuel heating economizer (1) comprises a tubular heating ring (2), a mold, an outer layer having vent holes (6), and a hollow layer having charcoal.    USE - A biomass solid fuel heating economizer.    ADVANTAGE - The biomass solid fuel heating economizer has a simple structure, has a convenient operation, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the economizer.    Biomass solid fuel heating economizer (1)    Tubular heating ring (2)    Vent holes (6)
NOVELTY - Medicine comprises 225 g longhairy Antenoron herb, 225 g oriental wormwood, 90 g radix curcumae, 150 g dried orange peel, 45 g radix scutellariae, 35 g frankincense, 80 g mirabilite, 35 g white alum, 45 g rhubarb, 45 g rhizoma sparganii, 45 g Gardenia, 25 g licorice and 35 g myrrh.    USE - The medicine is useful for inhibiting anal s-180 sarcoma cell proliferation (claimed).    DETAILED DESCRIPTION - Medicine comprises 225 g longhairy Antenoron herb, 225 g oriental wormwood, 90 g radix curcumae, 150 g dried orange peel, 45 g radix scutellariae, 35 g frankincense, 80 g mirabilite, 35 g white alum, 45 g rhubarb, 45 g rhizoma sparganii, 45 g Gardenia, 25 g licorice and 35 g myrrh. Preparation of the medicine, involves (a) subjecting frankincense, white alum and myrrh to carbon dioxide supercritical extraction at 15-30 MPa and 30-50 degrees C using 4-6% ethanol for 180-220 minutes to obtain supercritical extract for further use, (b) subjecting longhairy Antenoron herb, oriental wormwood, radix curcumae, dried orange peel, radix scutellariae, mirabilite, rhubarb, rhizoma sparganii, Gardenia and licorice to microwave extraction at 600-800 W using 50% ethanol for 2 times (each time for 5-10 minutes), and (c) combining the extracts, concentrating the combined extract, drying the concentrate, and tableting the dried concentrate into 500 tablets, where each tablet is 0.3 g.
NOVELTY - Method for preparing tablet, involves obtaining raw materials comprising turmeric, purple ginger, Stephania, rhizoma acori graminei and bitter herbs as raw material, crushing the raw materials, adding ethanol, placing mixture in microwave extracting device, extracting, combining the extracts, concentrating, adding diaion HP-10 macro-porous adsorption resin column, eluting with ethanol, decompressing, recovering ethanol, concentrating and drying to obtain microwave extract, adding ethanol, drying granule, tableting, and preparing into 500 tablets.    USE - The method is useful for preparing tablet which is used in preparation of drug for treating stomach pain and inhibiting proliferation of mouse P3X63AG8 myeloma cell (all claimed).    ADVANTAGE - The method improves curcumin content.    DETAILED DESCRIPTION - Method for preparing tablet, involves obtaining raw materials comprising 200 g turmeric, 200 g purple ginger, 200 g Stephania, 200 g rhizoma acori graminei and 200 g bitter herbs as raw material, crushing the raw materials, adding 5 l 70% ethanol, placing mixture in microwave extracting device at extraction power of 600-800 W, extracting for 2 times, each time for 5-10 minutes, combining the extracts, concentrating mixture, adding diaion HP-10 macro-porous adsorption resin column, eluting with 70% ethanol, collecting the 5 times volume of column, decompressing and recovering ethanol, concentrating and drying to obtain the microwave extract, adding 70% ethanol, drying granule, tableting, and preparing into 500 tablets, where each tablet has 0.3 g.
NOVELTY - The methanol to gas conversion burner has a heating tank (2) and a self-heating device (6). The heating tank is set with an oil inlet valve (1), and is set with a radiating fin (4). The self-heating device is provided with an exhaust hole (7). The heating tank is provided with a white steel mica heating set (3) covered outside of heating tank. The heating tank is provided with an automatic temperature control device (5).    USE - Methanol to gas conversion burner used for food boiler and petroleum industry.    ADVANTAGE - The environment-friendly and energy-saving burner can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methanol to gas conversion burner. (Drawing includes non-English language text)    Oil inlet valve (1)    Heating tank (2)    White steel mica heating set (3)    Radiating fin (4)    Automatic temperature control device (5)    Self-heating device (6)    Exhaust hole (7)
NOVELTY - A nickel-based methanation catalyst comprises a main component and accelerating agent. The main component includes nickel and magnesium. The accelerating agent includes carbon nanotubes. The content of nickel, magnesium and carbon nanotubes in the catalyst is 25-35 %mass, 38-53 %mass and 12-37 %mass, respectively.    USE - Nickel-based methanation catalyst (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nickel-based methanation catalyst, which involves dissolving nickel nitrate hexahydrate and magnesium nitrate hexahydrate in water to obtain solution (A), dissolving sodium hydroxide and sodium bicarbonate in water to obtain solution (B), adding the solution (A) and solution (B) into a reaction container, mixing, adjusting pH value to 9.8-10.2, aging, filtering, washing until the filtrate is neutral, drying and roasting to obtain nickel-magnesium oxide catalyst precursor, sieving precursor, diluting using quartz sand, reducing by introducing mixed gas of hydrogen and argon, then introducing carbon monoxide gas, removing impurities and cooling.
NOVELTY - A mesoporous potassium fluoride/calcium aluminate solid alkali is obtained by supporting potassium fluoride carrier to mesoporous calcium aluminate.    USE - Mesoporous potassium fluoride/calcium aluminate solid alkali used as ester exchange reaction catalyst for manufacturing biodiesel (claimed).    DETAILED DESCRIPTION - A mesoporous potassium fluoride/calcium aluminate solid alkali of formula: KF/CaxAl2O(x+3), where x is 0-2, is obtained by supporting potassium fluoride carrier to mesoporous calcium aluminate. An INDEPENDENT CLAIM is included for manufacture of mesoporous potassium fluoride/calcium aluminate solid alkali.
NOVELTY - Mixed refrigerant comprises isobutane as propane and propylene and unavoidable component, where the weight ratio of propane and propylene in liquid phase is 50:50 and the moisture content of refrigerant is 5 parts per million or less.    USE - The mixed refrigerant is used in refrigeration system for providing cooling effect.    ADVANTAGE - The mixed refrigerant is easy to handle, and replaced for the existing refrigerant without changing the specification of an apparatus. The global warming potential of the refrigerant for 100 years of the mixed refrigerant is 2.5 or less, and an ozone-crack coefficient is 0.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the refrigerant, which involves adding odor components to at least one of propane and propylene, mixing, sieving using molecular sieve, and adding water and mixing to obtain the product.
NOVELTY - Converting a biomass material, comprises (a) converting a biomass material in one or more steps into one or more 3-12C oxygenates, and (b) contacting the 3-12C oxygenates with hydrogen at a hydrogen partial pressure of more than 1.0 MPa in the presence of a sulfided carbon-carbon coupling catalyst, where the carbon-carbon coupling catalyst comprises greater than or equal to 60 wt.% of a zeolite and 0.1-10 wt.% of a hydrogenation metal, based on the total weight of the carbon-carbon coupling catalyst.    USE - The process is useful for converting a biomass material into a middle distillate boiling product (all claimed), preferably liquid transportation fuels or biofuels.    ADVANTAGE - The process efficiently converts the biomass material into the product, and can be operated for a prolonged period of time without substantial deactivation of the catalyst.
NOVELTY - Producing an end fuel composition, comprises (a) mixing a soap stock composition and a heavy fuel in predetermined proportions, and (b) centrifuging the resulting mixture to obtain the end fuel composition.    USE - The method is useful for producing an end fuel composition (claimed) from biomass, where the end fuel composition is useful in the field of industry including cement, sugar, glass, paper and heating.    ADVANTAGE - The method ensures economical and solid or liquid fuel composition produced from biomass with improved physico-chemical properties and high pumpability and without implementing complex chemical separation methods such as distillation and without environmental pollutions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel composition obtained by the method, comprising a mixture of soap stock composition and a heavy fuel, in which water content is less than 3 wt.%.
NOVELTY - Purifying biodiesel involves performing process under high-pressure using carbon dioxide at 2-50 megapascal to obtain desired product.    USE - Method for purifying biodiesel (claimed).    ADVANTAGE - The method enables to purify biodiesel in a rapid manner.
NOVELTY - Producing silage from a biomass comprises packing the biomass in a container to a bulk density sufficient to reduce oxygen levels within and surrounding the biomass, contacting the biomass with sulfur dioxide gas, formic acid and/or propionic acid to acidify the biomass and maintaining the biomass under conditions and for a time to produce silage from the biomass.    USE - The silage is useful to produce sugar streams, preferably monomeric sugars (claimed) and as fodder feed for livestock.    ADVANTAGE - The method: increases the rate and/or yield of monomeric sugars and produces less, preferably no lactic acid, when compared to a silage produced by an ensiling process that does not include the contacting step. The produced silage contains a lower level of bacteria, mold, and/or yeast when compared to a silage produced by an ensiling process that does not include the contacting step. The silage has good storage stability.
NOVELTY - A hydroisomerization process (P1) involves contacting a hydrocarbon feed stream comprising normal and singly branched 4-7C paraffins, under hydroisomerization conditions, with a catalyst comprising an aluminosilicate SSZ-82 zeolite and at least one Group VIII metal to form an isomerized product having a higher concentration of doubly and singly branched paraffins than the feed stream and having a 2,3-dimethylbutane to 2,2-dimethylbutane mole ratio of at least 0.7.    USE - As hydroisomerization process of light paraffins for the production of isomerized product of highly branched paraffins (claimed).    ADVANTAGE - The isomerized product comprises at least 25 mole% of dimethylbutane; and has research octane number (RON) of at least 85. The hydroisomerization process has maximum isomer yield; and provides high selectivity for producing high octane isomers of light paraffins, where the catalysts are also highly active, environmentally benign, and readily regenerable.
NOVELTY - Continuous production of bio-diesel from waste grease in a reactor, is claimed. The reactor has nano-structured and catalytically active inner reaction surface.    USE - The method is useful for continuous production of bio-diesel from waste grease in a reactor (claimed).    ADVANTAGE - The method is economical.
NOVELTY - Producing biodiesel, comprises feeding methanol into a tank and heating methanol to a temperature above a critical temperature of methanol to obtain a supercritical methanol, feeding a reactive matrix including a material oil and acetic acid into the tank, and adding a supercritical carbon dioxide into the tank. The supercritical methanol, the material oil, acetic acid, and the supercritical carbon dioxide are reacted with each other in the tank at 240-500 degrees C and 8.1-50 MPa for 0.1-1.5 hours to obtain biodiesel.    USE - The method is useful for producing biodiesel (claimed) used in various cooking oils, preferably waste cooking oils.    ADVANTAGE - The method is capable of rapidly producing biodiesel with high conversion rate of 97.83% and quality and reduced amount of glycerol by-product and without requiring additional extraction process in an economical manner.    DETAILED DESCRIPTION - Producing biodiesel, comprises feeding methanol into a tank and heating methanol to a temperature above a critical temperature of methanol to obtain a supercritical methanol, feeding a reactive matrix including a material oil and acetic acid into the tank, and adding a supercritical carbon dioxide into the tank with a total pressure of the supercritical methanol and the supercritical carbon dioxide of higher than 10 MPa. The supercritical methanol, the material oil, acetic acid, and the supercritical carbon dioxide are reacted with each other in the tank at 240-500 degrees C and 8.1-50 MPa for 0.1-1.5 hours to obtain biodiesel. The molar ratio of acetic acid to the material oil is 1:1 to 5:1, and methanol to the material oil is 20:1 to 90:1.
NOVELTY - Producing higher hydrocarbons, comprises: providing a carbohydrate; reacting the carbohydrate with hydrogen in the presence of a hydrogenolysis catalyst to produce reaction products comprising an alcohol, a polyol, and a higher polyol; recycling the higher polyol through the hydrogenolysis reaction to produce reaction products comprising an alcohol and a polyol and a higher polyol; and processing at least a portion of the reaction products to form a fuel blend.    USE - The method is useful for producing higher hydrocarbons (claimed) such as higher alkanes, olefins and aromatics, useful in transportation fuels (such as synthetic gasoline, diesel fuel and jet fuel), and industrial chemicals.    ADVANTAGE - The method: minimizes the formation of undesirable by-products such as coke, carbon dioxide and carbon monoxide, thus improving the overall yield of higher hydrocarbons; is capable of converting bio-based feedstocks, optionally without any additional costly purification steps to form higher energy density product of lower oxygen/carbon ratio; eliminates the steps required to convert bio-based feedstocks to fuel, thus reducing capital costs; produces carbohydrates that are highly reactive compounds that can be easily oxidized to generate energy, carbon dioxide, and water; and allows for collection and recycling of byproducts for use in other portions of the system.
NOVELTY - A photocatalytic capped colloidal nanocrystal, comprises first and second semiconductor nanocrystals, formed as a nanorod; a first inorganic capping agent overlying at least a portion of the first semiconductor nanocrystal; and a second inorganic capping agent overlying at least a portion of the second semiconductor nanocrystal. The first semiconductor nanocrystal nanorod regions lying at the ends of the nanorod, and the second semiconductor nanocrystal nanorod region disposed between the first semiconductor nanocrystal regions.    USE - For reducing carbon dioxide into methane and water (claimed). The methane is used as fuel for homes, businesses, and factories; and to produce thousands of products of everyday use, such as plastics.    ADVANTAGE - The photocatalytic capped colloidal nanocrystal reduces carbon dioxide to produce methane gas which is easily delivered as fuel for homes, businesses, and factories, while methane is also a basic raw material for many compounds to produce thousands of products of everyday use, such as plastics. Thus, the use of methane may help to decrease fossil fuel dependency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reducing (m1) carbon dioxide involving: introducing carbon dioxide gas and hydrogen gas into a reaction vessel; shining light onto a photoactive material within the reaction vessel, where the light has sufficient energy to produce charge separation within the photoactive material; passing the carbon dioxide gas through the photoactive material to react the carbon dioxide with the photoactive material; and initiating reduction of the carbon dioxide to methane and oxidation of the hydrogen to water.
NOVELTY - Cosmetic product in the form of foam to be applied to keratin fibers, preferably human hair, comprises a pressurized aerosol container, an aerosol dispenser and a cosmetic composition that contains (a) dimethyl ether as a first propellant, (b) one or more additional propellants including propane, propene, n-butane, isobutane, isobutene, n-pentane, pentene, isopentane and isopentene, (c) at least one cationic surfactant, (d) at least one water-soluble alcohol with 2-9 carbon atoms and 1-6 hydroxyl groups and (e) water.    USE - The cosmetic product in the form of foam is useful for styling keratin fibers, preferably human hair (wet hair) (all claimed).    ADVANTAGE - The cosmetic product allows uniform and comfort application of the composition to the hair thus providing good styling effect to the hair, and has good foam stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for styling wet hair, comprising producing the cosmetic product in aerosol form, spraying the composition using the aerosol dispensing apparatus onto wet hair, preferably hairline, shaping the hair into the desired shape with the fingers or with the aid of a comb or a brush, and drying the hair at room temperature or under heat.
NOVELTY - Fractionating lignocellulosic biomass involves providing feedstock comprising lignocellulosic biomass, extracting hemicelluloses from feedstock in presence of steam/hot water, and optionally first hydrolysis catalyst, generating first solids stream and first liquid stream, contacting first solids stream with acid or acid precursor, water, and solvent for lignin, to produce second liquid stream containing cellulose-rich solids and lignin, recovering the cellulose-rich solids from second liquid stream, hydrolyzing hemicelluloses to produce monomeric sugars, and recovering monomeric sugars.    USE - For fractionating lignocellulosic biomass (claimed), and for making glucose, as a pulp product, or as purified cellulose for making cellulose derivatives.    ADVANTAGE - The method efficiently fractionates any lignocellulosic-based biomass into its primary major components (cellulose, lignin, and if present, hemicellulose) so that each can be used in potentially distinct processes. An advantage of the process is that it produces cellulose-rich solids while concurrently producing a liquid phase containing a high yield of both hemicellulose sugars and lignin, and low quantities of lignin and hemicellulose degradation products. The flexible fractionation technique enables multiple uses for the products. The cellulose is highly reactive to cellulase enzymes for the manufacture of glucose. Other uses for celluloses can be adjusted based on market conditions.
NOVELTY - Biogas water removal device comprises an anaerobic digestion tank (20) for biogas generation connected to a gas reservoir (40) for storing biogas, a pipeline (50) adjacent to the upper portion of the anaerobic digestion tank for flowing biogas, a moisture condensation device (70) for condensation of moisture in the biogas to the outside air and a porous tube (71) installed in the interior of the pipeline and connected to the moisture condensation device.    USE - Used as biogas water removal device (claimed).    ADVANTAGE - The device: carries out anaerobic digestion process at an ambient temperature with a specific temperature difference with the outer side; increases the heat radiation performance to increase the moisture absorbance by using e.g. bent part on the pipeline, porous tube and cooling water spray unit; and prevents freezing rupture phenomenon of the pipeline or blockage of the pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biogas water removal device.    Anaerobic digestion tank (20)    Gas reservoir (40)    Pipeline (50)    Moisture condensation device (70)    Porous tube (71)
NOVELTY - Decomposition of biomass, comprises controlling supercritical or sub-critical condition within a reactor containing an aprotic solvent and biomass.    USE - The method is useful for decomposition of biomass (claimed).    ADVANTAGE - The method easily decomposes biomass under low temperature and pressure conditions utilizing less amount of aprotic solvent when compared with utilization of large amounts of polar solvents (water and alcohol) in regular decomposition method, does not require additional separation step of solvent and the biomass, produces product, which can utilized as mixed fuel by mixing with petroleum-based fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing furan derivative, comprising controlling supercritical or sub-critical condition within a reactor containing an aprotic solvent and biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for decomposition of biomass.
NOVELTY - Synthesizing an endocyclic hydrazine (I) and its salts, comprises: reacting a diamine compound (II) and an oxidizing agent consisting of salts of hypochlorous acid in an aqueous reaction medium at a temperature of 50-60 degrees C when n is 1; performing catalytic hydrogenation of the oxidation products to yield (I); and isolating (I).    USE - The method is useful for synthesizing (I) (claimed) such as pyrazolidine and hexahydropyridazine, where the pyrazolidine is useful as a precursor of antidiabetic drugs, anti-inflammatory drugs and antibiotics in a pharmaceutical industry and as pigments and dyes in cosmetic products, and the hexahydropyridazine is useful as a herbicide.    ADVANTAGE - The method is capable of economically and eco-friendly synthesizing (I) in an easy and clean manner.    DETAILED DESCRIPTION - Synthesizing an endocyclic hydrazine of formula (I) and its salts, comprises: reacting a diamine compound of formula (NH2-CHR1-CHR2-CHR3-(CHR4)n-NH2) (II) and an oxidizing agent consisting of salts of hypochlorous acid in an aqueous reaction medium at a temperature of 50-60 degrees C when n is 1; performing catalytic hydrogenation of the oxidation products to yield (I); and isolating (I).    R1-R4 = H, 1-2C alkyl, 1-6C aralkyl, or aryl, preferably phenyl or naphthyl, where one of R1-R4 represents alkyl group including more than three carbon atoms, and the other groups represent hydrogen atom; and    n = 0 or 1.
NOVELTY - Producing sugars and optionally alcohols and/or solvents from a biomass feedstock, comprises (a) performing pretreatment step that is carried out by contacting and heating the biomass feedstock with water and a basic/acidic compound to obtain a pretreatment substrate, (b) extracting a liquid stream from pretreated substrate to obtain a liquid stream and a liquid-depleted substrate, (c) mixing a part of obtained liquid stream with a pH neutralization agent, and (d) mixing the liquid stream comprising pH neutralization agent with the pretreated substrate to obtain a substrate comprising sugar.    USE - The method is useful for producing sugars and optionally alcohols and/or solvents from a biomass feedstock, which comprises wood, plant, lignocellulosic agricultural waste, and residues obtained from lignocellulosic materials processing industry (all claimed), where the alcohols include ethanol.    ADVANTAGE - The method is capable of effectively producing the sugars and optionally alcohols and/or solvents from biomass feedstock with high purity.    DETAILED DESCRIPTION - Producing sugars and optionally alcohols and/or solvents from a biomass feedstock, comprises (a) performing pretreatment step, which is carried out by contacting and heating the biomass feedstock with water and a basic or acidic compound to obtain a pretreatment substrate, (b) extracting a liquid stream from pretreated substrate to obtain a liquid stream and a liquid stream-depleted substrate, (c) mixing a part of obtained liquid stream with a pH neutralization agent, and (d) mixing the liquid stream comprising pH neutralization agent with the pretreated substrate or with liquid-depleted substrate to obtain a substrate comprising sugar.
NOVELTY - 3-Acetylmercapto-2-benzylpropionic acid is prepared. The obtained compound and glycine benzyl ester tosylate are dissolved in a reaction solvent (A), 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide or N,N'-dicyclohexylcarbodiimide is added as condensing agent, and amidation is carried out. The reaction solution is washed, reaction solvent is distilled off, and crude racecadotril is crystallized using alcohol/alkane mixed solvent.    USE - Preparation of racecadotril (claimed).    ADVANTAGE - The method enables economical, efficient, simple, quick and environmentally-friendly one-pot preparation of high-purity (not less than 95%) racecadotril with high yield, using reduced amount of reagents. Impurity-removal effect is excellent.
NOVELTY - The method involves forming an anode layer on a reaction prevention layer, where the reaction prevention layer is cerium. A cathode layer is formed on the reaction prevention layer by using the ion plantation in a chamber. The anode layer is treated with heat in temperature range of 900 to 1100 degree Celsius. The average thickness of the reaction prevention layer is in the range of 0.15 to 1 micro-meter. A gadolinia includes doped ceria, yttria doped ceria and samarium doped ceria. A doping element target includes gadolinia, and yttria and samarium oxide.    USE - Method for manufacturing solid oxide fuel cell.    ADVANTAGE - The anode layer on a reaction prevention layer, and the cathode layer is formed on the reaction prevention layer by using the ion plantation in a chamber, thus enables to steadily maintain the reaction prevention layer for a long time in a high temperature, and thus ensures a higher reliability of the fuel cell, also prevents the element having cathode material from being diffused to the electrolyte layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reaction prevention layer.    Vacuum chamber (100)    Coating piece stage (110)    Ceria target (130)    Doping element target (140)    Ion beam (150)
NOVELTY - The device has a liquefied gas tank provided with a boil off gas (BOG) heater. The BOG heater is provided with a reformer. The reformer heats compacted BOG is supplied from a BOG compressor. The BOG compressor compresses BOG generated from the liquefied gas tank. Endoergic reaction is performed according to hydrogen supplied from the reformer. The reformer collects exhaust gas generated in a fuel engine. The reformer is provided with a heating source and a hydrogen storage tank.    USE - Device for generating power in a fuel cell such as molten carbonate fuel cell (MCFC), solid oxide fuel cell and proton-exchange membrane fuel cell (PEMFC), of a liquefied gas carrier.    ADVANTAGE - The device has high energy utilization efficiency. The device enables producing electricity and hydrogen in a better manner. The device enables storing hydrogen in a hydrogen storage tank and supplying the hydrogen according to increase in load, so that BOG combustion process can be performed in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell power generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell power generating device.'(Drawing includes non-English language text)'
NOVELTY - Synthesis of 2-amino-3-(4-chloro)benzoyl-4-(N-alkyl/aryl piperazine-N'-methyl)thiophene (I), involves adding monochloroacetone in dropwise into substituted piperazine in presence of inorganic base at 30-40 degrees C, and then performing condensation reaction at 30-70 degrees C to give piperazine derivative (II); reacting the compound (II) and 4-chlorobenzoyl acetonitrile with an organic solvent, mixing sulfur, dripping organic amine, keeping the temperature at 25-65 degrees C for reacting, and obtaining the compound (I).    USE - For the synthesis of 2-amino-3-(4-chloro)benzoyl-4-(N-alkyl/aryl piperazine-N'-methyl)thiophene (claimed).    ADVANTAGE - The method is simple and convenient; uses raw materials which are easy to obtain; is environment-friendly; provides high product selectivity, high yield and high purity; and is suitable for industrial application.    DETAILED DESCRIPTION - Synthesis of 2-amino-3-(4-chloro)benzoyl-4-(N-alkyl/aryl piperazine-N'-methyl)thiophene, involves adding monochloroacetone in dropwise into substituted piperazine in the presence of inorganic base at 30-40 degrees C, and then performing condensation reaction at 30-70 degrees C to give piperazine derivative of formula (II); taking piperazine derivative (II) and 4-chlorobenzoyl acetonitrile in a molar ratio of 1-1.2:1, and reacting with an organic solvent, mixing sulfur, dripping organic amine, keeping the temperature at 25-65 degrees C for reacting, and obtaining the compound (I).    R'=methyl, ethyl, propyl, octyl, benzyl or aryl.
NOVELTY - Preparing praziquantel (VIII) by one-pot synthesis comprises (i) ammonolysis of dimethylchloroacetal (I) with aqueous ammonia solution to obtain 2,2-dimethoxyethanamine (II), (ii) condensing beta -phenylethylamine (III) with chloroacetyl chloride (IV) to obtain 2-chloro-N-phenethyl acetamide (V), (iii) condensing (V) with (II) to obtain 2-(2,2-dimethoxyethylamino)-N-phenethylacetamide (VI), (iv) cyclizing (VI) to obtain 2,3,6,7-tetrahydro-1H-pyrazino(2,1-a)isoquinolin-4(11bH)-one (VII), and (v) reacting (VII) with cyclohexyl carbonyl chloride and employing solvent crystallization.    USE - The method is useful for preparing praziquantel (claimed).    DETAILED DESCRIPTION - Preparing praziquantel of formula (VIII) by one-pot synthesis comprises (i) ammonolysis of dimethylchloroacetal of formula (I) with 20-40% aqueous ammonia solution (II) to obtain 2,2-dimethoxyethanamine of formula (II) where the molar ratio of (I) to ammonia is 1:15-30, (ii) condensing beta -phenylethylamine of formula (III) with chloroacetyl chloride of formula (IV) in presence of an chlorinated paraffins alkaline environment to obtain 2-chloro-N-phenethyl acetamide of formula (V), where the molar ratio of (III) to (IV) is 1:0.8-2.5, (iii) condensing (V) obtained in step (ii) with (II) obtained in step (i) in an organic solvent to obtain 2-(2,2-dimethoxyethylamino)-N-phenethylacetamide of formula (VI), where the molar ratio of (V) to organic solvent is 1:1.2-4, (iv) cyclizing (VI) under an acid catalyst to obtain 2,3,6,7-tetrahydro-1H-pyrazino(2,1-a)isoquinolin-4(11bH)-one of formula (VII), where the molar ratio of (VI) to acid catalyst is 1:1.2-5, and the acid catalyst includes sulfuric acid or methane sulfonic acid, and (v) reacting (VII) with cyclohexyl carbonyl chloride in an organic solvent and employing solvent crystallization to obtain (VIII), where the molar ratio of (VII) to cyclohexyl carbonyl chloride is 1:1-2, and the crystallization solvent includes isopropanol or acetone.
NOVELTY - A method, comprises contacting at least one substrate with at least one enzyme and at least one polymer comprising a set of monomer residues.    USE - The method is useful for producing a product from a biomass (claimed), preferably the production of sugars from cellulose in biomass, and for enhancing enzymatic activity.    ADVANTAGE - The method is cost-effective, and efficiently uses polymers to increase enzymatic activity and stability.    DETAILED DESCRIPTION - A method, comprises contacting at least one substrate with at least one enzyme and at least one polymer comprising a set of monomer residues having the structure of formula (I).    R1=H or alkyl; and    R(A) and R(B)=H, unsubstituted or substituted aliphatic group, unsubstituted or substituted alicyclic group, unsubstituted or substituted aryl, unsubstituted or substituted heteroaryl, or unsubstituted or substituted heterocyclyl; provided that at least one of R(A) and R(B) is other than H.    INDEPENDENT CLAIMS are:    (1) a method of hydrolyzing biomass, comprising: (a) providing biomass, a hydrolysis enzyme, and a thermally-responsive polymer; (b) contacting the biomass with the hydrolysis enzyme in the presence of the thermally-responsive polymer, where the thermally-responsive polymer is: poly N-isopropylacrylamide, poly N-isopropylmethacrylamide, or a copolymer comprising a set of first monomer residues and a set of second monomer residues, where each of the first monomer residues is independently selected from N-isopropylacrylamide, N-isopropylmethacrylamide, and any combinations, and each of the second monomer residues is an aminooxy-bearing methacrylamide monomer residue; and (c) hydrolyzing at least a portion of the biomass to produce sugars; and    (2) a composition, comprising: at least one substrate; at least one enzyme; and at least one polymer comprising a set of monomer residues having the structure of formula (I).
NOVELTY - A heterogeneous hydrogenation catalyst comprises solid surface substantially free of metals; and at least one defect frustrating at least one pair of the at least one Lewis acid site and the at least one Lewis base site to provide at least one frustrated pair of Lewis acid and Lewis base sites. The solid surface has at least one Lewis acid site and at least one Lewis base site. The frustrated pair of Lewis acid and Lewis base sites are catalytically active.    USE - For catalytically hydrogenating an alkene (claimed); and for production of biofuels, hydrogenated oils and fats, and plastics; and upgrading both petroleum and bio-based fuels.    ADVANTAGE - The catalyst has significant commercial value. The catalyst is more stable and degrades much slower than homogenous catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) heterogeneous hydrogenation catalyst comprising solid surface having non-metallic Lewis acid moieties and non-metallic Lewis base moieties spaced a distance apart from one another such that enable catalytic activity is present between and the formation of an acid-base adduct is prevented;    (2) heterogeneous hydrogenation catalyst comprising sheet of catalytically active material, substantially free of metals, having unsatisfied Lewis acid-base pairs along a surface of the sheet;    (3) making hydrogenation catalyst involving mechanically processing hexagonal boron nitride in presence of an alkali metal element to produce defective surface that catalyzes a hydrogenation reaction;    (4) hydrogenation process involving contacting hydrogenatable compound with hydrogen gas and the catalyst in a reactor; and catalytically hydrogenating the hydrogenatable compound.
NOVELTY - The method involves arranging welding projections (113a-113c) of an manifold and welding guides (114) of an manifold to be engaged with each other while maintaining a uniform gap between each other to bond manifolds in an up and down stacking structure. A manifold is pressed and the vibration is applied to the other manifold in the left and right direction to bond the two manifolds. A longitudinal direction of non-horizontal welding projection does not coincide with vibration direction of the manifold and height of non-horizontal welding projection is varied.    USE - Method of manufacturing manifold for fuel cell.    ADVANTAGE - The frictional heat generated between the welding projection and the welding guide reaches a predetermined friction temperature such that appropriate amount of molten resin is provided during the vibration welding. Thus the welding quality is improved and incomplete bonding caused when the frictional heat between the welding projection and the welding guide is below predetermined friction temperature or the melting rate of the welding projection is prevented. The mismatch caused between the vibration direction and the longitudinal direction of the welding projection is prevented and welding strength is ensured. The durability is increased and thus the performance of the fuel cell is improved. The manufacturing cost and manufacturing time of manifold is reduced and generation of fine powder is prevented to improve the safety of the working environment. The minimum thickness of the manifold is achieved and the weight of the manifold is reduced. Since individual manifold is additionally stacked or multilayer manifold is separated and then bonded by vibration welding, the degree of freedom in the design is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the manifold.    Protruding portion (112)    Welding projections (113a-113c)    Welding guide (114)
NOVELTY - Treating rubber sewage involves entering rubber sewage into preliminary sedimentation tank and transporting rubber precipitate to regulating tank. The suspension and colloidal granules are transported to air system and polyaluminum chloride and polyacrylamide are added. The suspension and colloidal granules are removed by vortex concave air floating machine from sewage. The sewage is transported to hydrolysis acidification tank and then sewage is treated by acidification bacteria.    USE - Method for treating rubber sewage (claimed).    ADVANTAGE - The method enables to treat rubber sewage in a simple and cost-effective manner.    DETAILED DESCRIPTION - Treating rubber sewage involves entering rubber sewage into preliminary sedimentation tank and transporting rubber precipitate to regulating tank. The suspension and colloidal granules are transported to air system and polyaluminum chloride and polyacrylamide are added. The suspension and colloidal granules are removed by vortex concave air floating machine from sewage. The sewage is transported to hydrolysis acidification tank and then sewage is treated by acidification bacteria. The sewage is transported to anoxic-aerobic oxidation pond and then treated by microorganism to remove organic pollutant in sewage. The sewage is now transported to secondary sedimentation tank and the precipitate is removed. The sewage is transported to catalytic oxidation reactor and then ferrous sulfate and hydrogen peroxide are added into the catalytic oxidation reactor. The organic pollutant is removed from sewage in the catalytic oxidation reactor. The sewage is now entered into oxidation flocculation reaction tank and then oxidizing agent is added to completely oxidize organic pollutant in sewage. The flocculating agent and alum are added into sewage, where flocculation reaction time is 20-40 minutes. The sewage is entered into three sedimentation pond and then water is ready to be discharged.
NOVELTY - Hydrocortisone sodium succinate is dried by placing wet material in microwave feed tray to thickness of 20-40 mm, programming microwave power at 3-5 W/g feed, and performing microwave drying at 30-55 degrees C for 300-500 seconds.    USE - Method for drying hydrocortisone sodium succinate (claimed).    ADVANTAGE - The low-cost and non-polluting drying process does not produce waste heat and dust, and does not contaminate medicine.
NOVELTY - The system (100) has a dust collector (110) to collect dust included in synthetic gas and ejects synthetic gas to pinned layer single reactor (120). A discharging unit (130) discharges desulphurizing agent and desalting agent to outside. A division unit (140) separates desulphurizing agent and desalting agent, and ejects large desulphurizing agent and small desalting agent to upper and lower portions. A reactor (180) is provided with synthetic gas which is desalted desulfurizing agent and desalting agent sprayed to inner portion, to remove sulfide and chlorine compound.    USE - High temperature purification system for simultaneously removing desulphurization and desalination in synthetic gas using fixed bed single reactor, for use in gasification melting furnace or gasifier used during manufacture of fuel cell or chemical fuel cell.    ADVANTAGE - The desulphurization agent and desalination agent included in the synthetic gas are removed effectively using the dust collector and the pinned layer single reactor. The utilization ratio of the desulphurizing agent and desalting agent can be enhanced effectively. The establishment area of the high temperature purification system is reduced and the cost of establishing the high temperature purification system can be minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the high temperature purification system for simultaneously removing desulphurization and desalination in synthetic gas.(Drawing includes non-English language text)    High temperature purification system for simultaneously removing desulphurization and desalination in synthetic gas (100)    Dust collector (110)    Pinned layer single reactor (120)    Discharging unit (130)    Division unit (140)    Reactor (180)
NOVELTY - A support is arranged to process chamber filled with supercritical fluid. A complex of metal catalyst is dispersed in supercritical fluid. Temperature of support or atmospheric temperature of processing chamber interior is controlled. The temperature difference between temperature of support and atmospheric temperature is fluctuated. The supercritical state of supercritical fluid is released and metal catalyst is deposited on surface of support, to obtain metal catalyst support.    USE - Manufacture of metal catalyst support used for manufacturing fuel cell (claimed).    ADVANTAGE - The method enables manufacture of metal catalyst support with reduced generation of variation in the particle diameter of metal catalyst. The fuel cell manufactured using metal catalyst support has excellent electric power generation characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) metal catalyst support, which carries metal catalyst on support;    (2) manufacture of fuel cell, which involves manufacturing metal catalyst support and forming electrode layer which has gas diffusion property on the surface of electrolytic membrane by metal catalyst support; and    (3) catalyst support apparatus, which comprises a process chamber and a temperature control portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of flowchart explaining carrying process of the metal catalyst with respect to the support in catalyst support apparatus. (Drawing includes non-English language text)    Arranging process (S100)    Dissolution process (S110, S112)    Absorption process (S120-S124)    Precipitation process (S140)    Ex-post facto process (S150)
NOVELTY - The fuel cell system (1) has a pre-heater (100) that is provided for preheating the fuel. A back up reformer (200) is provided in a fuel cell stack module (300), for reforming the preheated fuel. The fuel cell stack module is provided for producing electricity after reaction of reformed fuel. A circulator (400) is provided for selectively supplying the electricity generated in fuel cell stack module to pre-heater. A bypass line (420) is provided to detour the product about the pre-heater.    USE - Fuel cell system.    ADVANTAGE - Since the circulator is provided for selectively supplying the electricity generated in fuel cell stack module to pre-heater, the energy application efficiency of the fuel cell system can be improved. By controlling the preheat mood of the pre-heater, the state of fuel can be controlled flexibly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Pre-heater (100)    Back up reformer (200)    Fuel cell stack module (300)    Circulator (400)    Bypass line (420)
NOVELTY - The kit has an outline mold provided with a broadening line and a shifting line for determining an absorption line from a gas mixture, where concentration of gas and mixture of gases are measured at certain pressure. A narrowband laser performs a gas concentration measurement process, where wavelength of the laser is overtaken above an absorption in the gas. An optical or optoacoustic detection unit receives the outline mold. A light scattering unit obtains a gas-containing sample. A gas component is selected from a group consisting of oxygen, carbon dioxide, methane, nitrogen and hydrogen.    USE - Kit for determining gas concentration of a gas mixture inside a food package for liquid or solid substances, porous construction materials e.g. Styrofoam (RTM: Closed-cell extruded polystyrene foam), wood, ceramics and pharmaceutical preparations, and utilized for a human and an animal to treat sinus cavities, mastoid, inner ear, lungs or intestines for diagnosis of diseases extra such as sinusitis, otitis, Bronchopulmonary dysplasia, chronic obstructive pulmonary disease and colic or necrotizing enterocolitis, diagonsis of a lung lobe during malignant tumor growth (all claimed).    ADVANTAGE - The kit can determine oxygen concentration by feeding on a water meadow line that is accessed for examination in an easy manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for determining gas concentration of a gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a kit for determining gas concentration of a gas mixture inside a food package.'(Drawing includes non-English language text)'    Photodiodes (FD)
NOVELTY - Invention relates to agriculture. The method of production of compost from organic wastes comprises mixing the wastes in the form of sugar beet pulp with paunch manure, adding of bioactivator and aerobic composting, at that interlayering of sugar beet pulp of natural moisture with calcium lime in the ratio of 20:1 by weight is carried out, air-dry defecation is added in the ratio of 1:1 by weight to the pulp with simultaneous addition of bioactivator, and composting is carried out at a temperature from 20 to 50 degrees C and humidity of 50-70% during 2 months, at that the bioactivator is used as the compost starter prepared in sugar beet paunch manure using the method of cultivation of microorganisms from vermicompost, and the composting is carried out in layers with the layers of 0.3 m of pulp and defecate with placement of paunch manure between the layers.    USE - Agriculture.    ADVANTAGE - Invention enables to obtain the agrochemically valuable compost.1 ex
NOVELTY - A tebuconazole is prepared by carrying out condensation reaction of p-chlorobenzaldehyde with pinacolone under action of alkali to obtain 1-(4-chloro-phenyl)-4,4-dimethyl-pent-1-en-3-one, reacting with hydrogen gas for hydrogenation under action of hydrogenation catalyst to obtain 1-(4-chloro-phenyl)-4,4-dimethyl-pent-3-one, performing epoxidation reaction with sulfonium salt to obtain 2-(4-chlorophenethyl)-2-tert.-butyl oxide, and carrying out ring-opening reaction with triazole in organic solvent under action of organic amine and crown ether.    USE - Preparation of tebuconazole (claimed).    ADVANTAGE - The process is safe, nonflammable, and environment-friendly, has high product yield, and reduces byproducts generation.    DETAILED DESCRIPTION - A tebuconazole is prepared by carrying out condensation reaction of p-chlorobenzaldehyde with pinacolone under action of alkali to obtain 4,4-dimethyl-1-(4-chlorophenyl)-1-penten-3-one of formula (II), reacting with hydrogen gas for hydrogenation under action of hydrogenation catalyst to obtain 1-(4-chloro-phenyl)-4,4-dimethyl-pent-3-one of formula (III), performing epoxidation reaction with sulfonium salt of formula (CH3)3S+CH3SO4- to obtain 2-(4-chlorophenethyl)-2-tert.-butyl oxide of formula (V), and carrying out ring-opening reaction with triazole in organic solvent under action of organic amine and crown ether.
NOVELTY - New quantum energy high yield and quality rice planting method involves improving soil during spring by ploughing soil and applying ecological fertilizer, performing seed germination, sowing the germinated seeds and spraying in seedling bed, coating the seeds with slurry, applying the fertilizer containing brown sugar, potassium mineral powder, urea, bean cake or peanut cake, rice bran, wooden meal, edible fungi culture medium residue, wheat bran, animal excrement on the sowed seedling, and performing anaerobic fermentation.    USE - The new quantum energy method is useful for planting rice (claimed).    ADVANTAGE - The method enables to plant rice with high quality and yield and cost-effectively.    DETAILED DESCRIPTION - New quantum energy high yield and quality rice planting method involves (a) improving soil during spring by ploughing soil and applying 20-30 kg ecological energy and 5-10 kg/acre ecological fertilizer for 7-10 days, then deeply turning at height of 25-30 cm, until the ecological fertilizer is uniformly embedded in the soil, where the ecological fertilizer comprises nitrogen, phosphorus and potassium fertilizer in a ratio of 4:20:10 and trace elements required for rice, exposing the seeds under sunlight for 3 hours and adding water at 35-40 degrees C, adding 0.5-1.5% effective microorganism to the water barrel, and soaking for 5-8 hours, maintaining the soaked seeds at 25-30 degrees C, and performing germination for 24-36 hours, sowing the germinated seeds and spraying in seedling bed, coating the seeds with slurry for 24 hours, applying the fertilizer containing brown sugar, powdered rock phosphate, potassium mineral powder, urea, bean cake or peanut cake, food industrial leftovers, rice bran, wooden meal or edible fungi culture medium residue, wheat bran, animal excrement on the sowed seedling, and performing anaerobic fermentation at 20-30 degrees C for 10-15 days.
NOVELTY - The system has a hydrogen generating reactor (20) which is connected with a methane reactor (30) through a material conveying pipe (21) to convey hydrogen and methane to a product gas collecting device. The hydrogen generating reactor is provided with a material return device (22). The material flow rates of material conveying pipe and hydrogen generating reactor are adjusted. The material reflux ratio of methane reactor and material return device is adjusted. The material is buffered so as to adjust the material anaerobic fermentation speed.    USE - System for producing mixture of hydrogen and methane by fermentation of biomass such as wood, straw, leaf, sawdust, wooden chip, animal corpse and excrement, municipal or domestic organic garbage, crop waste, wood fiber, organic waste or sludge, terrestrial plant and aquatic plant (all claimed).    ADVANTAGE - The hydrogen and methane conversion rate can be improved, and the material anaerobic treatment effect can be adjusted reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing mixture of alkyl hydrogen and fermentation of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the mixture producing system.    Hydrogen generating reactor (20)    Material conveying pipe (21)    Material return device (22)    Methane reactor (30)    Fermentation slag tank (60)
NOVELTY - Fuel comprises an organic energy carrier material comprising impurities, preferably sulfur compounds uniformly distributed in the energy carrier material. The sulfur compounds decompose during combustion process in a combustion plant into acidic flue gas components. The energy carrier material is mixed with magnesium lime to reduce the acidic flue gas components.    USE - The ground magnesium lime (dolomite) is useful as an aggregate for the energy carrier material in form of crushed and dried biomass for thermal energy production in a wood combustion plant. The fuel is useful for a wood combustion plant for thermal energy production (all claimed).    ADVANTAGE - The fuel can be produced without acidic pollutant compounds in simple and cost-efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the fuel containing organic energy carrier material, comprising crushing the energy carrier material, mixing the crushed energy carrier material with magnesium lime, and pressing the energy carrier material mixed with magnesium lime into pellets.
NOVELTY - The present invention provides a method of using ultrasonic wave to modify tung oil biodiesel, which includes: mixing an oil containing 20~80wt% tung oil, 10~50wt% canola oil and 0~30wt% palm oil, an alcohol and a transesterification catalyst to be a mixture, and using the ultrasonic wave to sonicate the mixture for obtaining a tung oil biodiesel having the low kinematic viscosity and the low iodine value. By regulating the oil volume and the ultrasonic power, the present invention can increase the blended content of tung oil and improve the disadvantages of high kinematic viscosity and high iodine value of tung oil biodiesel.
NOVELTY - Enterococcus species MA17 (KCTC12308BP) having mixed acid fermentation productive capacity from Rhodophyta, is new.    USE - The Enterococcus species MA17, Clostridium butyricum MA15 or microorganism consortium are useful for producing mixed organic acid e.g. acetic acid, propionic acid, butyric acid, lactic acid, succinic acid, valeric acid and/or caproic acid (all claimed) and producing bio-fuel.    ADVANTAGE - The bio-fuel production is economical and highly-efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) Clostridium butyricum MA15 (KCTC12308BP) having mixed acid fermentation productive capacity from Rhodophyta; (2) microorganism consortium, comprising Enterococcus species MA1, Enterococcus species MA2, Enterococcus species MA3, Enterococcus species MA6, Enterococcus species MA9, Enterococcus species MA12 or Enterococcus species MA17 and Clostridium butyricum MA11, Clostridium butyricum MA14 or Clostridium butyricum MA15; and (3) producing mixed acid, comprising culturing any of above strain or microorganism consortium with Rhodophyta in a culture medium, and recovering mixed organic acid.
NOVELTY - Hydrogen-storage-material comprises ammonia borane and poly(ethylene oxide). The poly(ethylene oxide) has a weight average molecular weight of 1-9 MDa.    USE - The hydrogen-storage material is useful for releasing the hydrogen stored (claimed) upon demand, and as a hydrogen source or hydrogen fuel source.    ADVANTAGE - The hydrogen-storage-material: utilizes poly(ethylene oxide) which reduces foaming and/or swelling of the hydrogen-storage-material when hydrogen is released from the ammonia borane; can be produced in a cost effective manner; and exhibits shorter incubation times at low temperatures before hydrogen is released.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) releasing hydrogen stored within the hydrogen-storage-material, comprising heating the material to release hydrogen from the ammonia borane;    (2) manufacturing the hydrogen-storage- material, comprising either mixing a powder of ammonia borane with a powder of poly(ethylene oxide), or dissolving ammonia borane and poly(ethylene oxide) in a solvent to form a solution, and solidifying the solution to form the hydrogen-storage-material; and    (3) use of poly(ethylene oxide) in the hydrogen-storage material, to reduce foaming and/or swelling of the hydrogen-storage-material when hydrogen is released from the ammonia borane.
NOVELTY - Hydrogen generating device (1) has reformer generating fuel gas which is mainly composed of hydrogen from a source gas, combustor (13) heating the reformer (6), hydrodesulfurizer (3) heated by the reformer to remove sulfur compounds in the source gas by hydrodesulfurization, and cooler (19) cooling the hydrodesulfurizer, where the reformer includes a low temperature portion and high temperature portion having temperature higher than the low temperature portion, and the cooler is provided at a position corresponding to the high temperature portion of the reformer.    USE - As hydrogen generating device.    ADVANTAGE - The hydrogen generating device has reduced size, and reduces amount of mounting of hydrodesulfurization catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view of the hydrogen generating device.    Hydrogen generating device (1)    Hydrodesulfurizer (3)    Reformer (6)    Combustor (13)    Cooler (19)
NOVELTY - The apparatus (110) has a pre-compactor (111) receiving solid waste (101) and compacting the solid waste to form a compacted solid waste. A supply device (116) adds carbon bed source material (103) to a compacted solid waste. A feed device (112) receives the compacted solid waste and carbon bed source material and introduces the compacted solid waste and carbon bed source material as a combined feed into a plasma gasifier reactor. A scrubber system contacts a stream of a syngas (104) with water to remove particulates from the syngas and form a sludge with water and removed particulates.    USE - Apparatus for feeding solid waste i.e. municipal solid waste into a plasma gasifier reactor.    ADVANTAGE - The apparatus feeds the solid waste into the plasma gasifier reactor, while achieving high level of conversion of organic waste material to a syngas and preventing production of toxic and environmentally harmful species in an efficient manner.    DETAILED DESCRIPTION - The carbon bed source material is met coke and anthracite coal. INDEPENDENT CLAIMS are also included for the following:    (1) an apparatus for processing solid waste with organic and inorganic waste material    (2) a method for feeding solid waste with organic and inorganic waste material into a plasma gasifier reactor    (3) a method for processing solid waste with organic and inorganic waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram illustrating a method for feeding municipal solid waste into a plasma gasifier reactor and converting the municipal solid waste into a syngas and a slag.    Solid waste (101)    Carbon bed source material (103)    Syngas (104)    Apparatus for feeding solid waste (110)    Pre-compactor (111)    Feed device (112)    Supply device (116)
NOVELTY - The device has ozonated water exhaust port (160) that is used ejecting water. Storage tank (300) is provided with sterilizing water generated in chamber (30) through fluid path (D) connected to ozonated water exhaust port. Hydrogen water and sterilizing water are stored in storage tank provided with pump (200) connected to flow path (C). Input terminal is connected to bottom surface of storage tank, and spray port (150) used for spraying hydrogen water stored in storage tank and flux of hydrogen water is ejected using pressure of pump through hydrogen water exhaust port.    USE - Hydrogen water preparing device.    ADVANTAGE - Flowing structure of water can be improved in order to increase the concentration of active hydrogen in water. The hydrogen concentration of hydrogen water can be penetrated, electrode module hydrogen atoms adhered to the cathode surface can be separated and water spraying effect can be enhanced to direction perpendicular to the cathode surface.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen water manufacturing device.    Chamber (30)    Spray port (150)    Ozonated water exhaust port (160)    Pump (200)    Storage tank (300)    Flow paths (C,D)
NOVELTY - Producing polymers from algae, comprises: (a) culturing an alkenone-producing alga under a growth condition sufficient to produce alkenones within the alga; (b) optionally chemically modifying the alkenones to produce alkenone derivatives; and (c) polymerizing the alkenones or alkenone derivatives.    USE - The method is useful to produce polymers from algae, where the polymers are useful for forming hydrocarbons (claimed), or a liquid biofuel (comprising diesel and gasoline) or gaseous biofuel comprising syngas and/or a synthetic hydrocarbon gas (methane, propane and butane).    ADVANTAGE - The method: is capable of converting a mixture of fatty acid methyl esters (FAMEs) and alkenones to hydrocarbons without separating the FAMEs from the alkenones; is efficient in controlling the foreign algae population among the more desirable oil-producing algae; and eliminates several costly steps including solvent extraction, hence it is simple and cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a polymer produced by the method.
NOVELTY - System comprises: a fatty acid methyl ester stream; and a first strong acid catalyst resin vessel (40). The first strong acid catalyst resin vessel comprises a strong acid catalyst resin. The strong acid catalyst resin has a density of 30-45 lb/ft within the first strong acid catalyst resin vessel. The first strong acid catalyst resin vessel receives the fatty acid methyl ester stream. First strong acid catalyst resin vessel outputs a treated fatty acid methyl ester stream.    USE - The system is useful for treating fatty acid methyl esters streams (claimed) to produce biodiesel.    ADVANTAGE - The system provides the treated fatty acid methyl ester stream that comprises no more than trace amounts of monoglyceride content under the ASTM D6584 test, in a cost effective manner with high amounts of recycling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating fatty acid methyl esters streams, comprising: receiving the fatty acid methyl ester stream at the first strong acid catalyst resin vessel; and outputting a treated fatty acid methyl ester stream from the first strong acid catalyst resin vessel.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a system for treating biodiesel.    Heat exchanger (10)    Retention tank (20)    Chilled biodiesel filter (30)    Ion exchange resin vessel (40)    Finishing filter (50)
NOVELTY - Treating biomass comprises: providing lignocellulosic biomass solids in a hydrothermal digestion unit in the presence of a digestive solvent, and a supported hydrogenolysis catalyst containing sulfur, molybdenum or tungsten, and cobalt and/or nickel, incorporated into a group 4 metal oxide support; and heating the lignocellulosic biomass solids and digestive solvent in the presence of hydrogen, and supported hydrogenolysis catalyst to form a product solution containing many oxygenated hydrocarbons.    USE - The method is useful for treating biomass (claimed) in the production of higher hydrocarbons for use in transportation fuels and industrial chemicals from biomass.    ADVANTAGE - The method utilizes hydrogenolysis catalyst that: retains a crush strength (at least 0.25 kg, preferably at least 0.4 kg) of at least 50%, preferably at least 60% after being subjected to an aqueous phase stability test compared with before the aqueous phase stability test; and further maintains stability and activity with minimal loss of structural integrity during the aqueous phase reactions. The method controls the degradation of carbohydrate in the hydrogenolysis process, while hydrogenation reactions can be conducted along with the hydrogenolysis reaction at 150 degrees C to less than 300 degrees C, thus, a separate hydrogenation reaction section can optionally be avoided and the fuel forming potential of the biomass feedstock fed to the process can be increased, and thus the method results in a capital cost savings and process operational cost savings.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a composition comprising the lignocellulosic biomass, the hydrogenolysis catalyst, water and digestive solvent.
NOVELTY - Co-producing lube base stock and transportation fuel from a feedstock of biological origin, involves: a) converting a feedstock of biological origin to a ketone or a dimer acid in the presence of a first catalyst; and b) hydrogenating the ketone or the dimer acid to produce a hydrocarbon in the presence of a second catalyst comprising a hydrogenation catalyst and a hydrothermally stable binder.    USE - For co-producing lube base stock and transportation fuel from a feedstock of biological origin (claimed).    ADVANTAGE - The co-production method: 1) expand jet fuel production; 2) satisfies regulatory requirement for renewable diesel; and 3) produce different viscosity base stocks that are not readily available from current processes. In addition to offering high quality products, simultaneous production will not only reduce capital investment but also potentially save on operating cost via process integration.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a lube base stock prepared from a biologically derived oil having a viscosity of 4-100 cSt at 100 degrees C, a viscosity index of 90-160, an oxygen content of less than 10 ppm and a pour point less than 0 degrees C;    (2) a jet fuel prepared from a biologically derived oil having a freezing point of less than -40 degrees C, a smoke point greater than 25 mm, an oxygen content of less than 10 ppm, and a heat of combustion at least 43 kJ/g; and    (3) a diesel fuel prepared from a biologically derived oil having a cloud point of less than -10 degrees C, a cetane number greater than 50, an oxygen content of less than 10 parts per million (ppm), and a heat of combustion at least 40 kJ/g.
NOVELTY - Obtaining biofuel from lignocellulosic and/or amylaceous biomass, comprises (a) performing reduction of particles of the lignocellulosic and/or amylaceous biomass, (b) performing fermentation of the mash using microorganisms for producing and modulating production of enzymes that degrade lignin, cellulose and hemicelluloses, followed by fermentation using microorganisms, preferably Bacillus ssp. and 2-10% of microorganisms of the Saccharomyces spp., and (c) performing extraction of alcohols.    USE - The method is useful for obtaining biofuel from lignocellulosic and/or amylaceous biomass (claimed) for production of sugars converted into alcohols.    ADVANTAGE - The method enables economical production of biofuel with less energy consumption and without using biomass pretreatment steps using acids, alkalis and isolated enzymes.    DETAILED DESCRIPTION - Obtaining biofuel from lignocellulosic and/or amylaceous biomass, comprises (a) performing reduction of particles of the lignocellulosic and/or amylaceous biomass, (b) performing fermentation of the mash using microorganisms for producing and modulating production of enzymes that degrade lignin, cellulose and hemicelluloses at temperature of 10-80 degrees C and pH of 2-12, followed by fermentation using microorganisms, preferably Bacillus ssp. at temperature of 10-50 degrees C and pH of 2-12 and 2-10% of microorganisms of the Saccharomyces spp. at temperature of 10-60 degrees C and pH of 2-12, and (c) performing extraction of alcohols.
NOVELTY - The method involves mixing low-temperature carbonization gas with oxygen content. Pulverized coal is made to put in a pulverized coal burner of a power boiler assembly. The low-temperature carbonization gas is discharged into a combustion chamber. A coal cooling process is performed at temperature of 60 degree Celsius. A drying process is performed. Drying gas is discharged into a rotary exhaust gas boiler. A rotating chamber is connected to a power boiler to flow out liquid fuel.    USE - Waste biodegradable or non-biodegradable combustion material manufacturing method.
NOVELTY - Preparing semi-carbonized biomass pulverized fuel comprises placing biomass raw material comprising cellulose, hemicellulose and lignin as main component in a sealed semi-coking chamber, semi-carbonizing the biomass raw material at specific temperature, and drying for 20-40 minutes to obtain semi-carbonized biomass fuel, and pulverizing the semi-carbonized biomass fuel.    USE - The method is useful for preparing semi-carbonized biomass pulverized fuel (claimed).    ADVANTAGE - The biomass pulverized fuel: can replace the liquid fuel including whale-oil, paraffin and bunker oil and solid fuel including coal and coke as an alternative fuel; has glass particle shape, high calorific value and fast-ignition combustion rate; contains less than 1% moisture content and average calorific value of more than 5200 kcal; and is environmentally friendly and clean fuel in comparison with conventional solid fuels or liquid fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the semi-carbonized biomass pulverized fuel prepared by the above mentioned method.
NOVELTY - An isolated variant of a parent cellobiohydrolase (CBH) enzyme, where the variant has cellulase activity, has at least 80% sequence identity to SEQ ID NO. 3, shown in Figure 1 given in the specification, and has significantly improved performance in a Whole Hydrolysate Acid-Pretreated Corn Stover (whPCS) Assay and a Dilute Ammonia Corn Stover (daCS) assay over the parent CBH enzyme, is new.    USE - The CBH variant is useful for hydrolyzing a cellulosic substrate, for making a detergent composition and a feed additive (all claimed), and for producing ethanol.    ADVANTAGE - The CBH variant has improved properties including but not limited to altered temperature-dependent activity profiles, thermostability, pH activity, pH stability, substrate specificity, product specificity, and chemical stability. The detergent composition comprising CBH variant exhibits enhanced cleaning ability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated polynucleotide comprising a polynucleotide sequence encoding a variant of a parent CBH polypeptide above;    (2) a vector comprising the isolated polynucleotide of (1);    (3) a host cell comprising the isolated polynucleotide, vector or expression vector above;    (4) a method of producing a variant CBH polypeptide;    (5) a method for hydrolyzing a cellulosic substrate by contacting the substrate with an isolated variant CBH polypeptide above; contacting the substrate with a host cell of (3); or a combination of both;    (6) a cell culture supernatant comprising a CBH variant above; and    (7) a method of producing a cell culture supernatant comprising a CBH variant by culturing the host cell of (3) under suitable conditions to express the CBH variant; and collecting the cell culture supernatant of the culture, thus producing a cell culture supernatant comprising the CBH variant.
NOVELTY - Producing renewable material involves: (a) converting biologically a hemicellulose-derived material to form a first mixture comprising a first renewable material; and (b) converting a substantial amount of a material comprising cellulose and lignin in the presence of at least a portion of the first mixture to form a second mixture comprising a second renewable material.    USE - The method is useful for producing renewable material (claimed).    ADVANTAGE - The process can result in requiring less fermentation reactor volume thus reducing the overall capital expenditure of an ethanol production facility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for producing ethanol from lignocellulosic feedstock which involves: (a) hydrolyzing in the presence of water the feedstock comprising lignin, cellulose and hemicellulose to form a liquid portion comprising xylose and a solids portion comprising cellulose and lignin; (b) separating at least a substantial amount of the liquid portion from the solids portion to form a liquid fraction and a solids fraction; (c) contacting the liquid fraction with a fermentation organism to form a first mixture comprising ethanol; (d) mixing the solid fraction of step (b) with at least a portion of the first mixture generated in step (c) to form a slurry; and (e) contacting the slurry of step (d) with an enzyme and the fermentation organism to form a second mixture comprising ethanol.
NOVELTY - The method involves processing a biomass feedstock. The biomass feedstock is grinded and crushed at 60-80 degrees C to obtain a dry biomass feedstock. The dried biomass feedstock is disintegrated into granules. Immersion hot oil is heated at 250-300 degrees C under positive pressure. The synthetic oil is collected from the biomass feedstock by a reservoir.    USE - Method for preparing high-energy liquid fuel from biomass by immersion heating process.
NOVELTY - SAPO-34 molecular sieve comprises anhydrous chemical composition containing diglycolamine, and mixture of silicon, aluminum and phosphorus.    USE - SAPO-34 molecular sieve is used in catalyst for converting oxygen-containing compound into alkene, catalyst for acid catalyzed reaction e.g. methanol-to-olefin reaction, and methane/carbon dioxide adsorption and separation material.    DETAILED DESCRIPTION - SAPO-34 molecular sieve comprises anhydrous chemical composition of formula: mDGA.(SixAlyPz)O2 (I).    DGA=diglycolamine;    m=0.03-0.25;    x=0.01-0.30;    y=0.4-0.6;    z=0.25-0.49;and    x+y+z=1.    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of SAPO-34 molecular sieve, which involves preparing initial gel mixture containing silicon dioxide, aluminum oxide, phosphorus pentoxide, water and diglycolamine, introducing the prepared mixture into a high pressure synthesis kettle and tightly-closing the kettle, increasing the temperature to 150-220 degrees C, crystallizing the initial gel mixture under self-generated pressure for 5-72 hours, separating solid product after completion of the crystallization, washing the product to be neutral with deionized water, and drying the product. The mol ratio of silicon dioxide and aluminum oxide, and phosphorus pentoxide and aluminum oxide is 0.05-1.5 and 0.5-1.5, respectively. The mol ratio of water and aluminum oxide, and diglycolamine and aluminum oxide is 5-200 and 2.5-30, respectively;    (2) catalyst for preparing alkene, which is obtained by air roasting the SAPO-34 molecular sieve;    (3) catalyst for acid catalyzed reaction, which is obtained by air roasting of the SAPO-34 molecular sieve;    (4) catalyst for preparing alkene by conversion reaction of oxygen-containing compounds, which is obtained by air roasting of the SAPO-34 molecular sieve; and    (5) methane/carbon dioxide adsorption and separation material, which is obtained by air roasting the SAPO-34 molecular sieve.
NOVELTY - Producing solutions of sugars from lignocellulosic biomass, comprises: (a) pretreating a filler comprising lignocellulosic biomass; (b) enzymatic hydrolysis of the pretreated filler and washing using cellulolytic enzymes to produce an effluent comprising a hydrolyzate containing sugar and a solid residue; (c) separating the hydrolyzate and the solid residue; (d) washing the solid residue; (e) baking the solid residue in a medium; (f) separating the solid fraction and the liquid fraction; (g) treating obtained solid fraction; and (h) enzymatic hydrolysis of obtained the solid fraction.    USE - The process is useful for producing solutions of sugars (claimed), preferably glucose.    ADVANTAGE - The process effectively transforms various types of native lignocellulosic biomass into one or more sugar solutions, with an optimal extraction of the cellulose fraction, in simple and cost-effective manner.    DETAILED DESCRIPTION - Producing solutions of sugars from lignocellulosic biomass, comprises: (a) pretreating a filler comprising lignocellulosic biomass; (b) enzymatic hydrolysis of the pretreated filler and optionally washing using cellulolytic and/or hemicellulolytic enzymes to produce an effluent comprising a hydrolyzate containing sugar and a solid residue; (c) separating the hydrolyzate and the solid residue; (d) washing and optionally drying the solid residue; (e) baking the washed and dried solid residue in a medium comprising at least one hydrated inorganic salt of formula (MXn.n1aH2O) to obtain a solid fraction and a liquid fraction; (f) separating the solid fraction and the liquid fraction obtained in step (e); (g) optionally treating the solid fraction obtained in step (f); and (h) enzymatic hydrolysis of the solid fraction obtained in step (f) and/or (g).    M = a metal comprising 1-13 of the periodic table;    X = an anion;    n = 1-6; and    n1a = 0.5-12.
NOVELTY - The manufacturing method involves stacking and compression-molding a first thermoplastic resin sheet and a second thermoplastic resin sheet which includes 130-3200 mass parts carbonaceous material with respect to 100 mass parts of thermoplastic resins so that the outermost surface may turn into a surface which is coated by the paste of the first thermoplastic resin sheet. The paste contains 10-100 mass parts of dispersion medium to the surface of the first thermoplastic resin sheet whose 50-100 mass % of carbonaceous material is fibrous carbon.    USE - Manufacturing method for fuel cell separator.    ADVANTAGE - Ensures simple manufacture of fuel cell separator with excellent mechanical characteristic and electroconductivity.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of a fuel cell separator.    Fuel cell separator (1)    Groove (2)    Layers (41,42)
NOVELTY - A green microalgae diesel treatment method involves preparing a crude bio-oil and hydrogenated pretreating crude bio-oil. The pretreated bio-oil is catalytic hydrogenated to obtain liquid hydrocarbon fuel green diesel.    USE - Method for treating green microalgae diesel.    ADVANTAGE - The method enables treating the green microalgae diesel in an eco-friendly manner with low viscosity, high calorific value and good thermal stability.
NOVELTY - A biodiesel and hydrogenated coal tar high cetane diesel oil production method involves mixing biodiesel and coal tar feedstock with hydrogen, sequentially hydrotreating the mixture to obtain a product effluent. The effluent is cooled and subjected to a high pressure separation and fractionation to obtain a light oil fraction and high cetane diesel distillate.    USE - Method for producing biodiesel and hydrogenated coal tar high cetane diesel oil.    ADVANTAGE - The method enables reducing the difficulty of the hydrogenation of coal tar, reducing the equipment required, the investment and operating cost and improving diesel quality.
NOVELTY - Biogas slurry insecticide composition comprises 99.5-99.8 wt.% biogas slurry and 0.2-0.5 wt.% insecticidal composition. The insecticidal composition comprises sulfoxaflor and flufiprole in a weight ratio of 1:1-8.    USE - Biogas slurry insecticide composition in the form of emulsion or powder, is used for preventing and treating aphids (claimed).    ADVANTAGE - The insecticide has no residue, and good aphid killing effect. It reduces agrochemical using amount, reduces environmental risk and promotes growth of crops.
NOVELTY - The method involves performing pyrolysis of organic compound containing substance. The tar compounds are provided with pyrolysis gas and pyrolysis residual substance. The thermal decomposition of the tar compounds is performed. The decomposing products containing process gas is generated from the thermal decomposition of the tar compounds. The gasification of pyrolysis residual substance with the process gas is performed for forming product gas. The oxygen-containing gas is supplied.    USE - Method for removing organic compounds containing materials e.g. biomass formed from tar compounds during pyrolysis in fluidized bed reactor.    ADVANTAGE - The cold gas efficiency is improved. The loss of pyrolysis residual substance can be avoided. The heat loss can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a reactor.    DESCRIPTION OF DRAWING(S) - The drawings show a block diagram illustrating the process for removing organic compound and a sectional view of the reactor.    Reactor (3)    Cylindrical base portion (4)    Reactor spaces (5-7)    Supply device (8)    Outlet (14)
NOVELTY - Biodigester has a subsystem with two chambers, a V-shaped valve (4), a pressure controlling valve (3). A series of horizontal perforated pipe is attached to a bottom vertical pipe connection provided for communicating with both chambers. A draining pipe (9) is provided for flowing liquid substrate (6) and solid substrate (7).    USE - Biodigester used for producing biogas.    ADVANTAGE - The biodigester enables to increase biogas generation by increasing pressure of gas in a chamber for proper flow of materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biodigester.    Pressure controlling valve (3)    V-shaped valve (4)    Feeding pipe (5)    Flowing liquid substrate (6)    Solid substrate (7)    Draining pipe (9)
NOVELTY - An alternative gas production from synthesis gas, feeding hydrogen gas (H2), carbon monoxide (CO), carbon dioxide (CO2) and water in high temperature methanation unit, feeding in low temperature methanation unit comprising m-stage reactor at m is greater than or equal to 2 excluding last stage to produce outlet stream which is fed to low temperature methanation unit comprising single stage reactor, and adding carbon dioxide and stream 1 containing 40-100% carbon dioxide, 0-60% hydrogen gas and 0-20% carbon monoxide.    USE - Preparation of natural gas alternative (claimed).    ADVANTAGE - The syngas has good stability and high quality, and method has high yield, is efficient and requires short time.    DETAILED DESCRIPTION - An alternative gas production from synthesis gas by feeding raw gases containing hydrogen gas, carbon monoxide, carbon dioxide and water in high temperature methanation unit, feeding in low temperature methanation unit comprising m-stage reactor at m is greater than or equal to 2 excluding last stage to produce outlet stream which is fed to low temperature methanation unit comprising single stage reactor, and adding hydrogen gas and stream 1 containing 40-100% carbon dioxide, 0-60% hydrogen gas and 0-20% carbon monoxide. Ratio hydrogen gas-carbon dioxide mixture/carbon monoxide-carbon dioxide mixture is not less than 3, and volume ratio of stream 1 to low temperature methanation reactor stream is not less than 0-0.5.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparing alternative gas using double low temperature methanation reactor.    Low temperature methanation reactor inlet gas (9)    Low temperature methanation reactor outlet gas (10)    Double low temperature methanation reactor outlet gas (11)    Supplementing stream (13)    Water (14)
NOVELTY - An alternative to the production of synthesis gas methanation method by feeding hydrogen gas (H2), carbon monoxide (CO), carbon dioxide (CO2) and water (H2O) in high temperature methanation reactor comprising greater than or equal to 2 in stages except final stage of reactor to produce outlet stream which is fed to primary reactor inlet to produce effluent streams Vn, Vn' and Vn'', compressing effluent stream Vn' in 1st stage of reactor, recycling, feeding to low temperature methanation unit comprising greater than or equal to 2 m stages except final stage to produce effluent stream which is fed to next reactor, and supplementing carbon dioxide.    USE - Preparation of natural gas alternative (claimed).    ADVANTAGE - The method consumes less energy and has controllable conditions, and synthesis gas has good quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of substitute natural gas using double temperature methanation reactor.    Raw synthesis gas (1)    High temperature methanation reactor feed synthesis gas (2)    Double high temperature methanation reactor feed synthesis gas (3)    Mixed stream (4)    High temperature methanation reactor feed gas (5)
NOVELTY - Recombinant polypeptide comprising an amino acid sequence i.e. at least 55% identical to the amino acid sequence of SEQ ID NO:2 (a 333 amino acid sequence fully defined in the specification) or SEQ ID NO:3 (a 300 amino acid sequence fully defined in the specification), is new, where the polypeptide has beta -mannanase activity.    USE - The recombinant polypeptide is useful in an enzyme composition, producing a beta -mannanase and hydrolyzing a lignocellulosic biomass substrate to produce glucose and other sugars (all claimed).    ADVANTAGE - The recombinant polypeptide converts a wide variety of plant-based and/or other cellulosic or hemicellulosic materials into fermentable sugars with improved efficacy, fermentable sugar yields and/or capacity to act on a greater variety of cellulosic feedstock. The recombinant polypeptide produces the beta -mannanase in a cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an enzyme composition comprising the recombinant polypeptide, and further comprising one or more cellulases or one or more other hemicellulases;    (2) a nucleic acid encoding the recombinant polypeptide;    (3) an expression vector comprising the nucleic acid in operable combination with a regulatory sequence;    (4) a host cell comprising the expression vector;    (5) a composition comprising the host cell and a culture medium;    (6) producing a beta -mannanase, comprising culturing the host cell in a culture medium, under suitable conditions to produce the beta -mannanase;    (7) a composition comprising the beta -mannanase produced in accordance with the method in supernatant of the culture medium;    (8) hydrolyzing a lignocellulosic biomass substrate, comprising contacting the lignocellulosic biomass substrate with the polypeptide or the compositions, to yield glucose and other sugars; and    (9) a composition comprising the recombinant polypeptide and a lignocellulosic biomass substrate.
NOVELTY - An enzyme composition comprises a recombinant polypeptide comprising an amino acid sequence that is at least 80% identical to the amino acid sequence of fully defined 395 amino acids (SEQ ID NO: 2) or fully defined 364 amino acids (SEQ ID NO: 3), both given in the specification, where the polypeptide has beta-mannanase activity, and one or more cellulases.    USE - The enzyme composition and methods are useful for producing a beta-mannanase; and for hydrolyzing a lignocellulosic biomass substrate (all claimed).    ADVANTAGE - The enzyme composition is capable of, in conjunction with commercial, newly identified, or engineered cellulases and other hemicellulases, converting a wide variety of plant-based and/or other cellulosic or hemicellulosic materials into fermentable sugars with sufficient or improved efficacy, improved fermentable sugar yields, and/or improved capacity to act on a greater variety of cellulosic feedstock.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a nucleic acid encoding the recombinant polypeptide comprising an amino acid sequence that is at least 80% identical to SEQ ID NO: 2 or to the mature sequence of SEQ ID NO: 3, where the recombinant polypeptide has beta-mannanase activity;    (2) an expression vector comprising the nucleic acid in operable combination with a regulatory sequence;    (3) a host cell comprising the expression vector;    (4) a method of producing a beta-mannanase, comprising: culturing the host cell in a culture medium, under suitable conditions to produce the beta-mannanase;    (5) a composition comprising the host cell and a culture medium; and the beta-mannanase in supernatant of the culture medium; and    (6) a method for hydrolyzing a lignocellulosic biomass substrate, comprising: contacting the lignocellulosic biomass substrate with the enzyme composition, to yield glucose and other sugars.
NOVELTY - An enzyme composition comprises a recombinant polypeptide comprising an amino acid sequence that is at least 70% identical to the amino acid sequence of fully defined 493 amino acids (SEQ ID NO: 2) or fully defined 461 amino acids (SEQ ID NO: 3), both given in the specification, where the polypeptide has beta-mannanase activity, and one or more cellulases.    USE - The enzyme composition and methods are useful for producing a beta-mannanase; and for hydrolyzing a lignocellulosic biomass substrate (all claimed).    ADVANTAGE - The enzyme composition is capable of, in conjunction with commercial, newly identified, or engineered cellulases and other hemicellulases, converting a wide variety of plant-based and/or other cellulosic or hemicellulosic materials into fermentable sugars with sufficient or improved efficacy, improved fermentable sugar yields, and/or improved capacity to act on a greater variety of cellulosic feedstock.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a nucleic acid encoding the recombinant polypeptide comprising an amino acid sequence that is at least 70% identical to SEQ ID NO: 2 or to the mature sequence of SEQ ID NO: 3, where the recombinant polypeptide has beta-mannanase activity;    (2) an expression vector comprising the nucleic acid in operable combination with a regulatory sequence;    (3) a host cell comprising the expression vector;    (4) a method of producing a beta-mannanase, comprising: culturing the host cell in a culture medium, under suitable conditions to produce the beta-mannanase;    (5) a composition comprising the host cell and a culture medium; and the beta-mannanase in supernatant of the culture medium; and    (6) a method for hydrolyzing a lignocellulosic biomass substrate, comprising: contacting the lignocellulosic biomass substrate with the enzyme composition, to yield glucose and other sugars.
NOVELTY - A particulate-form neutron absorber has an average particle diameter of 7 mm or less, and a density to settle in water.    USE - Particulate-form neutron absorber is used for slurry for critical prevention method (all claimed) of debris generated from fuel cell of nuclear power reactor.    ADVANTAGE - The particulate-form neutron absorber easily prevents recryticality of fissionable substance and nuclear power reactor accident, and is manufactured with uniform particle size.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of particulate-form neutron absorber;    (2) particulate-form neutron absorber-containing slurry; and    (3) critical prevention method of debris.
NOVELTY - Biogas plant (1) comprises a hydrolysis reactor, a fermenter (3), a biogas outlet arrangement on the fermenter, a conveying device for conveying biomass from the hydrolysis reactor into the fermenter, and a discharge device for discharging the fermentation mass from the fermenter. The hydrolysis reactor is designed as a mixing tank (2). The mixing tank is assembled with the fermenter such that a common partition wall (6) is formed in a region between the mixing tank and the fermenter. The partition wall in the operating state of the biogas plant is contacted with the biomass in the tank.    USE - Used as a biogas plant.    ADVANTAGE - The biogas plant has a simple design.    DETAILED DESCRIPTION - Biogas plant (1) comprises a hydrolysis reactor, a fermenter (3), a biogas outlet arrangement on the fermenter, a conveying device for conveying biomass from the hydrolysis reactor into the fermenter, and a discharge device for discharging the fermentation mass from the fermenter. The hydrolysis reactor is designed as a mixing tank (2). The mixing tank is assembled with the fermenter such that a common partition wall (6) is formed in a contact region between the mixing tank and the fermenter. The partition wall in the operating state of the biogas plant is contacted with the biomass in the mixing tank on one side and with the fermentation mass in the fermenter on the other side such that heat transfer is carried out from the fermentation mass by the partition wall in the biomass of the mixing tank.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic side view of the biogas plant.    Biogas plant (1)    Mixing tank (2)    Fermenter (3)    Partition wall (6)    Concrete floor (7)
NOVELTY - The system (10) has feeding unit (15) that receives the biodegradable material and homogenize the biodegradable material. A container (20) holds the biodegradable material for anaerobic digestion of the biodegradable material. The container has an inlet port (60) connectable with the feed unit for receiving the homogenized biodegradable material, and outlet port (70) that discharges the biogas produced. A gas storage assembly (40) is in fluid communication with the container and has a tank (45) made up of adsorbent for adsorbing the biogas.    USE - Production system for biogas made by anaerobic digestion of biodegradable material, and used in households.    ADVANTAGE - Provides a compact and portable system for generation of energy from biodegradable material, by providing a gas storage assembly which has a tank made up of adsorbent for adsorbing the biogas, so to store large amount of biogas within small volume, thus, the system can be deployed on households and allowing efficiently manage the waste generated at a household.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the production system of biogas by anaerobic digestion of biodegradable material.    Biogas production system (10)    Feeding unit (15)    Container (20)    Gas storage assembly (40)    Tank (45)    Inlet port (60)    Outlet port (70)
NOVELTY - Preparing resorcinol by using solvent-m-phenylenediamine hydrolysis involves heating m-phenylenediamine, ether solvent, catalyst, polymerization inhibitor and inorganic strong acid according to the mole ratio of 1:3.3:0.01:0.002:3.5 respectively at 80 degrees C, stirring for 1 hours, heating to 140-160 degrees C, and pressurized to 1.2-1.5MPa, and then hydrolyzing for 5 hours, cooling to 40 degrees C to obtain layered material, removing the organic phase containing solvent by using vacuum distillation and to obtain resorcinol crude product.    USE - For preparing resorcinol (claimed) which is widely applied to rubber, medicine, pesticide, dye chemical agent and photo-sensitive material; and also used in the preparation of benzophenone ultraviolet absorbent, dye, synthetic resin, and flame retardant explosive.    ADVANTAGE - The present process provides resorcinol with high yield and purity; has low requirement of relative device; and is green and environment-friendly.
NOVELTY - The organic combustion propagator includes light charcoal or firewood, grills and other, where a spreader is obtained from a mixture of two components. The former component is monocot plant of subclass zingiberidae, where wax acts as fuel and vegetable as oxidizing agent.    USE - Organic combustion propagator for barbecue.    ADVANTAGE - The organic combustion propagator ensures long lasting flames without commonly encountered problems such as toxicity, smoke or odor.
NOVELTY - Purifying heavy metal wastewater comprises weighing gravel, natural zeolite and modified zeolite according to a ratio of 3:1:1 and then mixing with composite filler and emergent plants including Canna, Acorus and cattail by a constructed wetland, an ecological floating bed including dry umbrella grass and rhizoma acori graminei and an aquatic pond including Hyacinthus, black algae and fox tail algae, and collecting heavy metal wastewater and then processing for 3-4 days by a purification treatment process.    USE - The method is useful for purifying heavy metal wastewater to produce biochar (claimed).    ADVANTAGE - The method is capable of simply purifying heavy metal wastewater in an economical manner.
NOVELTY - Method for obtaining fodder protein from solid cellulose-containing wastes, involves processing waste by inoculating micromycetes into nutrient medium containing solid cellulose-containing substrate which is biologically inert and mixed with an aqueous medium phase-liquid paraffin, or their mixtures, where the concentration of the nutrient medium is 20-40 vol.%.    USE - The method is useful for obtaining fodder protein from solid cellulose-containing wastes (claimed).
NOVELTY - The device has organic waste dryer (1) which is installed with a frame. A drive motor (5) is installed at the upper portion of the frame. A vent pipe (8) and hot air inlet port (10) are respectively set at lower and upper portions of frame. The hot air of 150 degrees C is supplied forward and backward into the drying chamber (2) through hot air inlet port, while rotating drive motor (11) at predetermined speed. Multiple crush blades (14) are installed at the exterior of the shaft (13), and arranged in longitudinal direction of the drying chamber in fixed interval.    USE - Device for processing fuel using organic waste and waste fiber.    ADVANTAGE - The processing of fuel using organic waste and waste fiber can be performed efficiently at low cost. The waste resources can be recycled and the environmental contamination can be prevented. The device is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for processing fuel using organic waste and waste fiber.    Organic waste dryer (1)    Drying chamber (2)    Drive motor (5)    Vent pipe (8)    Hot air inlet port (10)    Drive motor (11)    Shaft (13)    Crush blades (14)
NOVELTY - Preparing antitumor molecular targeted drug crizotinib, comprises e.g. preparing racemic 1-phenylethanol derivative from 1-(2,6-dichloro-3-fluorophenyl)ethanone, splitting racemic 1-phenylethanol derivative into S-type and R-type alcohol using N-(tert-butoxycarbonyl)-L-proline and p-toluenesulfonic acid and 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide hydrochloride, splitting obtained byproduct mixture by hydrolysis, converting configuration, reacting with aromatic ether, reducing nitro group, brominating, carrying out addition reaction, performing acid hydrolysis, and then recrystallizing.    USE - The method is useful for preparing antitumor molecular targeted drug crizotinib (claimed).    ADVANTAGE - The method: has short production time and high product yield; and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparing antitumor molecular targeted drug crizotinib, comprises preparing racemic 1-phenylethanol derivative from 1-(2,6-dichloro-3-fluorophenyl)ethanone, splitting racemic 1-phenylethanol derivative into S-type and R-type alcohol, splitting obtained byproduct mixture by hydrolysis, and converting configuration of byproduct, reacting with aromatic ether, reducing nitro group, brominating the aromatic ring, carrying out addition reaction, performing acid hydrolysis and recrystallizing to obtain pure final product, where the splitting of racemic 1-phenylethanol derivative into S-type and R-type alcohol utilizes N-(tert-butoxycarbonyl)-L-proline and p-toluenesulfonic acid catalyst and condensing agent 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide hydrochloride.
NOVELTY - A multifunctional automatic conversion device, comprises two pieces of production control and automatic control, methane pressure transformation and automatic movement of working parts, gas pressure and groove copper gas floating cylinder, check point automatic control, and starting point of floating cylinder for automatic operation.    USE - As a multifunctional automatic conversion device (claimed).    ADVANTAGE - The multifunctional automatic conversion device aims at two variable-pressure part which are combined into a whole and a floating cylinder automatic regulator, thus the gas flow rate reaches the function of three times automatic control device, which is composed of two bulky form a whole automatic control device.
NOVELTY - The nitrogen oxide reduction type scrubber (100) has a burner (110), which generates a flame through a combustion gas supplied to a combustion gas inlet port (111). A burning chamber (120) is arranged at a lower unit of the burner. A process gas flowing through a process gas inlet port (112) is burnt with the flame generated in the burner. A methane supply port (130) provides the methane (CH4) in liquefied natural gas within the burning chamber. The air supply ports (140,150) supply the air to the burning chamber inside an upper side space unit and a lower space unit.    USE - Nitrogen oxide reduction type scrubber for removing the harmful material from a process gas released during manufacturing of a semiconductor device.    ADVANTAGE - The nitrogen oxide reduction type scrubber has a burner, which generates a flame through a combustion gas supplied to a combustion gas inlet port, thus effectively removing the process gas, preventing the reaction of combustion promotion and methane of the process gas, and reducing the cost and exhaustion of the nitrogen oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a burning chamber (120) is arranged at a lower unit of the burner.    Nitrogen oxide reduction type scrubber (100)    Burner (110)    Combustion gas inlet port (111)    Process gas inlet port (112)    Burning chamber (120)    Methane supply port (130)    Air supply ports (140,150)    Methane (CH4)
NOVELTY - The system has an excrement handling unit (20), a livestock shed (10) laid in underground, a first filter purging station (40), and a second filter purging station (50). The biogas generated in the excrement handling unit is stored after desulfurization in gas-storage tank (60) and is used as energy source of power generation with heat supply unit (80). The bad air inside livestock shed is filtered and the temperature inside the shed is set to a constant value. The bad air in the underground is cleaned up and the underground is ventilated through first filter purging station.    USE - Energy neutral type odorless underground livestock shed system.    ADVANTAGE - The livestock excretion inside the shed is aversion fermented efficiently. The need for a separate heating and cooling facility, and ventilator is avoided. Wastage of installation space above the ground is prevented. The bad smell inside the livestock shed can be completely purified.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy neutral type odorless underground livestock shed system.    Livestock shed (10)    Excrement handling unit (20)    Filter purging stations (40,50)    Gas-storage tank (60)    Heat supply unit (80)
NOVELTY - The method involves injecting the human excrement sludge, the sewage sludge, and the food waste inside a first substance input box (381) combined with a sanitary landfill (100). The liquid mixtures are introduced through a liquid pump arranged inside a second material input box (200). The liquid mixtures are contacted with the sludge, when injecting the liquid mixtures in the second material input box. The air is consecutively supplied by an air pump through an input pipe (201) so as to accelerate the production of the gas.    USE - Method for producing gas used as fossil fuel from human excrement sludge, sewage sludge, and food waste injected in sanitary landfill.    ADVANTAGE - The gas can be produced effectively by recycling the human excrement sludge, sewage sludge, and food waste. Hence, the sludge injected in the sanitary landfill can be minimized. The construction cost of the environment-friendly gas production system can be reduced. The efficiency of the gas production system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the gas production system.    Sanitary landfill (100)    Second material input box (200)    Input pipe (201)    Heat generation rod (306)    First substance input box (381)
NOVELTY - Production of organic fertilizer, involves selecting by-product of vegetable oil meal, composting the by-product of vegetable oil meal with 1 wt.% yeast, storing the semi-finished product, mixing with 10 wt.% starch, processing the mixture, drying the processed mixture, and granulating or pulverizing the dried materials to obtain granules or powder.    USE - The method is useful for production of organic fertilizer (claimed).    ADVANTAGE - The method uses the waste material as raw material, thus solves the problem of soil pollution, and produces organic fertilizer which improves the crop growth.
NOVELTY - The system has a submerged membrane module that is equipped within a bioreactor for filtering the foul water. The bioreactor filters the foul water in biological treatment space by separating film module and foul water. A rotary disc is equipped within the bioreactor for inducing the turbulence of foul water with the rotation of rotary disc. The mobility filter media is flown according to flow of foul water. A bio-filter is formed on surface for biologically processing the contaminant of mobility filter media.    USE - Fluidized bed anaerobic wastewater treatment method.    ADVANTAGE - The contamination of submerged membrane module can be reduced effectively. The energy consumption of submerged membrane module can be reduced effectively by operating the bioreactor in anaerobic condition. The energy efficiency can be improved reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane association type fluidized bed anaerobic wastewater treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fluidized bed anaerobic wastewater treatment system. (Drawing includes non-English language text)    Bioreactor (110)    Submerged membrane module (120)    Rotary disc (130)    Biogas storage tank (160)    Water level sensor (180)
NOVELTY - This fuel additive helps to maximize mileage , reduce pollution, reduce vibration and no out come of hazardous gases. This is simply prepared by diesel or bio diesel mixed with methanol and distilled at 200 for every litre of diesel or bio diesel with methanol we get only 20% fuel additive and the rest may be used again industrial for thermal application
NOVELTY - Apparatus for sewage treatment, comprises at least one tank, at least one inlet branch to the tank, at least one outlet branch from the tank, at least one microwave generator able to subject the sewage present internally of the tank to at least one temperature raising treatment, at least a cooling circuit of the microwave generator, and at least one blowing device connected to the tank, the blowing device being connected to an outlet of the cooling circuit and sending the heated gases arriving into the tank.    USE - The apparatus is useful for sewage treatment, in particular sewage of animal origin (claimed).    ADVANTAGE - The apparatus for treating sewage enables to reuse the treated sewage as a substrate for producing compost and/or biogas and/or fertilizer, and to promote following sewage depurations. It can effectively eliminate the majority of microorganisms, such as bacteria, molds, mold spores and bacteria present in the sewage. It enables an effective extraction of ammonia nitrogen from sewage; and is capable of treating sewage with reduced energy consumption in order to substantially reduce its operating costs.
NOVELTY - Process for converting phenolic feeds into aromatic hydrocarbons involves subjecting phenolic feeds to a one-pot hydrotreatment by contacting with a metal catalyst and a solid acid catalyst in absence of external supply of molecular hydrogen and in the presence of hydrogen donor in primary reactor, and recovering the obtained products from the reaction mixture.    USE - Process for converting phenolic feeds into aromatic hydrocarbons e.g. benzene, toluene and alkylbenzene for preparing synthetic biofuels, chemicals and aviation fuel additive (claimed).    ADVANTAGE - The aromatic hydrocarbon is efficiently produced at mild reaction conditions without affecting the environment.
NOVELTY - The device has a bioreactor which has a case that is made of glass, fiber, or reinforced plastic. The bioreactor has a bubbler, a biomass input unit, and a biogas outlet. An anodic element made of a nano-carbonic material is placed in a hollow loop that is made a porous plastic, and is installed in the center of the case. A cathode-mixer, which is made of an electrically conducting material, mixes and facilitates an electrochemical activation of concentration of methane in biogas.    USE - Electrochemical activation device for concentration of methane in biogas.
NOVELTY - Bioreactor element comprises a substantial longitudinal dimension and at least partially transparent wall (2) of plastic material for conveying a medium inoculated with microorganisms nutrient solution (1) for the production of biomass by photosynthesis, where the bioreactor is designed in one piece and many parallel channels (3, 4), of which at least one allows for the passage of the nutrient solution and at least one channel allows for the flow of fluid for the production of the biomass.    USE - The bioreactor element is useful for production of biomass (claimed).    ADVANTAGE - The bioreactor element enables efficient production of biomass, and can be produced in one piece in an economical manner by eliminating sealing problems.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic cross-sectional view of the bioreactor element.    Nutrient solution (1)    Transparent wall (2)    Parallel channels (6) Heating or cooling fluid (3,4)    Holding member (7)
NOVELTY - A traditional Chinese medicine tablet comprises 225 g loosestrife, 225 g capillary wormwood, 90 g turmeric, 150 g dried orange peel, 45 g skullcap, 35 g frankincense, 80 g Glauber's salt, 35 g alum, 45 g Chinese rhubarb, 45 g Scirpus fluviatilis, 45 g cape jasmine, 45 g licorice and 35 g myrrh.    USE - Traditional Chinese medicine tablet used for suppressing C127 breast cancer cell proliferation (claimed).    DETAILED DESCRIPTION - A traditional Chinese medicine tablet comprises 225 g loosestrife, 225 g capillary wormwood, 90 g turmeric, 150 g dried orange peel, 45 g skullcap, 35 g frankincense, 80 g Glauber's salt, 35 g alum, 45 g Chinese rhubarb, 45 g Scirpus fluviatilis, 45 g cape jasmine, 45 g licorice and 35 g myrrh. The traditional Chinese medicine tablet is prepared by crushing Glauber's salt and alum into fine powder with particle size of 5-45 mu m, crushing frankincense and myrrh into powder, adding supercritical carbon dioxide and ethanol as entrainer at 4-6 vol.% of extraction solvent into extractor, extracting at 30-50 degrees C with pressure of 15-30 MPa and carbon dioxide flow rate of 1-3 mL/g crude drug.minute for 180-220 minutes, obtaining supercritical extract, adding frankincense powder, myrrh powder and remaining ingredients, crushing, adding 3.6 L of 70% ethanol, microwave extracting twice at 600-800 W for 5-10 minutes each, combining extracts, concentrating, adding into Diaion HP-10 (RTM: high porous polymer ion-exchange resin) macroporous resin column, eluting with 70% ethanol at 5 times bed volume, vacuum recovering ethanol, concentrating collected eluate, drying to obtain microwave extract, mixing Glauber's salt, alum, supercritical fluid and microwave extract, adding starch and 70% ethanol, pelletizing, drying, and compressing to obtain 500 tablets at 0.3 g/tablet.
NOVELTY - A metal phase carrier-supported catalyst (I) comprises metal phase carrier, metal oxide active component and metal oxide additive.    USE - Metal phase carrier-supported catalyst is used as carbon dioxide hydrogenation catalyst for synthesis of methane for preparing synthesis gas by methane-carbon dioxide reforming and autothermal reforming of methane (all claimed).    ADVANTAGE - The metal phase carrier-supported catalyst has high activity, stability, permeability and thermal conductivity, and excellent durability, and is prepared by simple process.    DETAILED DESCRIPTION - A metal phase carrier-supported catalyst comprises metal phase carrier, metal oxide active component and metal oxide additive. The metal phase carrier-supported catalyst is of formula: xM1OyM2O/ZT (I), where M1O is active component metal oxide, M2O is metal oxide additive, ZT is metal phase carrier, x is amount (in mass) of active component metal oxide in catalyst and y is amount (in mass) of metal oxide additive in catalyst. An INDEPENDENT CLAIM is included for preparation of metal phase carrier-supported catalyst, which involves impregnating metal phase carrier in suspension containing aluminum powder, drying to make aluminum of metal particles dispersed in surface of carrier phase, performing surface alloying of metal phase carrier, extracting using 5-20 %mass aqueous solution of hydrochloric acid or sodium aluminum, washing, metal phase carrier having porous surface layer by drying, impregnating in aqueous solution containing salt of nickel and/or iron, and aluminum, cerium, lanthanum, manganese, tungsten, magnesium, calcium, sodium and/or potassium, drying at 300-600 degrees C, and calcining.
NOVELTY - A ruthenium water oxidation catalyst compound (I) is new.    USE - Ruthenium water oxidation catalyst compound used in photolysis water molecular device (claimed).    DETAILED DESCRIPTION - Ruthenium water oxidation catalyst compound of formula (I) is new.    Y'=1-4C straight-chain alkyl; and    L=ligand comprising groups of formulae (A)-(E).    An INDEPENDENT CLAIM is included for preparing compound (I).
NOVELTY - An organic fertilizer comprises nitrogen, phosphorus, potassium, magnesium, calcium, sodium, iron, copper, zinc, manganese, selenium and vitamins and growth nutrients.    USE - Organic fertilizer used for promoting plant germination (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising mixing 20-30 wt.% celery and 10-30 wt.% garlic leaves, crushing into pulpy material, crushing 30-40 wt.% straw into 5-10 cm fragments, fermenting with bacteria and brown sugar at feedstock ratio of 1:1, heating at 55-65 degrees C, stirring, maintaining adequate amount of oxygen during fermentation, adjusting pH value to 6-8, mixing, controlling pH value and temperature, collecting through discharge port, liquid fermenting for 5-7 days at 45-50 degrees C, stirring, maintaining adequate amount of oxygen during fermentation, adjusting pH value to 5.8-6.8, mixing, and controlling pH value and temperature.
NOVELTY - An organic fertilizer comprises fermented bacteria, straw and organic chelating agent.    USE - Organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising crushing 70 wt.% water hyacinth into pulpy material, crushing 30 wt.% straw into 5-10 cm fragments, adding bacteria, fermenting at 45-55 degrees C for 24 hours, degrees, stirring once every 0.5 hours, adding water at mass ratio of 1:1, 20 wt.% calcium carbonate, hydrolyzing, adding organic chelating agent, mixing, fermenting at 55-65 degrees C for 48 hours, stirring once every 2 hours, extracting, adding humic acid and calcium enzyme, dissolving 3 wt.% lime in water, placing in reaction vessel, 2 wt.% baking soda, stirring for 0.5 hour, reacting at 55-60 degrees C, extracting, and standing.
NOVELTY - A bio-organic fertilizer comprises 800-820 pts. wt. agricultural waste, 12-18 pts. wt. calcium superphosphate, 4-6 pts. wt. potassium mineral powder, 4-6 pts. wt. fermenting enzyme, 40-60 pts. wt. ore powder, 90-110 pts. wt. boron soil powder, 8-12 pts. wt. humic acid, and 4-6 pts. wt. fungus.    USE - Bio-organic fertilizer.    ADVANTAGE - The fertilizer has complete nutrients that can improve the soil and product quality, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-organic fertilizer comprising mixing all raw materials, adding 60-65 wt.% water, stirring uniformly at 15 degrees C, stacking materials at a width of 1.5-2 m and height of 0.5-0.8 m cubic material stack, providing vent holes up to the cubic material stack. When the stack temperature is raised to 50 degrees C, overturned is performed, two times a day. When the stack temperature is at greater than or equal to 65 degrees C, turning four times a day. The fermentation temperature is controlled at less than or equal to 70 degrees C, when the material has no material original odor or little ammonia odor, white mycelium is produced to prepare the fertilizer.
NOVELTY - A fertilizer comprises 20-40% manure, 5-50% composting plant stalks, 5-50% mushroom fungus waste slag, 5-10% monoammonium phosphate, and 10-30% potassium chloride.    USE - A fertilizer used for cotton seedling (claimed).    ADVANTAGE - The fertilizer is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising:    (A) granulating manure to a particle size of not greater than 5 mm;    (B) anaerobic fermenting plant stalk for 10-20 days, adding deodorant, uniformly stirring, and granulating to a particle size of not greater than 1 mm; and    (C) mixing the manure, rice stalk, mushroom fungus waste slag, monoammonium phosphate, and potassium chloride.
NOVELTY - A biological water-soluble fertilizer comprises 8-15 pts. wt. Bacillus subtilis, 38-50 pts. wt. humic acid, 5-10 pts. wt. amino acid, 2-4 pts. wt. acetic acid, 5-10 pts. wt. herbal ingredients, 18-30 pts. wt. nitrogen-phosphorus-potassium inorganic fertilizer, and 4-8 pts. wt. trace elements. Herbal ingredients include 1-2 pts. wt. yellow seedlings, 1-2 pts. wt. herba violae, 1-2 pts. wt. indochina dragon-plum fruit, 1-2 pts. wt. seaweeds, and 1-2 pts. wt. duckweeds.    USE - Biological water-soluble fertilizer.    ADVANTAGE - The fertilizer is non-toxic and harmless.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological water-soluble fertilizer comprising mixing all raw materials, fermenting, sieving to 80-100 meshes, and mixing uniformly.
NOVELTY - 2-amino-1-(2,5-dimethoxyphenyl)propan-1-one hydrochloride preparation involves dissolving 1-(2,5-dimethoxyphenyl)propan-1-one in an organic solvent in presence of hydrogen chloride gas to obtain solution, which is added drop wise in nitroxime to obtain (2E)-1-(2,5-dimethoxyphenyl)-2-(N-hydroxyimino)propan-1-one. The obtained product is dissolved in methanol in presence of palladium catalyst under acidic conditions to obtain second intermediate, which is hydrogenated to obtain desired product.    USE - Method for preparing 2-amino-1-(2,5-dimethoxyphenyl)propan-1-one hydrochloride (claimed).    ADVANTAGE - The method enables to prepare 2-amino-1-(2,5-dimethoxyphenyl)propan-1-one hydrochloride in simple, economical and environment-friendly manner.
NOVELTY - Dehydrating agent preparation involves using alpha-amylase for degrading corn starch to obtain degradable starch, and then horseradish peroxidase, hydrogen peroxide and N,N-diallyl-N,N-dimethylammonium chloride are mixed with degradable starch for performing graft copolymerization to obtain product.    USE - Method for preparing dehydrating agent used for treating sludge (claimed).
NOVELTY - A biodiesel nanoemulsion comprises 5-40 pts. wt. biodiesel, 5-25 pts. wt. nonionic surfactant and water.    USE - Biodiesel nanoemulsion used as drilling lubricant (claimed).    ADVANTAGE - The nanoemulsion has good stability. It is environmentally friendly and easy to transport.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biodiesel nanoemulsion comprising mixing biodiesel and surfactant, heating at 60 degrees C, adding water, stirring, cooling and standing.
NOVELTY - An oil and natural gas producing device comprises carbon dioxide heat preservation tank, coal screw, oxygen storage tank (15), steam storage tank, hydrogen storage tank, deaerator (14), multi-plasma torch generator, oil synthesizer (6), purification separator (7), microwave fractionator (8), methane generator, cooler, gasoline tank, and diesel tank.    USE - Oil and natural gas producing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of oil and natural gas producing device.    Oil synthesizer (6)    Purification separator (7)    Microwave fractionator (8)    Deaerator (14)    Oxygen storage tank (15)
NOVELTY - A biodiesel is produced by using catalytic distillation tower system composed of catalytic distillation tower which is plate-type in which tower plate (11) is floating valve tray or sieve tray disk, mixing inferior oil (1) and acid catalyst (2), adding obtained mixture on top of distillation tower, feeding alcoholic substance (3) to bottom of catalytic distillation tower, heating alcohol to vaporize, reacting bottom effluent (8) of inferior oil and vaporized alcohol substance (4), and collecting bottom plate in which alcohol is 1-6 carbon-containing straight chain fatty alcohol.    USE - Production process of biodiesel (claimed).    ADVANTAGE - The process improves reaction conversion rate, reduces reaction product acid value, and obtains high alcohol concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of production process of biodiesel.    Cottonseed acidified oil (1)    Load sulfonic acid catalyst (2)    Fresh methanol (3)    Overhead methanol steam (4)    Bottom reaction effluent (8)    Tower plate (11)
NOVELTY - A biodiesel is produced by mixing inferior oil (1) and 1st alcohol substance (2), heating and pressurizing to obtain intermediate product (3), providing catalytic distillation system comprising catalytic distillation tower, mixing intermediate product and acid catalyst (4) to obtain mixture, feeding mixture on top of catalytic distillation tower, heating 2nd alcohol (5) at bottom of catalytic distillation tower to obtain vaporized alcohol material (7), reacting intermediate product and vaporized alcohol material, and collecting bottom effluent (12) product from bottom of tower plate.    USE - Production process of biodiesel (claimed).    ADVANTAGE - The process improves esterification conversion rate, reduces intermediate product acid value, and has short processing time.    DETAILED DESCRIPTION - A biodiesel is produced by mixing inferior oil and 1st alcohol substance, heating and pressurizing to obtain intermediate product, providing catalytic distillation system comprising plate-type catalytic distillation tower composed of tower plate (16) which is floating valve tray type or sieve tray disk-type, mixing intermediate product and acid catalyst to obtain mixture, feeding mixture on top of catalytic distillation tower, heating 2nd alcohol at bottom of catalytic distillation tower to obtain vaporized alcohol material, reacting intermediate product and vaporized alcohol material, and collecting bottom effluent product from bottom of tower plate which is biodiesel in which 1st and 2nd alcohol substance are 1-6 carbon containing straight chain fatty alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of production process of biodiesel.    Acidified cottonseed oil (1)    Methanol (2)    High temperature and pressure product (3)    Load sulfonic acid (4)    Fresh methanol (5)    Vaporized alcohol material (7)    Bottom effluent (12)    Tower plate (16)
NOVELTY - 2nd-generation biodiesel is produced by filtering collected waste oil, dehydrating, desalting to obtain cooking oil containing triglyceride and fatty acid components, placing in high-pressure reactor, performing hydrogenation refining with transition metal phosphide catalyst at 200-480 degrees C with hydrogen pressure of 0.5-10 MPa and hydrogen:oil volume ratio of 10-2000 for 4-6 hours, separating in gas-liquid separation device to obtain liquid product and gas product, separating liquid product in oil-water separation device to obtain crude product, and separating glycerol.    USE - Production of 2nd-generation biodiesel (claimed).    ADVANTAGE - 2nd-generation biodiesel has low pour point and high cetane number, preparation is simple, clean, and environment-friendly and has low power consumption, and catalyst has excellent hydrogenation property and good selectivity, and reduces hydrogen consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of transition metal nickel phosphide catalyst which involves preparing 120 ml dipping solution containing 75.5 g nickel hypophosphite, impregnating 100 g macroporous silicon dioxide (SiO2) carrier in dipping solution, standing at room temperature for 2 hours, placing in vacuum drying box at 60 degrees C for 4 hours to obtain sample, placing in tube furnace, and processing under nitrogen at 250 degrees C for 3 hours to obtain catalyst of formula Ni2P/SiO2.
NOVELTY - Marsh gas preparation involves crushing natural peat to 40-200 meshes. The obtained crushed powder is added with alkali liquid (1-3%). The mixture is heated at 80-100 degrees C for 0.5-3 hours, where the pH of the mixture is 7-8. The mixture is added with urea and active sludge (30-80 wt.%). The mixture is fermented at 30-55 degrees C for 5-40 days to obtain desired product, where the content of marsh gas is measured.    USE - Method for preparing marsh gas (claimed).
NOVELTY - Biofuel preparation involves utilizing grass and macroalgae.    USE - Method for preparing biofuel (claimed).    ADVANTAGE - The method enables to prepare stable biofuel.
NOVELTY - This utility new type claims a one composite semi-permeable filter film, in turn is terylene base layer from the outer to the inner, polytetrafluoroethylene layer and inner layer terylene base layer, the outer layer terylene base layer upper surface is coated with poly-ether sulfone layer, lower surface of inner layer terylene base layer is coated with poly-ether sulfone layer between the adjacent layer through adhesive bonding, wherein the outer layer polyester base layer and inner layer terylene is terylene weaving of grid structure. The composite semi-permeable film can filter the dust, bacteria, and keep odour, forming the microorganism activity required environment and is capable of the kitchen garbage, sludge and other organic waste into high quality fertilizer or drying, which greatly reduces the building scale and device investment of cost and for peripheral atmospheric environment does not have any influence, it is not only economic and environment-friendly.
NOVELTY - Metal corrosion inhibitor comprises 30-40 wt.% imidazoline derivative, 5-10 wt.% dimer acid, 3-7 wt.% polyaspartic acid, 3-10 wt.% benzoxazole, 1-5 wt.% organic amine, 2-6 wt.% nitrogen-containing heterocyclic compound, 0.05-0.10 wt.% metal ion deactivator, and balance dispersant.    USE - Metal corrosion inhibitor used for methanol fuel vehicle.    ADVANTAGE - The metal corrosion inhibitor is suitable for different metal corrosion and corrosion inhibition including copper, brass, No. 45 steel, stainless steel, aluminum, zinc, or tin. It contains fewer additives, is non-toxic and pollution-free, and is environment friendly.
NOVELTY - Vegetable oil is prepared by cleaning oilseed, removing impurity, regulating oilseed moisture content by cyclone airflow drier, separating skin and seed, hardening, tempering, extracting crude oil, performing supercritical degumming, adsorption deacidifying by fixed bed adsorption of free fatty acid using microcrystalline cellulose derivatives, adsorption dehydrating by fixed bed adsorption of water using anhydrous microcrystalline cellulose, and filtering vegetable oil.    USE - Preparation of vegetable oil for fuel.    ADVANTAGE - The preparation of vegetable oil is environmental-friendly, and has high drying efficiency, short drying time, low energy consumption, and excellent product quality. Fixed beds used are recyclable and has simple operation, low energy consumption, and high efficiency dehydration and/or deacidification.    DETAILED DESCRIPTION - Vegetable oil is prepared by cleaning oilseed, removing impurity, regulating oilseed moisture content by cyclone airflow drier, separating skin and seed, hardening, tempering, extracting crude oil, performing supercritical degumming, adsorption deacidifying by fixed bed adsorption of free fatty acid using microcrystalline cellulose derivatives, adsorption dehydrating by fixed bed adsorption of water using anhydrous microcrystalline cellulose, and filtering vegetable oil in which microcrystalline derivative is prepared by selecting food grade anhydrous microcrystalline cellulose, adding 10-35 wt.% food grade sodium hydroxide, potassium hydroxide, sodium carbonate, and/or potassium carbonate, grinding, dispersing, microwave treating for 3-15 minutes, vacuum cooling to 20-40 degrees C, and crushing to 100-200 mesh particle size.
NOVELTY - A biodiesel is prepared by adding primary oil with 9-11.5 mg KOH/g acid value in reaction container, performing alkali treatment, adding activated carclazyte to obtain primary oil with 3 mg KOH/g acid value, performing transesterification reaction on pretreated primary oil, methanol, and catalyst, standing to separate layers in which upper layer is biodiesel and lower layer is methanol, recovering methanol by decompression, adding carclazyte which is 0.5-5 mass% of primary oil, stirring at 80-120 degrees C for 20-60 minutes to obtain biodiesel primary product, and adding stabilizing agent.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The preparation avoids large amount of wastewater, reduces free fatty acid, removes alkali and acid reaction, and obtains product which is free from soap and impurity and has increased stability.
NOVELTY - Wastewater treatment comprises placing ozone catalytic oxidation device in external sludge thickener, oxidizing for 100-150 minutes, controlling suspended solid content to 0.05-0.08 g, performing sludge reduction, removing heavy metals, filtering sludge, dewatering with flocculant to sludge moisture content of 40-60%, drying to water content of 10-20%, removing heavy metals, adding primary fertilizer, modified attapulgite clay and manure, mixing, fermenting, extruding, granulating, and packaging.    USE - Wastewater treatment.
NOVELTY - A composite fertilizer comprises 15-25 wt.% nitrogen, 10-15 wt.% phosphorus, 8-10 wt.% potassium, 5-10 wt.% chicken manure, 6-10 wt.% potassium nitrate, 10-18 wt.% humic acid, and balance ash. The nitrogen, phosphorus, potassium, mixed chicken manure fermentation, in proportion to the nitrogen, phosphorus, potassium, nitrate, potassium chloride , humic acid and ash added to the good chicken manure fermentation, are mixed and pelletized, and the resulting granules are cooled.    USE - Composite fertilizer used for crops, e.g. maize, rice, or sorghum.    ADVANTAGE - The fertilizer has increased production efficiency.    DETAILED DESCRIPTION - A composite fertilizer comprises 15-25 wt.% nitrogen, 10-15 wt.% phosphorus, 8-10 wt.% potassium, 5-10 wt.% chicken manure, 6-10 wt.% potassium nitrate, 10-18 wt.% humic acid, and balance ash. The nitrogen, phosphorus, potassium, mixed chicken manure fermentation, in proportion to the nitrogen, phosphorus, potassium, nitrate, humic acid and ash added to the good chicken manure fermentation, are mixed and pelletized, and the resulting granules are cooled.
NOVELTY - A fertilizer comprises 20-40 mass% granular manure, 10-50 mass% granular plant straw, 10-50 mass% ferrous sulfate, and 10-30 mass% monoammonium phosphate.    USE - A fertilizer used for alkaline soil (claimed).    ADVANTAGE - The fertilizer has improved plant straw utilization ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising:    (A) granulating manure to obtain a particle size of not more than 5%, and drying to obtain a moisture content of 15%;    (B) carrying out anaerobic fermentation of plant straw for 10-20 days, adding deodorant, stirring, granulating, sieving, and drying to obtain a moisture content of less than 20%; and    (C) uniformly mixing granular manure, granular plant straw, ferrous sulfate, and monoammonium phosphate.
NOVELTY - This utility new type claims a one anti-shell marsh pneuma tank, include with an inner cavity of a tank body, a tank body upper part of the inner cavity of lower part of the inner cavity of the pneuma room, the tank body of fermentation room, the tank body set with upper room connected with the fermentation of feeding tube, a discharge hole and gas-guide tube, a fermentation room is set in the anti - . A - proof structure is set on the biogas liquid level low, this utility new type anti - of the liquid is set on the lower surface, the intercepting the slag liquid surface following can be valid to prevent slag floating on the liquid surface of upper crust, and slag is always in the marsh gas-liquid, good fermentation effect. And the anti - end is set two adjustable fixing upper layer between the pool wall along pool wall upper lower, time up when the biogas slurry liquid surface low change, it can adjust anti - to make the in. This utility new type low investment, high fermentation rate, the structure is simple, it only needs on the basis of common marsh gas tank up and one of anti - , is very good for popularization and application.
NOVELTY - This utility new type relates to a large medium marsh gas project one automatic control system, said automatic control system for large-middle biogas engineering include fermentation system and control system, a fermentation system comprise preprocessing pool, an anaerobic fermenting tank, a marsh gas purifier, a gas storage cabinet pneuma and marsh liquid pool, said control system comprise PLC programming device and computer, a PLC programmer with the computer system for electrically connecting. This utility new type is equipped with on-line flow meter, on-line measuring the engineering device of each link, pressure meter, on-line gas analyzer and an online thermometer to monitor working state of engineering device, and the measured working condition of data transmission to the PLC programmer, and visual display of the upper computer, at the same time, the computer can also send commands to the PLC programmer, timely and valid of monitoring, adjusting the working state of each link in the engineering device, increases the controllability of the engineering device, and improves the operation management level of marsh gas, time saves time and labour force and is suitable for popularization use.
NOVELTY - A one pot process for preparation of cephalothin sodium involves: i) reacting 7-aminocephalosporanic acid with 2-thienylacetyl chloride in the presence of an amine in a solvent at a temperature; ii) optionally, treating reaction mixture as obtained from step (i) with activated carbon; and iii) adding a sodium ion source solution in a solvent to the reaction mixture as obtained from step (i) or step (ii) at a temperature to obtain cephalothin sodium.    USE - As one pot process for the preparation of cephalothin sodium (claimed) used as antibiotic having broad spectrum of antibiotic activity for treating systemic infections caused by susceptible microorganisms such as both gram-positive and gram-negative bacteria.    ADVANTAGE - The method uses non-hazardous materials and hence is applicable for industrial scale production of the compound. The method is simple, cost effective, commercially viable, sustainable, eco-friendly, and free from impurities. The method avoids multistep synthesis; provides cephalothin sodium in high yield and high purity; and forms compound free from impurities.    DETAILED DESCRIPTION - A one pot process for the preparation of cephalothin sodium of formula (II) involves at least one of the following steps individually or in the given sequence: i) reacting 7-aminocephalosporanic acid of formula (III) with 2-thienylacetyl chloride of formula (IV) in the presence of an amine in a solvent at a temperature; ii) optionally, treating reaction mixture as obtained from step (i) with activated carbon; and iii) adding a sodium ion source solution in a solvent to the reaction mixture as obtained from step (i) or step (ii) at a temperature to obtain cephalothin sodium (II).
NOVELTY - The device has minuteness bubble emissive elements (400) that are connected to the gas supply line unit. The gas supply line unit supplies the gas to the liquid tank (100) which circulates the liquid received inside the liquid tank. The liquid circulating line unit (200) is provided inside the liquid tank. The gas supplied in the gas supply line unit (300) is emitted to the microbubble. The water is vibrated with ultrasound and the microbubble is swept away.    USE - Device for producing microbubble in water using ultrasonic vibrator.    ADVANTAGE - The noxiousness effluent can be reduced and energy-saving with the combustion of fuel is ensured. The fuel efficiency can be improved. The frictional force generated between the inner pipe surface and fuel can be decreased.    DETAILED DESCRIPTION - The gas supply line unit injects the gas inside tank and the vibration is generated by the ultrasonic oscillator equipped in the inside and is adhered to one side of the perforated pipe. The gas barrel balls are formed around bolt portion and curve groove is formed according to outer periphery. The rear end of perforated pipe is inserted and fixed in front portion. INDEPENDENT CLAIMS are included for the following:    (1) cell culture medium;    (2) cell culturing method, involves adding cells into culture medium, and culturing the cells, where the medium comprises 103-1018/ml microbubbles with a diameter of 1000 mu m to 1 nm;    (3) high efficiency mixed fuel; and    (4) high efficiency mixed fuel manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microbubble producing device.    Liquid tank (100)    Vent (101)    Liquid circulating line unit (200)    Gas supply line unit (300)    Minuteness bubble emissive elements (400)
NOVELTY - A cotton bollworm-preventing and curing biogas slurry composite insecticide contains 99.5-99.8 wt.% biogas slurry, and 0.2-0.5 wt.% insecticidal composition containing abamectin and phenthoate with weight ratio of 1:10-30.    USE - A cotton bollworm-preventing and curing biogas slurry composite insecticide (claimed).    ADVANTAGE - Biogas slurry composite insecticide is environment-friendly, safe to use, and highly efficient in preventing and curing cotton bollworm, does not contain biogas slurry residue, fully utilizes biogas slurry insecticide active ingredient, reduces farm chemical use amount, and promotes growth and enhances pest control ability of crops.
NOVELTY - A synthetic gas is prepared by feeding hydrogen (H2) gas, carbon monoxide (CO), carbon dioxide (CO2) and water (H2O) in high temperature methanation unit comprising not less than 2 n-reactors which are connected in series to produce outlet stream Vn and is fed to next reactor stage through reactor inlet, converting to obtain outlet stream Vn', compressing, and feeding outlet stream Vn in low temperature methanation unit comprising not less than 2 m-reactors which are connected in series.    USE - Preparation of synthetic gas for natural gas alternative (claimed).    ADVANTAGE - The method has improved conversion rate, consumes less energy and is low cost, and gas has high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of synthesis for natural gas alternative using double high temperature methanation reactor.    Raw gases (1)    High temperature methanation reactor feed synthesis gas (2)    Double high temperature methanation reactor feed synthesis gas (3)    High temperature methanation reactor feed mixture (4)    High temperature methanation reactor feed gas (5)
NOVELTY - Fermenting liquid is prepared by adding fresh chicken manure and molasses alcohol waste liquid into fermentation substrate, further adding clean water at 20-35 degrees C and fermenting mixture for more than 45 days.    USE - The fermenting liquid is useful for killing root knot nematode, inhibition of root-knot nematode eggs hatch (all claimed) and organic agriculture.
NOVELTY - A waste biomass magnetic activated carbon is prepared by pretreating waste biomass, impregnating pretreated waste biomass in zinc chloride solution to obtain impregnated waste biomass, adsorbing lauric acid, sodium dodecyl sulfate, and 2 surfactant layers on inner and outer surface of ferrous ferric oxide (Fe3O4) to obtain required magnetization agent, uniformly mixing magnetization agent and dipped waste biomass, drying to obtain molded article, performing cracking on molded article at 400-500 degrees C under inert gas protection, washing cracking product using water, and drying.    USE - Preparation of waste biomass magnetic activated carbon (claimed).    ADVANTAGE - The preparation is simple, clean, environment-friendly, controls amount of magnetic additive, has low activating temperature, cheap and easy to obtain raw material, avoids secondary pollution, and obtains product which has high specific surface area activity, good absorption property, enough magnetic strength, and stable magnetic property.    DETAILED DESCRIPTION - A waste biomass magnetic activated carbon is prepared by pretreating waste biomass, i.e. washing, drying, crushing, and screening, impregnating pretreated waste biomass in zinc chloride solution to obtain impregnated waste biomass in which waste biomass is agricultural waste, wood, or wood waste, adsorbing lauric acid, sodium dodecyl sulfate, and 2 surfactant layers on inner and outer surface of Fe3O4 to obtain required magnetization agent, uniformly mixing magnetization agent and dipped waste biomass, drying to obtain molded article, performing cracking on molded article at 400-500 degrees C under inert gas protection, washing cracking product using water, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of preparation of waste biomass magnetic activated carbon. (Drawing includes non-English language text).
NOVELTY - Method for treating municipal sewage water involves constructing plant expression vector comprising super promoter and Vitreoscilla hemoglobin gene, constructing transgenic Alternanthera philoxeroides plant, breeding the transgenic plant, transplanting to sewage water, and repairing water.    USE - The method is useful for treating municipal sewage water in high latitudinal and longitudinal area (claimed).    ADVANTAGE - The method enhances oxygen binding ability and oxygen demand, and improves cold resistance of A.philoxeroides.
NOVELTY - Organic fertilizer comprises 300 pts. wt. of dry silkworm excrement, 10-20 pts. wt. of peanut powder, 20-40 pts. wt. of peanut shell powder, 0.5-1.5 pts. wt. of microbial agent, 4-8 pts. wt. of tea seed shell powder, 20-40 pts. wt. of Saccharum officinarum ash and 1-6 pts. wt. of lime powder.    USE - The organic fertilizer is useful for cultivating hawthorn (claimed).    ADVANTAGE - The organic fertilizer has simple preparation process, reduced production cost, improved utilization rate, increased yield, improved quality, prolong storage period, and ecological and social benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing organic fertilizer comprising (1) mixing the dry silkworm excrement, peanut powder, peanut shell powder in a mixer to obtain a mixed material, adding the mixed material in a fertilizer production device and mixing the microbial agent with the mixed material, (2) carrying out solid state fermentation in the continuous fertilizer production device under controlled temperature below 80 degrees C and 40% moisture to obtain fermentation of organic fertilizer, (3) uniformly mixing the tea seed shell powder, Saccharum officinarum ash and lime powder and adding into the continuous fermentation of organic fertilizer using fan spray, and (4) drying the obtained material in step (3) at 80-90 degrees C to the moisture content of less than 13% and packaging.
NOVELTY - Biological enzyme modified environmentally friendly fuel comprises 60-90 wt.% diesel, 8-30 wt.% ethanol, 0.1-1 wt.% alkyl nitrate modifier, and 1-10 wt.% biological enzyme modifier.    USE - Used as biological enzyme modified environmentally friendly fuel.    ADVANTAGE - The fuel has high cetane number, low sulfur content, low ash content, and is energy saving. The method is simple, safe, and clean.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biological enzyme modified environmentally friendly fuel, comprising adding diesel in to a the reaction tank, then adding ethanol and biological enzyme modifier, sealing and reacting for 24-48 hours, then adding alkyl nitrate modifier, stirring to uniformity and reacting for 5-10 minutes.
NOVELTY - Biocatalyst comprising 1-3 pts. wt. of mixed microbial agent, 100 pts. wt. of hydrolase accelerator and 61-329 pts. wt. of mineral nutrient accelerator, is new.    USE - The biocatalyst is useful in marsh gas fermentation (claimed).    ADVANTAGE - The biocatalyst has membrane filtration function, biological degradation complementary function, deodorization and pathogenic microorganism suppressing function, and can be prepared in a simple and cost effective manner without pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the preparation of biocatalyst; and    (2) use of biocatalyst in marsh gas fermentation, where the application method comprises adding 350-650 pts. wt. of livestock and poultry excrement as raw material into 100-300 pts. wt. of sludge inoculum and 163-430 pts. wt. of biocatalyst and then fermenting at water control rate of 75-85%, adding chlorine into the fermented product until the concentration is 7-12% and then mixing and fermentation at 20-40 degrees C.
NOVELTY - Producing ethanol fuel comprises (1) adding straw pulp with diluted sulfuric acid solution to dissolve, carrying out hydrolysis reaction and then separating supernatant liquid, (2) adding the filter residue in the substrate having enzyme, introducing the mixture in a shaker and then shaking, boiling the obtained product in a water bath for enzyme deactivation, separating the supernatant and then adding sugar for digestion, and (3) neutralizing the acidolysis and enzymolysis solution and then adding ammonium sulfate, monopotassium phosphate, hydrated magnesium sulfate and yeast extract.    USE - The method is useful for producing ethanol fuel (claimed).    ADVANTAGE - The method is capable of producing ethanol fuel in a cost effective and eco-friendly manner with less energy consumption.    DETAILED DESCRIPTION - Producing ethanol fuel comprises (1) adding straw pulp with diluted sulfuric acid solution in a ratio of 1 g:18-22 ml to dissolve at 170-190 degrees C, carrying out hydrolysis reaction for 2-4 hours and then separating supernatant liquid by centrifugation, (2) adding the filter residue in the substrate having 60-100 u/g of enzyme and water concentration of 0.01/m, introducing the mixture in a shaker and then shaking at 50 degrees C for 30 hours, boiling the obtained product in a water bath for enzyme deactivation, separating the supernatant by centrifugation and then adding sugar for digestion and (3) concentrating and neutralizing the acidolysis and enzymolysis solution and then adding ammonium sulfate, monopotassium phosphate, hydrated magnesium sulfate and yeast extract, adjusting the pH value of the mixed solution to 5.5 to obtain hydrolysis fermentation culture base, adding hydrolysis fermentation culture base and yeast Candida shehatae in the ratio of 1:10 at 28 degrees C and speed of 100 revolutions per minute for 48 hours.
NOVELTY - Composition comprises 99.5-99.8 wt.% biogas slurry and 0.2-0.5 wt.% fungicidal composition. The fungicidal composition comprises procymidone, and myclobutanil in weight ratio of 1:7.5.    USE - The composition in the form of emulsion or powder is useful for preventing and treating anthracnose (claimed).    ADVANTAGE - The composition has an effective rate of more than 85%, rapid effect and sustained fungicidal properties, does not leave any biogas slurry residue, makes full use of antifungal components of biogas slurry, reduces dosage of pesticides, is safe as it reduces environmental risks, and enables direct absorption of nutrients present in slurry by vegetables and crops and thus promotes crop growth and enhances disease resistance of crops.
NOVELTY - Process for preparing moxifloxacin hydrochloride, involves: condensing (1-cyclopropyl-6,7-difluoro-8-methoxy-4-oxo-1,4-dihydro-3-quinoline carboxylic acid-O3, O4)bis(acyloxy-O)borate with (S,S)-2,8-diazabicyclo(4.3.0)nonane in presence of base in a solvent system to produce intermediate compound (4aS-Cis)-(1-cyclopropyl-7-(2,8-diazabicyclo(4.3.0)-non-8-yl)-6-fluoro-8-methoxy-4-oxo-1,4-dihydro-3-quinoline carboxylic acid-O3, O4)bis(acyloxy-O)borate; optionally isolating the intermediate compound; and hydrolyzing the intermediate compound to form moxifloxacin hydrochloride.    USE - For preparing moxifloxacin hydrochloride (claimed) used for the treatment of endocarditis, meningitis, tuberculosis, respiratory tract infections, anthrax and cellulitis.    ADVANTAGE - The improved process is commercially viable, economical, and environment friendly. It employs minimal purification steps and wastage of material. The process provides moxifloxacin hydrochloride with high purity in high yield. Moreover, it uses user friendly, cost efficient raw material and solvents.    DETAILED DESCRIPTION - Process for preparing moxifloxacin hydrochloride, involves: i) condensing (1-cyclopropyl-6,7-difluoro-8-methoxy-4-oxo-1,4-dihydro-3-quinoline carboxylic acid-O3, O4)bis(acyloxy-O)borate of formula (II) with (S,S)-2,8-diazabicyclo(4.3.0)nonane of formula (III) in presence of a base in a solvent system to produce intermediate compound (4aS-Cis)-(1-cyclopropyl-7-(2,8-diazabicyclo(4.3.0)-non-8-yl)-6-fluoro-8-methoxy-4-oxo-1,4-dihydro-3-quinoline carboxylic acid-O3, O4)bis(acyloxy-O)borate of formula (IV); ii) optionally isolating the compound IV; and iii) hydrolyzing IV to form moxifloxacin hydrochloride. The compound II has a moisture content of 10-50%. The solvent system comprises an organic solvent and water.
NOVELTY - The fuel generator has an accommodation unit (4) that accommodates fuel generation element (1). An exhaust valve (7) is provided between accommodation unit and gas outlet. The opening angle of the exhaust valve is cyclically varied at opening angles including first opening angle and second opening angle smaller than the first opening angle. The increase in pressure in accommodation unit due to oxidizing gas supplied to the accommodation unit from outside is greater in case where opening angle of exhaust valve is at second opening angle.    USE - Fuel generator of fuel cell system (claimed).    ADVANTAGE - The increase in pressure in accommodation unit due to oxidizing gas supplied to the accommodation unit from outside is greater in case where opening angle of exhaust valve is at second opening angle, so that oxidizing gas can be spread evenly round the fuel generator. Thus pressure loss of fuel generation element can be avoided easily. The generation amount of the fuel gas from fuel generator is increased, and the battery capacity of fuel cell system is improved. The durability of fuel generator and fuel cell system can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel generator. (Drawing includes non-English language text)    Fuel generation element (1)    Fuel cell portion (2)    Heater (3)    Accommodation unit (4)    Exhaust valve (7)
NOVELTY - An electrolyte (110) containing dissolved carbon dioxide, precipitation agent and alcohol is injected to a reactor (160) containing an anode (120), a cathode (130) and an ion permeable membrane (140) between anode and cathode. A voltage is applied to the reactor. The carbon dioxide dissolved in electrolyte is electrolyzed. Thus, reduction of carbon dioxide is enabled.    USE - Method for reducing carbon dioxide used for generating alkane and hydrogen (claimed).    ADVANTAGE - The method enables efficient and economical reduction of carbon dioxide having excellent selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) carbon dioxide reductor (100); and    (2) electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of carbon dioxide reductor.    Carbon dioxide reductor (100)    Electrolyte (110)    Anode (120)    Cathode (130)    Ion permeable membrane (140)    Reactor (160)
NOVELTY - Mixture comprises soft manure as decomposition accelerator, fishmeal, blood of slaughtered cattle or sheep, liver of slaughtered bovine animals or sheep, source of carbohydrate, a liquid milk product as microbial growth accelerator and water, where the mixture is obtained by utilizing anaerobic fermentation process.    USE - Mixture for production of fermented products i.e. fermented liquid product or solid fermented product used as fertilizer for plants (grains (maize, sorghum, wheat, barley and oats), legumes, vegetables and ornamentals), particularly wheat, barley and oats (all claimed), and used in agriculture, particularly in agriculture organic area.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for producing fermented products from anaerobic fermentation of the mixture, which involves adding components of the mixture in a conventional bio-digester, preferably stainless steel; fermenting components of the mixture anaerobically for 7 days in the bio-digester; separating the liquid and solid phases through a filter; deodorizing the liquid with using activated carbon, and with eliminating pathogens; and recovering the solid phase in a container; and    (2) a method for preparing a liquid foliar fertilizer, which involves adding the liquid fermented product and a mixture of mineral salts in a conventional mixing tank; homogenizing the mixture for 5 hours; and adding acceptable additives to the mixture.
NOVELTY - Recycling medium impact polystyrene involves crushing and washing waste; qualitatively characterizing wastes; sulfonating waste; wash-sulfonated recovering waste; and both qualitatively and quantitatively characterizing sulfonated polymer.    USE - The processes are useful for recycling medium impact polystyrene; and for producing biodiesel from oils with high content of free fatty acids catalyzed by the acid catalyst (all claimed).    ADVANTAGE - In the process, certain operating conditions within ranges allow the degree of sulfonation to be maximized and the consumption of acid to be minimized, conferring on the method a technical effect which is not obvious and is different from sulfonation processes known in the prior art. The catalyst can promote (within the established esterification ranges) reaction yields up to 90%, easily removed from the medium following filtration.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an acid catalyst obtained through the recycling process of medium impact polystyrene; and    (2) a process for producing biodiesel from oils with high content of free fatty acids catalyzed by the acid catalyst, which involves determining the content of free fatty acids in the oil using Cd-3d-63 of the American Oil Chemistry Society (AOCS) technique; esterifying the oil with 0.06-0.18 gram of sulfonated polystyrene per gram of free fatty acid in the sample and a ratio of 30 to 50 mmol of methanol per mmol of free fatty acid in the sample into a vessel that allows stirring at 600-800 revolutions per minute (rpm) at the temperature conditions of 60 degrees C for a time of 1 hour; and obtaining the percent product yield of 100 with the difference of 1 and the ratio of free fatty acid content in the bottom phase formed after esterification, from the content of free fatty acids in the sample at the beginning of reaction.
NOVELTY - Producing wood fiber for product uses from non-food plant biomass, involves: (a) hot-water extraction carried out by contacting a charge of the non-food plant biomass material with water, in a pressurized vessel at an elevated temperature up to 250 degrees C, to yield an aqueous extract containing hemicellulosic components and a lignocellulosic residue; (b) separating the aqueous extract from the lignocellulosic residue; (c) further processing the separated aqueous extract; and (d) processing the lignocellulosic residue to yield useful products.    USE - The process is useful for producing wood fiber for product uses from non-food plant biomass, where the obtained wood fiber residue is useful for producing: wood composite products (including furniture products, structural materials, plastic/wood composite decking, or other reconstituted wood product such as medium-density fiberboard, oriented strand board, or fiber board); lignocellulosic fuel pellets; bioconversion feedstock products; crystalline cellulose; and additional bioconversion feedstock products such as fermentable sugars (all claimed).    ADVANTAGE - The process provides fibrous material with high yield and high resistant to water sorption.
NOVELTY - Increasing the production of a glycolytic intermediate and an organic compound by a cell that is able to express a nucleic acid molecule, is claimed. The expression of the nucleic acid molecule gives the cell the ability to increase the production of a glycolytic intermediate and the organic compound. The carbon substrate is sugar and protein.    USE - The method is useful for increasing the production of a glycolytic intermediate and an organic compound (claimed), where the organic compound is used as biofuel or chemical feedstock.    ADVANTAGE - The method increases ethanol fermentation yield and provides clean biofuel in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bacterium capable of expressing a nucleic acid molecule, where the expression of the nucleic acid molecule confers on the bacterium the ability to increase the production of a glycolytic intermediate and to increase the conversion of the glycolytic intermediate into an organic compound.
NOVELTY - Improving carbon capture in a microbial fermentation of a substrate comprising carbon monoxide (CO), involves: (a) in a bioreactor comprising a culture of one or more microorganisms, fermenting a gaseous substrate comprising CO to produce a fermentation broth comprising one or more products; (b) passing at least a portion of the fermentation broth via a bleed stream, from the bioreactor; (c) passing at least a portion of a permeate stream from the bioreactor; (d) removing at least a portion of the one or more products from the bleed stream.    USE - The method is useful for improving carbon capture in a microbial fermentation of a substrate comprising carbon monoxide (claimed).    ADVANTAGE - The method efficiently improves microbial fermentation of a substrate, and overcomes the disadvantages of the previous methods.    DETAILED DESCRIPTION - Improving carbon capture in a microbial fermentation of a substrate comprising carbon monoxide (CO), involves: (a) in a bioreactor comprising a culture of one or more microorganisms, fermenting a gaseous substrate comprising CO to produce a fermentation broth comprising one or more products; (b) passing at least a portion of the fermentation broth via a bleed stream, from the bioreactor; (c) passing at least a portion of a permeate stream from the bioreactor; (d) removing at least a portion of the one or more products from the bleed stream and/or permeate stream to provide a product depleted stream; (e) passing the product depleted stream to a clarifying module where at least a portion of one or more components of the product depleted stream selected from biomass, proteins, organic components, or inorganic components is removed from the product depleted stream to provide a treated stream; and (f) passing at least a portion of the treated stream to the bioreactor.
NOVELTY - The system has a flat gas permeation membrane (2) that separates the first and second environments. The first and second structural elements (3,4) comprises element for creating a vortex motion on the surface of the permeation membrane. The structural elements provide the two chambers (8,9,l0,23,24,25) to provide fluidic communication in the vicinity of the membrane. The element for creating vortex motion comprises an inlet of inlet chamber and gas diverter that incline to a non-null inclination angle below 90 degrees with respect to the plane on which the flat membrane lies.    USE - System for separation of gas such as oxygen from air and hydrogen from syngas.    ADVANTAGE - Since the vortex motion is generated in the chambers, the thickness of the boundary layer above the membrane is reduced and the gas separation efficiency can be increased. The speed of the gas can be regulated in different areas of the membrane thus the pressure in the area can be reduced and the working life of the gaskets can be extended.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for the separation of gas.    DESCRIPTION OF DRAWING(S) - The drawings show a sectional view and an enlarged sectional view of the system for the separation of the gas.    Flat gas permeation membrane (2)    Structural elements (3,4)    Gas (6,7)    Chambers (8,9,10,23,24,25)    Partition walls (51)
NOVELTY - Processing residual products, comprises: subjecting the solid residual products (1) to crushing with subsequent mixing and subjecting obtained discharge product to an aerobic biological treatment (3); mixing the discharge product from a final drying (8) in a mixer optionally with a discharge product from a first processing stage (11) of a solid residual product (4); and supplying the discharge product from final drying or optionally discharge product from a mixer for a thermal reprocessing. The discharge product, optionally after final drying, is subjected to a first processing stage.    USE - The method is useful for producing fertilizer and a building material (all claimed).    ADVANTAGE - The method enables economical reprocessing of residual products.    DETAILED DESCRIPTION - Processing residual products, comprises: subjecting the solid residual products (1) to crushing with subsequent mixing and subjecting obtained discharge product to an aerobic biological treatment (3); mixing the discharge product from a final drying (8) in a mixer optionally with a discharge product from a first processing stage (11) of a solid residual product (4); and supplying the discharge product from the final drying or optionally the discharge product from a mixer for a thermal reprocessing. The discharge product discharged from the aerobic biological treatment, optionally after final drying, is subjected to a first processing stage, comprising screening, separating, preferably air separating, and post-refining. The discharge product discharged from the first processing stage is optionally subjected to a second processing stage comprising coarse and fine crushing and screen separating, with subsequent dividing by the size of the grain fraction. The sludgy residual products are subjected to an anaerobic biological treatment stage, preferably a sludge digestion, in which the discharge product from the anaerobic treatment stage is supplied for the final drying.
NOVELTY - Advanced wastewater treatment, comprises (a) denitrifying raw water by inflowing raw water into a first anoxic tank (20) provided with a first fluidized bed carrier (70), (b) decomposing organic matter and nitrogen oxide by inflowing raw water into a first oxygen tank (30) provided with a second fluidized bed carrier, and (c) introducing raw water into a second oxygen tank (40) provided with impregnated separation membrane, injecting coagulant, mixing coagulant and crude raw water, and removing total phosphorus by inflowing into a rapid sedimentation tank.    USE - The method is useful for advanced wastewater treatment (claimed).    ADVANTAGE - The method is simple, resolves nitrification inhibition problem, solves the problem of rising the transmembrane pressure, minimizes the discharge of non co-precipitated sludge, reduces requirements of coagulant and hydraulic retention time and does not require additional equipment for removing low concentrations of total phosphorus.    DETAILED DESCRIPTION - Advanced wastewater treatment, comprises (a) denitrifying raw water by inflowing raw water into a first anoxic tank (20) provided with a first fluidized bed carrier (70), (b) decomposing organic matter and nitrogen oxide by inflowing crude raw water obtained from the step (a) into a first oxygen tank (30) provided with a second fluidized bed carrier, and (c) introducing crude raw water obtained from the step (b) into a second oxygen tank (40) provided with impregnated separation membrane, injecting coagulant, mixing coagulant and crude raw water, and removing total phosphorus by inflowing into a rapid sedimentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the advanced wastewater treatment device.    First anoxic tank (20)    First oxygen tank (30)    Second oxygen tank (40)    Partition wall (60)    First fluidized bed carrier (70)
NOVELTY - Absorbent solution comprises water, and a compound including N-alkyl-3-hydroxypiperidine and N-alkyl-4-hydroxypiperidine compounds (I).    USE - The absorbent solution is useful for removing acid compounds i.e. hydrogen sulfide, from a gaseous effluent including natural gas, synthesis gas, combustion fumes, refinery gases, amine gases, biomass fermentation gas, gases coming out from cement factory and incineration gases (all claimed).    ADVANTAGE - The absorbent solution has excellent acid compound absorption capacity, and excellent selectivity towards the hydrogen sulfide.    DETAILED DESCRIPTION - Absorbent solution comprises water, and a compound including N-alkyl-3-hydroxypiperidine and N-alkyl-4-hydroxypiperidine compounds of formulae (I).    R = 1-6C, preferably 1-3C alkyl, where hydroxyl group is located at 3rd or 4th position of a piperidine ring with respect to the nitrogen atom.    An INDEPENDENT CLAIM is included for removing acid compounds from a gaseous effluent comprising absorbing the acid compounds by contacting the effluent with an absorbent solution.
NOVELTY - A gas separation membrane (10) has a gas separation layer (1) formed using polybenzoxazole resin having solubility of 1 %mass or more with respect to a solvent chosen from tetrahydrofuran, chloroform, methyl ethyl ketone, and N-methylpyrrolidone at 30 degrees C.    USE - Membrane is used for gas separation module for gas separation apparatus used for separating carbon dioxide from mixed gas containing methane and carbon dioxide (all claimed).    ADVANTAGE - The gas separation membrane has excellent mechanical strength, gas permeability and gas separation selectivity, and favorable durability. The deterioration of the gas separation membrane is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas separation method, which involves selectively permeating carbon dioxide from a gas containing carbon dioxide and methane using the gas separation membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas separation membrane.    Gas separation layer (1)    Porous layer (2)    Gas separation membrane (10)
NOVELTY - Device for combined feed, admixture, dosage and hydrolysis of biomass in a biogas plant or other biomass processing plants and processes, comprises a container having an inner cubicle wall and a laterally displaced inner lowering wall. The upper end of the cubicle wall is located above the bottom end of the lowering wall and a biomass feed chamber (1) and a pump chamber (2) are present in the liquid-filled state of the container of two-sided separate gas chambers.    USE - The device is useful for combined feed, admixture, dosage and hydrolysis of biomass in a biogas plant or other biomass processing plants and processes (claimed).    ADVANTAGE - The device: has simple construction; and controls the transport of the liquid media in all desired amounts and directions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for combined feeding, admixing, dosing and hydrolyzing biomass for a biogas plant, or other biomass processing systems and processes by using the device, comprising (a) feeding the biomass feed chamber with biomass through an opening (3) directly from the delivery vehicle or device, so that a bulk dump (4) of fresh substrate is present, (b) spraying the bulk dump with fluid from an external source, from the pump chamber or from the fermenter of the plant via a nozzle system (6), where the hydrolysis of the biomass begins and the container bottom is filled with liquid, (c) mixing and homogenizing the biomass by an agitator, (d) transferring the mixed material into the pumping chamber by a high performance cutting pump, where the treatment is performed by crushing and further homogenization, and (e) transferring the material from the pump chamber into the fermenter.    DESCRIPTION OF DRAWING(S) - The figure shows a sectional view of a biomass feeding chamber and a pump chamber (Drawing includes non-English language text).    Biomass feed chamber (1)    Pump chamber (2)    Opening (3)    Bulk dump (4)    Nozzle system (6)
NOVELTY - Device for producing biogas by multi-step fermentation in a single container, comprises a container whose inner side is provided with additional partitions (3) which are arranged such that the total volume of the container is divided into at least two partial volumes, and partitioned container sectors are formed which do not form a separate container. The fermentation steps are controlled with respect to reaction course and residence time.    USE - The device is useful for producing biogas (claimed).    ADVANTAGE - The device simplifies technical parameters in containers for fermentation processes, and comprises single container for all the fermentation processes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the container body.    Container base (1)    Outer wall (2)    Partitions (3)    Hydrolysis sector (7)    Filling level (12)
NOVELTY - Odor treatment of biosubstrate, comprises introducing an odor treatment substance based on iron chloride into the biosubstrate. The odor treatment substance is supplied/mixed to the fermentation residue or to the final waste from the food production and to the biosubstrate (final waste), after final degassing of a biogas fermentation substrate, and prior to the application to land or landfill sites.    USE - The method is useful for odor treatment of biosubstrate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method for odor treatment prior to application (Drawing includes non-English language text).
NOVELTY - Monitoring device (24) for a biogas plant (10), comprises: a removal device (19), which is capable of removing a biogas sample from the biogas produced in a biogas reactor (12) of the biogas plant biogas; a water retention device, which is designed to retain the biogas sample contained water; a sensor device (22) which is adapted to determine an acid content in the retained water.    USE - The monitoring device is useful for a biogas plant (claimed).    ADVANTAGE - The monitoring device: allows detection of tipping over of the biogas plant at an early stage; and ensures a better control of the operation of a biogas plant.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biogas plant comprising at least one biogas reactor and at least one monitoring device; and    (2) monitoring a biogas plant, preferably a biogas plant, comprising removing a biogas sample from the biogas in a biogas reactor, retaining the water in the biogas sample, and determining an acid fraction in the retained water.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas reactor with a monitoring device.    Biogas plant (10)    Biogas reactor (12)    Removal device (19)    Sensor device (22)    Monitoring device (24)
NOVELTY - Settlement device (10) for colonization of microorganisms for a biogas reactor, comprises at least one surface support structure (12) for providing at least one settlement area for colonization of microorganisms. The settlement device is stored or storable in the biogas reactor by a storage device (16).    USE - The settlement device is useful for colonization of microorganisms for a biogas reactor (claimed).    ADVANTAGE - The settlement device: is able to efficiently operate the biogas reactors ; and prevent acidifying of a biogas reactor by suitable measures.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biogas reactor comprising a settling device; and    (2) operating a biogas reactor, comprising feeding the biogas reactor with easily degradable substrate, and rotating a settlement device within the biogas reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of the settlement device.    Settlement device (10)    Surface support structure (12)    Holding rods (14)    Storage device (16)    Covering (18)
NOVELTY - Producing biofuels, comprises producing (1) biofuels from algae under the formation of biomass, and converting (2) the biomass to the low molecular weight compound in a reactor, which the biomass contains microorganisms occurring in rumen.    USE - The method is useful for producing biofuels (claimed).    ADVANTAGE - The method allows rapid and economical production of the biofuels with less energy consumption in an environmentally-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) use of a reactor as an artificial rumen in a method, which is suitable for both a batch process and a feed process, comprising a device for supplying the biomass and optionally reagents, a device for removing the low molecular weight compounds and a fumigation plant;    (2) a system for producing biofuels; and    (3) a biofuel produced by the method.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a method for producing biofuels.    Producing biofuels from algae under the formation of biomass (1)    Converting the biomass to the low molecular weight compound in a reactor (2)    Outlet. (3)
NOVELTY - Sulfur exhaust process is performed by exhausting natural gas in hydrogenation reactor, exhausting all sulfides and elemental sulfur which is reduced to hydrogen sulfide, entering exhausted natural gas and hydrogen sulfide into cooling tower, cooling, entering cooled gas mixture of exhausted natural gas and hydrogen sulfide into low-pressure desulfurization device, removing sulfur compounds in gas mixture, and burning into atmosphere remaining gas.    USE - Sulfur exhaust process for recovery of natural gas (claimed).    ADVANTAGE - Process is simple and low cost, and reduces gas emissions into atmosphere.
NOVELTY - Preparing activated sludge involves attaching the activated sludge on the carrier material only after sterilization of sludge as raw material. The obtained material is fermented, filtered and then dried to assay the activity of yeast using activated sludge.    USE - Method for preparing activated sludge used for measuring the concentration of yeast in domestic sewage and as feed or compost (claimed).    ADVANTAGE - The method enables to prepare activated sludge of high efficacy that can be stored for longer duration of time in a simple and cost-effective manner.
NOVELTY - This utility new type provide the a one electrolyzing water to produce oxygen device, comprise the water storage bucket and the electrolytic water, electrolytic water from said water reservoir and the left and right water reservoir, a water reservoir through two connecting water tube connected, a water storage bucket connecting with the purifier, a purifier and connecting water tube connected, a water reservoir and the left and right of the bottom of a water reservoir connect with the anode electrolyte and the cathode electrolyte rod, water reservoir and the top of the left and right water reservoir connect first air outlet tube and a second air outlet tube, a first the pneuma tube filter and the upper end of the air inlet connecting bucket, a filtering bucket upper end of the carbon filter connecting activity, said activity carbon filter and the oxygen storage bucket connecting. A second outlet tube pneuma pneuma tube connect with the combustion, a combustion pneuma tube is set in the condensing tube, a condensing tube and the water storage bucket connecting. The utility model is made of oxygen does not contain water and other impurity, high purity, fully by means of electrolysis of water to obtain hydrogen and save the resource.
NOVELTY - Absorbent for purification of landfill gas to recover methane comprises 80-90 wt.% polyethylene glycol dimethyl ether, 10 wt.% solvent, 0.1-0.5 wt.% stabilizing agent and rest of water.    USE - For purification of landfill gas to recover methane (claimed).    ADVANTAGE - The absorbent recovers methane having purity of 85-97%, and has methane recovery rate of not less than 96%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification of landfill gas to recover methane involving filtering landfill gas containing impurity through preprocessing tower, removing the sulfide, chlorinated hydrocarbons, volatile organic compound and carbon dioxide to obtain methane.
NOVELTY - Recombinant Saccharomyces cerevisiae for degrading kitchen waste, comprising expression vector comprising alpha-amylase gene, maltogenic amylase gene and acid protease gene, is new.    USE - The recombinant Saccharomyces cerevisiae is useful for degrading kitchen waste (claimed) for conversion into ethanol.    ADVANTAGE - The recombinant Saccharomyces cerevisiae provides kitchen waste solutions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for constructing recombinant Saccharomyces cerevisiae.
NOVELTY - A straw decomposing agent comprises Bacillus subtilis, Aspergillus niger, Trichoderma viride, Phanerochate chrysosporium, and Geobacillus stearothermophiIus as active component with total viable count of 1-2x 108/ml.    USE - A straw decomposing agent for organic fertilizer (claimed).    ADVANTAGE - Straw decomposing agent improves soil and increases crop yield and quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of straw decomposing agent which involves activating B. subtilis at 28-38 degrees C for 1-3 days, A. niger at 25 degrees C for 4-7 days, T. viride at 25-28 degrees C for 4-7 days, P. chrysosporium at 25-28 degrees C for 4-7 days, and G. stearothermophiIus at 60 degrees C for 1-3 days in slant culture medium, inoculating each in liquid culture medium, growing seed culture in shaker until total viable count is 1-2x 108/ml, inoculating 5% inoculated strain in fermentation culture medium, shaking culture medium until total viable count is 1-2x 108/ml, collecting each strain fermentation culture medium, combining each strain fermentation culture medium to obtain mixed bacteria fermentation culture medium, inoculating 1-5% mixed bacteria fermentation culture medium in composite microbial agent inoculum, and culturing at 28-30 degrees C for 4-7 days; and (2) preparation of organic fertilizer which involves fermenting crop straw with 2-5% straw decomposing agent at outdoor natural temperature condition for 25-35 days.
NOVELTY - Producing fermentation products from starch-containing material involves (a) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using alpha -amylase, optionally a protease having a thermostability value of not less than 20% determined as relative activity at (80/70) degrees C and optionally a carbohydrate-source generating enzyme, (b) saccharifying using a carbohydrate-source generating enzyme, and (c) fermenting using a fermenting organism.    USE - The method and enzyme composition are useful for producing fermentation products chosen from alcohol, preferably ethanol, more preferably fuel ethanol, potable ethanol and/or industrial ethanol from starch-containing material (all claimed) includes whole grains, corn, wheat, barley, rye, milo, sago, cassava, tapioca, sorghum, rice, peas, beans, and sweet potatoes. The fermentation products also include polyols, organic acids, ketones, amino acids, gases, antibiotics, enzymes, vitamins and hormones.    ADVANTAGE - The method produces higher fermentation product yield compared to existing method.    DETAILED DESCRIPTION - Producing fermentation products from starch-containing material involves (a) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using alpha -amylase, optionally a protease having a thermostability value of not less than 20% determined as relative activity at (80/70) degrees C and optionally a carbohydrate-source generating enzyme, (b) saccharifying using a carbohydrate-source generating enzyme, and (c) fermenting using a fermenting organism, where a cellulolytic composition is present or added during fermentation or simultaneous saccharification and fermentation. An INDEPENDENT CLAIM is included for enzyme composition which comprises the alpha -amylase, optionally protease having the above-mentioned property, optionally pullulanase and carbohydrate-source generating enzyme.
NOVELTY - The system has a carbon dioxide collecting apparatus arranged with a main engine and collecting high concentration carbon dioxide ejected in a molten carbonate fuel cell. Heat source is supplied to a steam generator by performing heat-exchange in high temperature exhaust gas generated from the fuel cell. The fuel cell produces electricity by performing electrochemical reaction of fuel flowing into a cathode and an anode pole. Air is utilized as a reducing agent in the electrochemical reaction. An exhaust gas fuel economizer is arranged in an engine room of a vessel.    USE - Fuel cell system for use in a vessel (claimed).    ADVANTAGE - The system ejects neogenesis energy from the main engine of the vessel so as to improve working efficiency of the vessel in an eco-friendly manner. The carbon dioxide collecting apparatus collects high concentration carbon dioxide, so that operating cost of the system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.'(Drawing includes non-English language text)'
NOVELTY - Method for processing lignocellulosic biomass by hydrolysis and saccharification, involves sprinkling water containing enzyme on lignocellulosic biomass to process lignocellulose, circulating and recovering at least one portion of treated product, and repeating the sprinkling process again.    USE - The method is useful for processing lignocellulosic biomass by hydrolysis and saccharification (claimed).    ADVANTAGE - The method does not require enhancement of installation and thus reduces installation cost, and consumes less energy.
NOVELTY - The system (10) equips wastewater line with ON-OFF valve in downstream rather than variable pressure-loss generation unit. The water-pouring speed detector detects the water-pouring speed of the liquid water poured by the high voltage gas-liquid separation apparatus (22) from the high-pressure water electrolyzer (12). The wastewater speed setting mechanism sets wastewater speed of liquid water based on detected water-pouring speed. The opening degree adjustment mechanism adjusts opening degree of variable pressure-loss generation unit based on set wastewater speed.    USE - Water electrolysis system used for production of hydrogen used as fuel gas for power generation reaction of fuel cell.    ADVANTAGE - Since the opening degree adjustment mechanism adjusts opening degree of variable pressure-loss generation unit based on set wastewater speed, the high voltage liquid water directly drained by only the ON-OFF valve is suppressed while adjustment of the water level in high voltage gas-liquid separation apparatus is performed easily. The generation of cavitation can be suppressed and the durability of ON-OFF valve can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a drainage method of water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory drawing of water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    High-pressure water electrolyzer (12)    Water retention apparatus (14)    Water circulation apparatus (16)    High voltage gas-liquid separation apparatus (22)
NOVELTY - A gas permeation membrane consists of polyimide structure (I) having repeating unit.    USE - Gas permeation membrane is used for separation of carbon dioxide from liquefied natural gas, and ethanol from ethanol-water for fuel.    ADVANTAGE - The gas permeation membrane is soluble in an organic solvent, and has excellent formability and gas-separation performance.    DETAILED DESCRIPTION - A gas permeation membrane consists of has polyimide structure of formula (I) having repeating unit.    R1=divalent organic group of formula (i);    R2=tetravalent organic group of formula (ii);    Ra,Rb=single bond, O, S, -SO2-, -CH2-, -C(=O)-, -C(CH3)2-, -C(CH3)(CH2CH3)-, -C(CF3)2-, -CH(CH3)-, -CH(OH)- or -NH-, or divalent organic group formed by removing two arbitrary hydrogen atoms of 3-12C alicyclic hydrocarbyl and 6-25C aromatic hydrocarbyl;    HFIP=-C(CF3)2OH;    p,q,r,s=0-2;and    p+q,r+s=1-4.    (i) H of OH group of HFIP in R1 is substituted by glycidyl group. The cyclic ether portion of glycidyl group is ring-opened and crosslinked.
NOVELTY - Salt mixture comprises: (a) benzophenanthridine alkaloids comprising sanguinarine, chelerythrine, macarpin and chelirubine in free or salt form, in substantially pure form or in form of extracts of Sanguinaria canadensis, Macleaya cordata, Macleaya microcarpa or Chelidonium majus; and (b) inorganic soluble salt of ferrous sulfate monohydrate, trimanganese tetraoxide, boric acid, zinc oxide, cupric sulfate pentahydrate, nickel-II sulfate hexahydrate, selenium sulfate pentahydrate, hexaammonium molybdenum oxide, tungsten VI chloride and copper-II sulfate.    USE - The salt mixture is useful in anaerobic digesters to stimulate the activity of methane gas-producing bacteria, preferably Archaea bacteria (claimed).    ADVANTAGE - The salt mixture: has components which have defined chemical structure and not cause toxicity (claimed).    DETAILED DESCRIPTION - Salt mixture comprises: (a) benzophenanthridine alkaloids comprising sanguinarine, chelerythrine, macarpin and chelirubine in free or salt form, in substantially pure form or in the form of extracts of Sanguinaria canadensis, Macleaya cordata, Macleaya microcarpa or Chelidonium majus; and (b) inorganic soluble salt of ferrous sulfate monohydrate, trimanganese tetraoxide, boric acid, zinc oxide, cupric sulfate pentahydrate, nickel-II sulfate hexahydrate, selenium sulfate pentahydrate, hexaammonium molybdenum oxide, tungsten VI chloride and copper-II sulfate. The salt mixture can be mixed in various levels in coordination of reference.
NOVELTY - Method for removing heavy metal in sludge involves injecting sulfuric acid into sludge, leaching the sludge using ultrasound, separating supernatant, injecting iron oxide bacteria into the supernatant, and leaching the supernatant.    USE - The method is useful for removing heavy metal in sludge (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - Performing a hydrolysis of a cellulosic biomass, involves providing the cellulosic biomass, providing a cellulose, providing a strain of Bacillus subtilis strain SH44, and mixing the cellulosic biomass, the cellulase and the strain of B.subtilis strain SH44 to perform hydrolysis.    USE - The method is useful for performing the hydrolysis of a cellulosic biomass (claimed).    ADVANTAGE - The method increases yield and a generating efficiency of the glucose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) cutting cellulose, involves performing the above-mentioned steps; (2) raw material of a hydrolysis of the cellulose, comprises the above-mentioned cellulose and a strain of B.subtilis strain SH44; (3) strain of B.subtilis strain SH44; and (4) mutant of the above-mentioned strain.
NOVELTY - The control device (10) for a biogas plant (12) adapted to generate signal based on parameters and kinetics of substrate supplied to a biogas reactor, is claimed. The control device is adapted to control the biogas plant based on the generated signal and to generate the signal as sensor data with respect to a substrate condition in the biogas reactor.    USE - The control device is useful in a plant (claimed), which is useful for producing biogas from substrates using microorganisms, where substrate includes starch such as corn starch, silage such as hole plant silage, corn silage, grass silage, grain silage and/or rye silage, waste such as sugar waste, food waste, bio-waste and/or agricultural waste including forestry waste and animal manure such as poultry manure, cattle manure, pig manure and/or cow manure, beet pulp including sugar beet pulp and fodder beet pulp, and distillers grains and/or cereals.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for operating a biogas plant; and    (2) a program product.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a biogas plant.    Control device (10)    Display (11)    Biogas plant (12)    Substrate (16)    Sensor device. (20)
NOVELTY - Method for processing organic waste water, involves processing organic waste with anaerobic microbe, adding waste water containing organic substance to the reaction tank holding carrier, starting the reaction tank, starting water flow of organic waste water in state which made carrier, and adding methane-bacterium aggregate having average particle diameter of 10-450 mu m or more, where the concentration of the methane-bacterium aggregate is 1-900 g/l.    USE - The method is useful for processing organic waste water (claimed).    ADVANTAGE - The method is rapid.
NOVELTY - A fuel is obtained by homogenizing a mixture containing 0.1-30% ground HAP biomass and 70-99.9% liquid fuel component.    USE - Fuel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of fuel, which involves mixing ground HAP biomass and liquid fuel component, processing obtained mixture in cavitator, and removing the mixture in cavitator before performing complete homogenization.
NOVELTY - The hydrogen obtaining method involves decomposing water into hydrogen and oxygen using the cumulative effect of a pair of emitters, whose ends are directed along the coordinates of one or more vectors pairs of radiators. Each pair of emitters includes electrical or magnetic high-frequency fields of identical frequencies, forming a volumetric intermittent energy field, whose dimensions per coordinate are determined based on the speed of light and the pair of coordinate radiating pulses.    USE - Obtaining hydrogen from water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hydrogen obtaining device.
NOVELTY - The method involves transporting waste water and waste material from cleaning and disinfection apparatuses and sanitary appliances to a separating device via a sewer system for separating into a liquid phase (42) and solid phase. The liquid phase is processed and treated to produce industrial water for feeding into the system. The solid phase is treated in a fermentation gas reactor for generate fermentation gas. The produced industrial water is fed into a water inlet (40) for supply of the cleaning and disinfection apparatuses, the sanitary appliances or end users.    USE - Method for treating kitchen wastes and leftovers (all claimed) e.g. medicament residue, effluent, organic and/or inorganic wastes of a care device such as hostel, clinical center, and hospital.    ADVANTAGE - The method enables treating waste water and waste material, so that effluent amount delivered to a treatment device can be reduced, effluent costs for an operator can be reduced, and water consumption can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an effluents and wastes water treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a treatment system for treatment of waste water or waste of a care facility.    Water inlet (40)    Liquid phase (42)    Treatment facilities (46-58)    Intermediate heating part (60)    Thermal disinfection part (62)
NOVELTY - A recombinant Myceliophthora thermophila polypeptide comprising an amino acid sequence identified in any of Tables 1-4, given in the specification, is new.    USE - The recombinant M. thermophila polypeptide and composition are useful for degrading a cellulosic biomass (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated nucleic acid encoding a polypeptide above;    (2) a recombinant vector comprising at least one nucleic acid of (1), where the nucleic acid is operably linked to a promoter;    (3) a recombinant host cell comprising at least one recombinant vector of (2), or at least one nucleic acid of (1) operably linked to a heterologous promoter, or a recombinant host cell in which expression of one or more genes encoding at least one polypeptide selected from the polypeptides of any of Tables 1-4 is disrupted;    (4) a method of producing a polypeptide above;    (5) a method for degrading a cellulosic biomass by contacting the cellulosic biomass with a composition comprising a recombinant biomass degradation polypeptide above;    (6) a composition comprising a cellulose and at least one recombinant biomass degradation polypeptide above; and    (7) a method of increasing production of active protein from a host cell by modifying expression of a protein production polypeptide of any of Tables 1-4 in the host cell.
NOVELTY - Aerobic fermented biogas residue complex microbial agent, comprises Bacillus e.g. B.subtilis strain BCRC 10058, Pseudomonas chosen from P.fluorescens strain PC17, Staphylococcus e.g. S.aureus strain JCM 2418, Streptomyces chosen from Streptomyces strain HBUM174047, Penicillium chosen from P.lilacinus, Aspergillus e.g. A.niger strain BAB1132, and Trichoderma e.g. T.viride strain NW537.    USE - As aerobic fermented biogas residue complex microbial agent.    ADVANTAGE - The aerobic fermented biogas residue complex microbial agent is environmentally-friendly, and overcomes problem of rural energy.    DETAILED DESCRIPTION - Aerobic fermented biogas residue complex microbial agent, comprises Bacillus at least one chosen from B.subtilis strain BCRC 10058, B.licheniformis strain BCRC 15413, B.megaterium strain BAB 2927, B.subtilis strain JM4, and B.megaterium strain BAB 2761, Pseudomonas chosen from P.fluorescens strain PC17, Staphylococcus at least one chosen from S.aureus strain JCM 2418, Staphylococcus strain IP105758, Staphylococcus strain F11, and Staphylococcus CIP103274, Streptomyces chosen from Streptomyces strain HBUM174047, Penicillium chosen from P.lilacinus, Aspergillus at least one chosen from A.niger strain BAB1132, A.glaucus strain NBRC 15417, A.niger strain Ter-331, A.niger strain C3-1, and Trichoderma chosen from T.viride strain NW537, T.viride strain Grl35, and Trichoderma strain FUE9. An INDEPENDENT CLAIM is included for preparation of the biogas residue, which involves preparing bacterial suspension, inoculating seed medium at 30 degrees C for 48 hours under 220 rotations per minute (rpm) to obtain seed liquid, inoculating the 10% culture in the fermentation medium, expanding the fermentation culture, mixing broth with sterilized bran, and preparing product.
NOVELTY - Bacillus brevis bacterial strain (I) having preservation number of CCTCC NO: M2013597, is new.    USE - (I) is useful in livestock and poultry including chicken, duck, goose, pig, cow, sheep and horse, and for deodorizing domestic rubbish including municipal domestic rubbish and municipal domestic fresh rubbish (all claimed).    ADVANTAGE - (I) has strong deodorizing ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing (I) comprising inoculating Bacillus brevis strain into lysogeny broth culture medium to culture at 4-61 degrees C.
NOVELTY - Producing bio-microbial fertilizer comprises: adding decomposing strain into cottonseed meal; activating and expanding the decomposing strain by internal heat of stacked cottonseed meal; uniformly mixing decomposed strain cottonseed meal with chicken manure; stacking the mixture, immediately turning the chicken manure for cooling when the temperature reaches 40-50 degrees C, stacking again until the temperature reaches 58-65 degrees C to obtain fermented odorless bio-fertilizer; and drying the bio-fertilizer aerobically, granulating, then bagging or directly adding into crops.    USE - The bio-microbial fertilizer is useful for saline-land crops (claimed).    DETAILED DESCRIPTION - Producing bio-microbial fertilizer comprises: (i) adding 2-4 pts. decomposing strain into 100 pts. cottonseed meal; (ii) activating and expanding the decomposing strain by internal heat of stacked cottonseed meal, immediately turning the cottonseed meal for cooling when the internal temperature reaches 40-50 degrees C, continuing to accumulate, immediately turning the cottonseed meal when the internal temperature reaches 58-65 degrees C, and stacking again until the temperature reaches 58-65 degrees C to obtain decomposed cottonseed meal; (iii) uniformly mixing 1-3 pts. decomposed strain cottonseed meal with 50-70 pts. chicken manure; (iv) stacking the mixture, immediately turning the chicken manure for cooling when the internal temperature reaches 40-50 degrees C, continuing to accumulate, immediately turning the chicken manure when the internal temperature reaches 58-65 degrees C, and stacking again until the temperature reaches 58-65 degrees C to obtain fermented odorless bio-fertilizer; and (v) drying the bio-fertilizer aerobically, granulating, then bagging or directly adding into crops. An INDEPENDENT CLAIM is also included for bio-microbial fertilizer, produced by above mentioned method.
NOVELTY - Improving low temperature fluidity of biodiesel, comprises adding methanol to biodiesel, forming a clathrate compound to flocculate saturated fatty acid methyl esters contained in the biodiesel, removing the clathrate compound, and mixing the additive biodiesel with removed clathrate compound.    USE - The method is useful for improving low temperature fluidity of biodiesel from vegetable oils and animal fats with a high content of saturated fatty acids (all claimed).    ADVANTAGE - The method effectively improves low temperature fluidity of biodiesel.
NOVELTY - Carbonyl-containing oxygenates are subjected to a carbon-carbon bond forming condensation reaction. The oxygenates are 3C oxygenates, 4C oxygenates, and/or 5C oxygenates derived from a bio-oil stream. The condensates are hydrotreated to form a hydrotreated feed stream and 6C or higher renewable biofuel is generated from the hydrotreated feed stream.    USE - Production of renewable biofuel from hydrotreated bio-oil.    ADVANTAGE - The method increases the yield of 6C or higher hydrocarbons from pyrolysis oil or bio-oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) process for enhancing the yield of hydrotreated bio-oil from a bio-oil stream containing oxygenates, which involves subjecting the oxygenates to a carbon-carbon bond forming condensation reaction and hydrotreating the condensate(s) to render the hydrotreated bio-oil. The yield of hydrotreated 6C or higher hydrocarbons is greater than the yield obtained in a similar process which does not include subjecting the oxygenates to condensation prior to hydrotreating; and    (2) A process for producing a renewable biofuel from a hydrotreated bio-oil which comprises: (a) subjecting a feedstream containing carbonyl oxygenates to a carboncarbon bond forming condensation reaction in the presence of an acidic or basic catalyst, wherein the oxygenates are selected from the group consisting of C3 oxygenates, C4 oxygenates and C5 oxygenates and mixtures thereof and further wherein the C3, C4 and C5 oxygenates originate from a bio-oil stream; (b) hydrotreating the condensates of step (a) to form a hydrotreated feedstream; and (c) generating a C6+ renewable biofuel from the hydrotreated feedstream. wherein the condensation in step (a) and the hydrotreating in step (b) occurs in different reactors.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the process in which a biomass-derived stream is condensed prior to introduction into a hydrotreater.
NOVELTY - Hormonema sp. strain is a fungal strain and has deposition number CECT 13092, and is new. Hormonema sp. strain has 162-167 nucleobases (SEQ ID NOs: 1-2), given in the specification.    USE - Hormonema sp. strain used for producing bioethanol (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for delignification of lignocellulosic biomass, which involves incubating Hormonema sp. strain and lignocellulosic biomass i.e. biopulp for 18-38 days at 18-28 degrees C and then performing hydrogen peroxide bleaching.
NOVELTY - Alcohol esters purification involves preparing alcohol esters by catalytic transesterification of vegetable oils or animal fats with low molecular weight alcohols and by washing with an acidified solution.    USE - Method for improving purification of alcohol esters of fatty acids, such as methyl, ethyl, propyl and butyl esters for use as fuel.    ADVANTAGE - The method improves purification of alcohol esters in a simple and cost-effective manner by using citric acid solution that significantly enhances oxidation stability of biodiesel without changing other properties, and provides biodiesel according to European standards (EN 14142) specifications.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the alcohol esters purification method. (Drawing includes non-English language text).
NOVELTY - Producing microbial organic fertilizer from municipal solid waste by applying bio-specific gas production for annealing, is disclosed.    USE - The process is useful for producing microbial organic fertilizer from municipal solid waste. No biological data given.
NOVELTY - Extracting and purifying natamycin from fermentation liquor comprises (a) regulating pH of natamycin fermentation liquor to 5-6.5, filtering, removing water, and collecting solid; (b) cleaning collected solid, allowing to stand, centrifuging and collecting solid; (c) adding sodium carbonate solution to obtain extract liquid, subjecting to ultrasonic oscillation treatment and solid-liquid separation, and collecting supernatant; and (d) regulating pH of supernatant using hydrochloric acid to 5-6, allowing to stand, crystallizing, filtering, collecting the solid, washing, freezing, and drying.    USE - The method is useful for extracting and purifying natamycin from fermentation liquor (claimed).    ADVANTAGE - The method: is simple; produces natamycin with high yield and high purity; does not use organic solvent; has low cost; is environmentally-friendly, and suitable for industrial production.
NOVELTY - Manufacture of fuel biodiesel involves mixing sodium borohydride with food waste oil or tung oil, adding sulfuric acid, removing odor from food waste oil, adding acid catalyst, methanol and primary fatty acid ester, precipitating, adding alkaline catalyst to produce secondary fatty acid ester, refining, and distilling fatty acid ester.    USE - Manufacture of fuel biodiesel used as light oil (claimed).
NOVELTY - Exporting renewably generated hydrogen from Australia to export markets comprises: generating electricity in Australia from facility powered by renewable energy e.g. wind, solar, biomass or geothermal; storing electricity that is intermittent in liquid air or liquid nitrogen forms and using stored electricity to power electrolysis plant in Australia to split water into hydrogen and oxygen; converting renewably generated hydrogen into vector or carrier to export e.g. liquid hydrogen, ammonia, methylcyclohexane or methane (liquid natural gas); and transporting vector via ships to export markets.    USE - The method is useful for exporting renewably generated hydrogen from Australia to export markets.    ADVANTAGE - The method provides regular and scheduled production of renewably generated hydrogen for export.
NOVELTY - Preparation of 2-((6-chloro-3-methyl-2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)methyl)benzonitrile compound (I) involves reacting 2-((6-chloro-2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)methyl)benzonitrile compound (II) and methanol in presence of a reducing agent, and carrying out Mitsunobu reaction in organic solvent.    USE - Preparation of benzonitrile compound used as intermediate for preparing alogliptin compound (claimed).    ADVANTAGE - The safe benzonitrile compound is environmentally-friendly manufactured.    DETAILED DESCRIPTION - Preparation of 2-((6-chloro-3-methyl-2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)methyl)benzonitrile compound of formula (I) involves reacting 2-((6-chloro-2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)methyl)benzonitrile compound of formula (II) and methanol in presence of a reducing agent, and carrying out Mitsunobu reaction in organic solvent. An INDEPENDENT CLAIM is included for preparation of alogliptin compound of formula (IV) or its salt, which involves reacting 2-((6-chloro-3-methyl-2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)methyl)benzonitrile compound (I) and (R)-3-aminopiperidine dihydrochloride of formula (VI) in organic solvent and alkali, and optionally reacting alogliptin (IV) and benzoic acid to obtain alogliptin benzoate of formula (V).
NOVELTY - Synthesis of cinepazide maleate involves: (a1) reacting pyrrolidine with chloro-acetyl chloride to form 2-chloro-1-pyrrolidin-1-yl-ethanone (II); (b1) reacting the ethanone (II) with piperazine in presence of ethanol to form 2-piperazin-1-yl-1-pyrrolidin-1-yl-ethanone (III); (c1) reacting (E)-3-(3,4,5-trimethoxy-phenyl)-acrylic acid with thionyl chloride to form 3,4,5-trimethoxycinnamic chloride (IV); (d1) reacting the ethanone (III) with the compound (IV) to form free base of cinepazide; and reacting the free base of cinepazide with maleic acid.    USE - For the preparation of cinepazide maleate (claimed) which is useful for treating cardiovascular and cerebrovascular diseases.    ADVANTAGE - The method is simple, economical, practical, and easy for industrial production of cinepazide maleate; and provides product in high yield. Particularly the present method does not use highly toxic solvents and inflammable and explosive reagents, thus is environment-friendly and industrially safe.    DETAILED DESCRIPTION - Synthesis of cinepazide maleate involves: (a1) reacting pyrrolidine with chloro-acetyl chloride to form 2-chloro-1-pyrrolidin-1-yl-ethanone (II); (b1) reacting the ethanone (II) with piperazine in presence of ethanol to form 2-piperazin-1-yl-1-pyrrolidin-1-yl-ethanone (III); (c1) reacting (E)-3-(3,4,5-trimethoxy-phenyl)-acrylic acid with thionyl chloride to form 3,4,5-trimethoxycinnamic chloride (IV); (d1) reacting the ethanone (III) with the compound (IV) to form free base of cinepazide; and reacting the free base of cinepazide with maleic acid. The step (a1) and (d1) involves use of alkaline solution. The step (b1) involves use of acid binding agent selected from triethylamine or potassium carbonate; and removal of excessive piperazine by acetone crystallization, or by dissolving excessive piperazine in organic solvent.
NOVELTY - A highly-enriched refining apparatus of biomethane from biogas has gas supply line in which collected livestock waste is supplied, bio-filter module which is installed in the supply line in which bio-gas, particles larger than predetermined size and water content are removed, bio-gas supply line which is connected to a bio-membrane unit in which resultant product of filter module is supplied, carbon dioxide discharge line in which separated carbon dioxide is provided through membrane unit, and purified biomethane emission line in which biomethane is supplied through membrane unit.    USE - Highly-enriched refining apparatus of biomethane from biogas (claimed).
NOVELTY - This utility new type claims a strengthening denitrification and phosphorus removal of one function of town sewage treatment device, the sewage treatment device comprising a main body processing facility, an aeration and washing system, a sludge discharging system, sewage reflux system is composed of a main body processing device of sloping-pipe precipitated pool, returning tank, an anoxic reaction tank, an aerobic reaction tank, a buffer tank and reaction tank, deodorizing decolouring reaction tank, in the anoxic reaction tank fill with cob core, an aerobic reaction pool in fill with a spherical light porous biological filter material, the upper growth of aerobic heterotrophic bacteria of organic pollutant in the sewage removing under the aerobic condition, ammonia nitrogen is oxidized to nitrate; and dephosphorization reaction pool in is filled with slow release phosphorus removal filter material, in the water of phosphate radical ion. The device construction with small scale, low operation cost, no need to add any chemical agent, the town domestic sewage in most of organic matter process, and enhances the removal of nitrogen and phosphorus, the water processing and recycling to reach the discharge standard.
NOVELTY - Producing biofuel from glycerin, comprises (i) dissolving glycerin in water; (ii) adding a metal catalyst to the obtained glycerin solution; (iii) adding a radical initiator to the mixture obtained in the step (ii); (iv) reacting by maintaining the reaction pressure below the vapor pressure of volatile organic compounds of the mixture to generate vapors; and (v) condensing the vapors to obtain volatile organic compounds.    USE - The method is useful for producing biofuel from glycerin (claimed).    ADVANTAGE - The method is environmentally friendly and economical, recycles wastes and produces biofuel which can replace fossil fuels to reduce emissions and toxic substances upon combustion of fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow of producing biofuel from glycerin (Drawing includes non-English language text).
NOVELTY - The system (10) has a return line (710) that supplies the waste gas to refining portion (200). The refining portions (100-300) produce the refinery gases and the waste gases. A presser portion (400) pressurizes the source gas and waste gas. The pressurized source gas and waste gas are refined in presser portion and second refining portion. A buffer tank (600) mixes the third waste gas with first waste gas which is supplied through return line. The first refinery gas and third refinery gas are provided to produce gas to consumer.    USE - System for refining natural gas such as methane gas and shale gas from gas well.    ADVANTAGE - The natural gas from gas well is changed by combustion, such that the collection rate of high purity methane can be increased efficiently. The power consumption of gas purification system can be reduced reliably. The size of buffer tank can be reduced effectively, such that waste gas generated in refining portion can be utilized. The cost of gas purification system can be reduced reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for Gas purification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas purification system. (Drawing includes non-English language text)    Gas purification system (10)    Refining portions (100-300)    Presser portion (400)    Buffer tank (600)    Return line (710)    Check valve (910)
NOVELTY - The system has chiller that supplies the catalyst oxidizing water of the low temperature to the packing tower through the heat exchange with the solvent of the regenerator (62). A high temperature heat exchanger (70) supplies the catalyst oxidizing water of the high temperature to the packing tower. A chiller (50) maintains the high temperature state using the refrigerant for removing the moisture within the biogas flowed out of the packing tower. A plastic filler broadens the contact area between the biogas and the catalyst oxidizing water.    USE - Refinery system for bio gas containing malodorous substance and siloxane gas.    ADVANTAGE - The front end processor of the biogas including the bad smell material and the siloxane generated in the anaerobic digestion process can be prevented. The siloxane included among the biogas can be completely removed, after filling the activated charcoal to the second-order product. The processing of the flux change is possible through the gas-liquid. The solubility towards the catalyst oxidizing water of the siloxane is increased and the removal efficiency of the siloxane is improved by increasing the disassembly efficiency of the siloxane. The siloxane removal efficiency can be maximized using the plastic of the material. The replacement time of each activated charcoal can be shortened and can evenly disperse the flow direction of the biogas with the branching board.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the refinery system.    Dust removal filter (10)    Chiller (50)    Regenerator (62)    High temperature heat exchanger (70)    Adsorption tower (80)
NOVELTY - The method comprises introducing molasses containing 52% of sugar with bacteria into anaerobic biogas digester, and diluting molasses with pure water to obtain a diluted solution containing 98.15% of pure water and 1.85% of molasses. The water has pH of 7.5. Organic matter of molasses is mixed with pure water.    USE - The method is useful for producing biogas (claimed).    ADVANTAGE - The method is capable of economically and efficiently producing the biogas with high productivity.
NOVELTY - A hydrophobic sorbent substance and liquidized sludge are mixed in a vessel to form a mixture, and left for residence time such that the hydrophobic contaminant is substantially sorbed out of the sludge and into the hydrophobic sorbent substance. Then, non-contaminant-laden hydrophobic sorbent substance is physically separated from the liquidized sludge. Thus, hydrophobic contaminant removing process is carried out.    USE - Method for removing hydrophobic contaminant from liquidized sewage sludge used for manufacturing biosolids fertilizer (claimed).    ADVANTAGE - The method enables effective removal of hydrophobic contaminant from liquidized sewage sludge by environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biosolids fertilizer, which is obtained by liquefying the liquidized biosolids sludge containing hydrophobic contaminants such that hydrophobic contaminants are diminished to 50% or less.
NOVELTY - The method involves adding phosphate slurry with mineral oil sludge, waste sludge, soybean and/or cottonseed to obtain a mixture. The obtained mixture is homogenized using a homogenizer.    USE - Method for manufacturing a mixed organic-mineral fertilizer for plants using phosphate sludge from a furniture industry.    ADVANTAGE - The method enables using waste from a furniture industry for agricultural application so as to protect environment.
NOVELTY - Preparation of radix berberidis extract comprises crushing radix berberidis, extracting 2 times in boiling water, where each extraction time is 30-40 minutes, and filtering; combining filtrates and concentrating; drying; and purifying using macroporous resin chromatographic column, washing with alkaline water, eluting in chromatographic column using ethanol, collecting ethanol eluent, concentrating, and drying to obtain an extract containing a tleast 80% berberine hydrochloride.    USE - Method for preparing radix berberidis extract (claimed).    ADVANTAGE - The method is simple, short, and easy and has low energy consumption and high extracting efficiency. The extract has 80% purity.
NOVELTY - Synthesizing isocyanate compound as key intermediate for hypoglycemic drug, involves: carrying out ester exchange reaction of methyl isocyanate and alcohol compound in the presence of a catalyst; and after processing, distilling to obtain the target product comprising isocyanate compound and methanol.    USE - For synthesizing isocyanate compound as key intermediate for hypoglycemic drug (claimed).    ADVANTAGE - The method for synthesizing isocyanate compound, is featured with simple technique, easy operation, no pollution and high yield of product; and is safe, reliable and convenient.    DETAILED DESCRIPTION - Synthesizing isocyanate compound as key intermediate for hypoglycemic drug, involves: carrying out ester exchange reaction of methyl isocyanate and alcohol compound of formula ROH in the presence of a catalyst; and after processing, distilling to obtain the target product comprising isocyanate compound of formula RNCO and methanol.    R=not defined.
NOVELTY - An isolated or recombinant lipase polypeptide comprising a sequence that is at least 80% identical to SEQ ID NO: 2 and having at least one or more mutations at a residue selected from Arg33, Leu64, Ala70, Gly181, Gly202, Lys208, Ser238, Gly266 and its combination and where the polypeptide has lipase activity and improved methanol tolerance and/or thermostability compared to a wild-type lipase of SEQ ID NO: 2, is new. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The isolated or recombinant lipase polypeptide is useful for producing fatty acid from tri-, di- or mono-glyceride (claimed); and for producing biodiesel products.    ADVANTAGE - The polypeptide has lipase activity and improved methanol tolerance and/or thermostability compared to wild-type lipase (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated or recombinant polynucleotide encoding the polypeptides;    (2) a vector comprising the polynucleotide;    (3) a host cell transfected with the polynucleotide or the vector; and    (4) a method of producing a fatty acid from tri-, di- or mono-glyceride comprising contacting the tri-, di- or mono-glyceride with the polypeptide under conditions where a fatty acid methyl ester is produced; or a method of producing a fatty acid from a tri-, di- or mono-glyceride comprising contacting the tri-, di- or mono-glyceride with the host cell under conditions where a fatty acid methyl ester is produced.
NOVELTY - Producing light oil fraction with low fatty acids from plant and animal-based fats, oils or greases involves introducing feedstock comprising free fatty acids (FFA) into processing system; heating feedstock to predetermined temperature at predetermined rate selected to produce light oil fraction with reduced fatty acid content; permitting feedstock to reflux at predetermined temperature for predetermined time selected to produce light oil fraction with reduced fatty acid; and separating light oil fraction from remainder of feedstock, where separated light oil fraction contains less than or equal to 10% FFA.    USE - For producing light oil fraction with low ( less than or equal to 1%) fatty acids from plant-based and/or animal-based fats, oils or greases (claimed); for making kerosene-range fuels such as jet fuel.    ADVANTAGE - The method produces light oil fraction with reduced free fatty acids from renewable source of fatty acids. The processing system is catalyst-free or catalyst may be used if desired, under relatively mild conditions. The process works by balancing decarboxylation and cracking reactions and by combining reactor with various separation strategies.
NOVELTY - Jet-range hydrocarbon product comprises a mixture of paraffins. The mixture exhibits a freeze point of less than or equal to -70 degrees C, a 95% distillation point of greater than or equal to 275 degrees C, and a smooth boiling point curve that is characterized as having no intervals of the boiling point curve having a slope that is steeper than 4 degrees C/mass% as defined by ASTM standard D2887 between mass recovered ranges of 20-80%. The steepness of the boiling point curve slope is calculated over any 10 mass% increments within the specified mass% ranges.    USE - The jet-range hydrocarbon product is useful in an aviation industry.    ADVANTAGE - The jet-range hydrocarbon product: can be produced from a biorenewable feedstock that does not include fatty acids or esters and have a boiling point distribution that more closely resembles petroleum-derived jet-range fuels, thus reducing reliance on petroleum-based sources; and exhibits smooth boiling point characteristics.
NOVELTY - Producing jet-range hydrocarbons involves: passing a stream comprising renewable C4 olefins to an oligomerization reactor containing a zeolite catalyst to produce an oligomerized effluent; separating the oligomerized effluent to produce a jet range hydrocarbon stream and a recycle stream comprising C8 olefins; and passing at least a portion of the recycle stream to the oligomerization reactor.    USE - The method is useful for producing jet-range hydrocarbons (claimed).    ADVANTAGE - The method produces jet-range fuels from a biorenewable feedstock without including fatty acids or esters, where the jet-range fuels have a boiling point distribution that more closely resembles petroleum-derived jet-range fuels.    DETAILED DESCRIPTION - Producing jet-range hydrocarbons involves: passing a stream comprising renewable C4 olefins to an oligomerization reactor containing a zeolite catalyst to produce an oligomerized effluent; separating the oligomerized effluent to produce a jet range hydrocarbon stream and a recycle stream comprising C8 olefins; and passing at least a portion of the recycle stream to the oligomerization reactor, where a first at least 10% of the jet-range hydrocarbon stream hydrocarbons boil between n-octane and n-undecane and where a second at least 10% of the jet-range hydrocarbon stream hydrocarbons boil between n-dodecane and n-pentadecane.
NOVELTY - Preparation of a sugar product from ligno-cellulosic material, involves (a1) optionally pre-treatment of the ligno-cellulosic material; (b1) optionally washing of the optionally pre-treated ligno-cellulosic material; (c1) enzymatic hydrolysis of the optionally washed and/or optionally pre-treated ligno-cellulosic material using an enzyme composition comprising at least two cellulase; and (d1) optionally recovery of a sugar product, where after the pre-treatment and before and/or during the enzymatic hydrolysis oxygen is added to the ligno-cellulosic material.    USE - For the preparation of a sugar product and fermentation product (claimed) which are converted into valuable products e.g. sugars or bio-fuel, such as bio-ethanol.    ADVANTAGE - The hydrolysis step is conducted at improved and optimized conditions, reduced process time. The present method reduces the dosage of enzyme and at the same time output of useful hydrolysis product is maintained at the same level or even increased. By the addition of oxygen it is possible to attain many process advantages, including optimal temperature conditions, reduced process time, reduced dosage of enzyme, re-use of enzymes, higher yields and other process optimizations, resulting in reduced costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of a fermentation product from ligno-cellulosic material, involving: carrying out steps (a1) to (c1); (e1) fermentation of the hydrolyzed ligno-cellulosic material to produce a fermentation product; and (f1) optionally recovery of a fermentation product, where after the pre-treatment and before and/or during the enzymatic hydrolysis oxygen is added to the ligno-cellulosic material.
NOVELTY - Preparing (P1) triazole compound involves reacting 2,6-difluorobenzyl azide with 2,3-dihalo compound to form triazole compound.    USE - For preparing triazole compound which further used to form rufinamide (claimed), where the triazole compound and rufinamide is used for the treatment of epilepsy or convulsions, particularly for the treatment of Lennox-Gastaut syndrome and other seizure disorders.    ADVANTAGE - The present process provides single pot preparation of rufinamide, thus avoiding the separation of the intermediates, which can be tedious. Also, the use of expensive reagents is avoided, which makes the process industrially advantageous and economical. The yield and purity of the products obtained by the process is much higher than the known processes.    DETAILED DESCRIPTION - Preparing (P1) triazole compound of formula (I) involves reacting 2,6-difluorobenzyl azide of formula (II) with 2,3-dihalo compound of formula X1-CH2-CH(X2)-C(=O)-R (III) to form compound (I).    R=-OR1 or NH2;    R1=H or 1-6C alkyl group;    X1 and X2=Cl, F, Br or I.    INDEPENDENT CLAIMS are included for the following:    (1) preparing (P2) 2,6-difluorobenzyl azide (II) involving reacting 2,6-difiuorobenzyl halide of formula (V) and an azide in the presence of an activating agent, hydrazine hydrate to form (II); and    (2) preparing rufinamide involving reacting compound (V) with an azide in the presence of hydrazine hydrate to form 2,6-difluorobenzyl azide (II), reacting (II) with 2,3-dihalo compound (III) to form compound (I), and reacting compound (I) with an aminating agent to form rufinamide.    X=Cl, Br or I.
NOVELTY - The structure has a bioreactor whose operating sections are provided with different diameters. The mechanical agitators are fixed on radial shafts. The working portions of bioreactor are divided into two portions by thin cylindrical partition. The partitions are centered by ring-shaped groove of pallet. The bottom portion of partitions is provided with opening for overflow of liquid. A beam separator is provided to separate heat-transfer agent from central collector connected with gas boiler which is installed outside of bioreactor.    USE - Installation structure for utilization of organic wastes.
NOVELTY - Composition comprises a solvent soluble extract of switchgrass.    USE - The composition useful for: preventing or treating an infection by an infectious agent in a plant, where the plant is tomato plant and the infectious agent is a bacterium including Clavibacter michiganensis subsp. michiganensis, Xanthomonas perforans, Pseudomonas syringae pv. Tomato or Pseudomonas mediterranea or a fungus including Fusarium sp. or Fusarium oxysporum; preventing food spoilage of a food product or inhibiting a food-borne pathogens in a food product, where the food-borne pathogen is Salmonella typhimurium, Salmonella enteritidis or Staphylococcus aureus; treating inflammation; and treating obesity (all claimed). Test details are described but no results given.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for processing Panicum virgatum (switchgrass) biomass, comprising obtaining the switchgrass biomass, treating the switchgrass biomass with the solvent and separating the solvent-soluble extractives portion of the switchgrass biomass from the cellulosic and/or lignocellulosic portion of the switchgrass biomass, and optionally, producing a biofuel from the cellulosic and/or lignocellulosic portion of the switchgrass biomass
NOVELTY - Recombinant cell having a nucleotide sequence encoding a polypeptide which is a lipase having at least 40% amino acid sequence identity to a polypeptide having a sequence of SEQ ID NO: 1 (comprising a fully defined sequence of 1147 amino acids as given in the specification), is new.    USE - The recombinant cell is useful for producing TAG, and increasing oil production in which amount of monounsaturated fatty acids in the oil is increased (all claimed), where the oil is useful in high-quality biodiesel.    ADVANTAGE - The recombinant cell is capable of producing oil that has high energy density, and provides biodiesel with high quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (M1) for producing triacylglycerol (TAG), comprising providing the recombinant cell, and culturing the cell under conditions that produce oil having TAG; and    (2) a method (M2) for increasing oil production, comprising providing the recombinant cell, and culturing the cell under conditions that produce oil in an amount that is increased relative to a corresponding non-recombinant cell.
NOVELTY - The fuel cell module (12) includes a first area (R1) where an exhaust gas combustor (52) and a start-up combustor (54) are provided, a second area (R2) where a reformer (46) and an evaporator (48) are provided, and a third area (R3) where a heat exchanger (50) is provided. A heat stress relaxing portion (117) is provided at least along a border between the first area and the second area, along a border between the second area and the third area, or along an outermost circumferential portion of the third area.    USE - Solid oxide fuel cell module for generating electricity by electrochemical reactions of fuel gas and oxygen-containing gas.    ADVANTAGE - Heat waste and heat radiation are suppressed suitably, thus improvement in the heat efficiency is achieved, and thermally self-sustaining operation is facilitated. A simple and compact structure is achieved in the entire fuel cell module. Degradation in the durability of the fuel cell peripheral equipment due to heat stress is suitably suppressed.    DESCRIPTION OF DRAWING(S) - The drawing is a cross sectional view showing a fuel cell peripheral equipment.    Fuel cell module (12)    Reformer (46)    Evaporator (48)    Heat exchanger (50)    Exhaust gas combustor (52)    Start-up combustor (54)    Heat stress relaxing portion (117)    First area (R1)    Second area (R2)    Third area (R3)
NOVELTY - A method of preparing a blended homogenous fuel product involves providing a fossil fuel component and an alcohol component, and mixing the components through ultrasonic energy, where the homogenous fuel product comprises 1-45 vol/vol.% water by volume of the alcohol component.    USE - For preparing a blended homogenous fuel product (claimed).    ADVANTAGE - The method produces acceptably pure bioethanol, with reduction in the production cost associated with the process of water removal. In the process, the blended fuel product comprising fossil fuel and an ethanol is not phase separated as a result of the presence of water, as ultrasonic energy has an effect on the phase separation of the three components of the fuel blend.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a blended homogenous fuel product comprising a fossil fuel component and an alcohol component, where the fuel product is mixed through ultrasonic energy, and where the homogenous fuel product comprises 1 to 45 vol/vol.% water by volume of the alcohol component.
NOVELTY - The power supply device combines fuel cell and storage battery, and discharges heat generated from fuel cell outside, after using a storage battery for a mechanism for heat-retaining in a fixed temperature range. The heat is discharged from another exit, after introducing air into a space provided between a container and the storage battery by which the storage battery is accommodated and is used for heat retention mechanism of storage battery as a medium of heat generated from the fuel cell using the air which passes a air cooled heat exchanger of fuel cell.    USE - Power supply device for use during measurement of flood and landslide.    ADVANTAGE - The power supply device can supply stable electric power even when the storage battery deteriorates by charging/discharging at sub-zero temperature. The power supply device can be provided with suitable heat retention mechanism, such that the power supply device can be used at very low method of cold region and high ground of environmental temperature. Long-term electric power generation can be stably attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the power supply device.
NOVELTY - This utility new type relates to a one biomass gasification combustion boiler system, belonging to combustion device, belonging to the technical field of boiler, include boiler provide for biomass gasification furnace of the gasification fuel, biomass gasification furnace through a gas pipeline connecting with the boiler, upper part of said biomass gasification furnace set with a feeding port, the biomass gasification furnace from upper to lower in turn is gas storage room, reaction room hop between a reaction room with hop set with heating fire grate, a feeding port through one conveying pipeline and the reaction room connected, this utility new type of biomass gasification furnace of gas storage room and the reaction room are separated from each other, so the storage of the gas storage room in gasification fuel of a boiler combustion can continuously use, even if the process for biomass gasification furnace process of feeding in, and would not interrupt is combustion boiler of process, and maintain stable steam parameter of boiler of produce, which can ensure the production process of continuous process.
NOVELTY - The machine has a biomass automatic conveying storage system which is provided with a storage tank for storing biomass granule. A front straw automatic pickup preprocessing system is suspended on the walking chassis integrated system. The crushing integration system is installed in bottom disk of walking chassis integrated system. The crushing integrated system and biomass dense forming automatic conveying storing system are connected with each other through a transmission mechanism.    USE - Machine for collecting and crushing waste crop straw.    ADVANTAGE - The labor consumption for agricultural straw collecting process can be reduced, and efficiency of the transportation can be improved. The stable agricultural ecological balance can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the machine for collecting and crushing waste crop straw.    Conveying auger (3)    Primary conveyor belt (6)    Cyclone separator (8)    Baffle (11)    Regulating nut (13)
NOVELTY - Earthworm feed preparation involves garbage and sludge in mass ratio of 30-40 and 60-70 respectively. Glass, plastic, metal, rubber and ceramics are removed by machine. Garbage and sludge are crushed into 2-10mm particles and mixed uniformly. The material is piled, and then fermented. Each ton of feed is added with biological microbial inoculum (10-30kg) and then fermented for 50-80 hours. Residue of fermented product is placed into steam furnace for 3-8 hours at 80-105 degrees C.    USE - Method for preparing earthworm feed (claimed).    ADVANTAGE - The earthworm feed is cost-effective and eco-friendly.    DETAILED DESCRIPTION - Earthworm feed preparation involves garbage and sludge in mass ratio of 30-40 and 60-70 respectively. Glass, plastic, metal, rubber and ceramics are removed by machine. Garbage and sludge are crushed into 2-10mm particles and mixed uniformly. The material is piled, and then fermented. Each ton of feed is added with biological microbial inoculum (10-30kg) and then fermented for 50-80 hours. Residue of fermented product is placed into steam furnace for 3-8 hours at 80-105 degrees C. The obtained product is cooled to 30 degrees C. L-tyrosine, L-alanine, L-arginine, citicoline and taurine are added to the obtained product and pH is adjusted to obtain the earthworm feed.
NOVELTY - The method involves performing crushing process to obtain organic waste sand granule and waste plastic. Multi-level drying treatment process is performed, where reaction temperature is maintained at 350 to 500 degrees centigrade. Pneumatic ash separating process is performed to obtain oil gas. Gas present in a carbon black is removed. Dust-removing treatment process is performed by using heavy oil. Light oil cooling and three-phase separation processes are performed to obtain the heavy oil, the light oil, water and gas.    USE - Municipal domestic rubbish treatment processing method.    ADVANTAGE - The method enables avoiding municipal solid waste pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a municipal domestic rubbish treatment processing method.'(Drawing includes non-English language text)'
NOVELTY - A green synthesis method of flower-shaped copper oxide nanocrystal comprises preparing copper sulfate solution and mixed tartrate and sodium hydroxide solution, adding copper sulfate solution to mixed tartrate and sodium hydroxide solution, stirring, forming bright transparent solution, transferring to widemouth bottle, sealing, heating, centrifuging, and separating.    USE - Green synthesis method of flower-shaped copper oxide nanocrystal used for optoelectronic visible light photocatalytic degradation of rhodamine B and visible light photocatalytic hydrogen production (claimed).    ADVANTAGE - The nanocrystal surface area is 15-40 m2/g and band gap of 1.2-1.7 eV. The method is simple, low-cost, environment-friendly and suitable for industrialization.
NOVELTY - A double- membrane double-loop sewage treatment device comprises regulating tank (1), anaerobic/anoxic membrane bioreactor (2), aerobic membrane bioreactor (3), sludge thickening tank (4), water pump (7), anaerobic sludge pump (16) and aerobic sludge pump (17).    USE - Double-membrane double-loop sewage treatment device used for denitrifying and removing phosphorus.    ADVANTAGE - The simple and convenient method saves carbon sources and operating costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of double-membrane double-loop sewage treatment device.    Regulating tank (1)    Anaerobic/anoxic membrane bioreactor (2)    Aerobic membrane bioreactor (3)    Sludge thickening tank (4)    Water pump (7)    Anaerobic sludge pump (16)    Aerobic sludge pump (17)
NOVELTY - A composite microbial inoculum is used for treating sewage sludge from petrochemical industry.    USE - Composite microbial inoculum used for treating sewage sludge from petrochemical industry (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composite microbial inoculum application method comprising adding glutaraldehyde suspension to polyphenylene oxide, stirring, washing with phosphate buffer solution (PBS) containing calcium chloride, and standing to prepare biological carrier; amplifying microbial inoculum; adding amplified microbial inoculum to biological carrier; and continuously adding composite microbial inoculum to petrochemical sewage until organic contaminants and heavy metal in petrochemical sewage and sludge are converted into stable harmless substance.
NOVELTY - Biological carbon-iron composite material comprises carbon-based nano iron, and microorganism capable of degrading inorganic salt contaminants in water fixed on carbon-based nano iron.    USE - Biological carbon-iron composite material used for water purification by physical adsorption and biodegradation.    ADVANTAGE - The composite material improves water purifying efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological carbon-iron composite material preparation by using inorganic iron salt and activated carbon to prepare carbon-based nano iron; and introducing inorganic salt contaminant-degrading microorganism into carbon-based nano iron.
NOVELTY - Method for producing biogas, involves constructing digester supporting a livestock farm, where the digester capacity is to digest daily fecal material and sewage of farms, collecting fecal material and sewage in the digester, maintaining dry matter concentration of livestock manure at 6?- 12%, performing anaerobic bacterial fermentation for at least 93 days, and sterilizing the processed sewage.    USE - The method is useful for producing biogas, preferably methane which is used for power generation. The wastewater produced during biogas production, is used for cultivating e.g. reed and grass, or is directly discharged into natural water bodies. The residue produced during biogas production, is used as fertilizer (all claimed).    ADVANTAGE - The method enables to produce biogas continuously, and is environmentally-friendly. The biogas production system is self-automatic and cost-effective, consumes less energy, enables to mass produce biogas cost-effectively, caused no environmental pollution and energy shortage problem, provides improved economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas production system.
NOVELTY - Producing cassava residue decomposition agent comprises using filter mud, manioc waste, bagasse ash at a weight ratio 3-4:3-4:1-2, adding microbial cells, mixing uniformly, fermenting for 15-30 days, crushing and drying at low temperature to obtain cassava residue decomposition agent. The microbial bacterium is Bacillus licheniformis. The total weight filter mud, cassava residue and bagasse ash is 2-8 wt.%.    USE - Method for producing cassava residue decomposition agent (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for producing cassava residue decomposition agent (Drawing includes non-English language text).
NOVELTY - Producing straw decomposition agent comprises using filter mud, cassava residue and bagasse ash as raw materials at a weight ratio 3-4:3-4:1-2, adding microbial cells, mixing uniformly, fermenting for 25-40 days, crushing and drying at low temperature to obtain straw rotten agent. The total content of the filter mud, cassava residue and bagasse ash is 2-8 wt.%.    USE - Method for producing straw decomposition agent (claimed).
NOVELTY - A base fertilizer is prepared by high temperature fermentation of bacteria for 1-3 days to break down cellulose enzymes into organic fertilizer.    USE - A base fertilizer.    ADVANTAGE - The fertilizer is environment-friendly.
NOVELTY - A sustained-release corn fertilizer is prepared by preparing activated strain of Bacillus licheniformis, fermenting at 30-40 degrees C with pH value of 7.0-7.4, oscillating under aerobic condition at 150-250 revolutions/minute, adding monosodium glutamate solution, glucose and glutamate, fermenting for 48-72 hours, adding 1-3% ammonium bicarbonate to adjust pH to 6.2-6.4, spray granulating, drying, screening, cooling, packaging and storing.    USE - Method for preparing sustained-release corn fertilizer (claimed).    ADVANTAGE - The fertilizer reduces labor intensity and production cost.
NOVELTY - C4 liquefied gas recycling by removing C3 fraction involves taking isomerization reaction. The obtained product is cooled and then separated to obtain C4 liquefied gas.    USE - Method for recycling C4 liquefied gas by removing C3 fraction (claimed).    ADVANTAGE - The C4 liquefied gas recycling method enables to utilize material that is cost-effective.
NOVELTY - Manufacture of piperitone (V) involves reacting methyl isobutyl ketone (I) and formaldehyde under catalysis of hydrogen chloride, obtaining intermediate (II), performing Michael addition reaction of obtained product with acetoacetate in presence of as base catalyst, obtaining ester intermediate (III), performing intramolecular aldol condensation reaction of obtained product under alkaline condition, obtaining carboxylate compound (IV), hydrolyzing and acidifying.    USE - Manufacture of piperitone (claimed).    ADVANTAGE - The method efficiently enables manufacture of piperitone with suppressed waste generation.    DETAILED DESCRIPTION - Manufacture of piperitone of formula (V) involves reacting methyl isobutyl ketone (I) and formaldehyde under catalysis of hydrogen chloride, obtaining intermediate of formula (II), performing Michael addition reaction of obtained product with acetoacetate in presence of as base catalyst, obtaining ester intermediate of formula (III), performing intramolecular aldol condensation reaction of obtained product under alkaline condition, obtaining carboxylate compound of formula (IV), hydrolyzing and acidifying.
NOVELTY - Method of recycling waste acid generated during production of trifluralin involves mixing waste acid with 15-25 %mass sulfur trioxide, then adding fuming nitric acid at a certain temperature to mixture, and then denitrifying in cyclic process.    USE - Method of recycling waste acid generated during production of trifluralin (claimed).    ADVANTAGE - The method is carried out efficiently and economically using simple process.
NOVELTY - 2-Aryl benzothiazole derivatives (I) preparation involves utilizing aromatic hydrocarbon containing carbonyl derivative (II) and benzothiazole derivative (III) (raw material), dimethyl sulfoxide (solvent), copper salt (catalyst) and oxygen (oxidant). The obtained reaction mixture is heated at 120-130 degrees C to obtain 2- benzothiazole derivatives (I).    USE - Method for preparing 2-aryl benzothiazole derivatives (I) (claimed).    ADVANTAGE - The 2-aryl benzothiazole derivatives (I) preparation method is cost-effective and eco-friendly.    DETAILED DESCRIPTION - 2-Aryl benzothiazole derivatives of formula (I) preparation involves utilizing aromatic hydrocarbon containing carbonyl of formula (II) and benzothiazole derivative of formula (III) (raw material), dimethyl sulfoxide (solvent), copper salt (catalyst) and oxygen (oxidant). The obtained reaction mixture is heated at 120-130 degrees C to obtain 2- benzothiazole derivatives (I)..
NOVELTY - Purifying esomeprazole sodium involves dissolving esomeprazole sodium crude product (90 %) in water in weight ratio of 1:2-10. The obtained solution is decolorized by adding activated carbon and then filtered and filtrate is concentrated by heating at 60 degrees C. Organic solvent is added to concentrated filtrate to obtain solution that is heated at 60 degrees C. The obtained solution is crystallized by stirring at 30 degrees C for 2 hours. The crystallized product is filtered to obtain crystals that is dried to obtain pure white esomeprazole sodium.    USE - Method for purifying esomeprazole sodium (claimed).    ADVANTAGE - The method enables to purify esomeprazole sodium that ensures 99.9% purity in simple, reliable and eco-friendly manner.    DETAILED DESCRIPTION - Purifying esomeprazole sodium involves dissolving esomeprazole sodium crude product (90 %) in water in weight ratio of 1:2-10. The obtained solution is decolorized by adding activated carbon and then filtered. The filtrate is concentrated by heating at 60 degrees C. Organic solvent is added to concentrated filtrate to obtain solution that is heated at 60 degrees C. The concentrated solution is crystallized by stirring at 30 degrees C for 2 hours. The crystallized product is filtered to obtain crystals that is dried to obtain pure white esomeprazole sodium.
NOVELTY - 5 alpha -Androstanedione (I) is prepared by taking androst-4-ene-3,17-dione (II) and borohydride salt, reducing in alcohol to prepare androst-4-ene-3,17-diol (III), hydrogenating using palladium-carbon catalyst in alcohol to prepare tetracyclic hormone (IV), and performing Jones oxidation in organic solvent.    USE - Method for preparing 5 alpha -androstanedione (claimed).    ADVANTAGE - The safe and environment-friendly synthesis has short reaction route, high yield of greater than or equal to 70%, easy-to-control reaction, simple operation, greatly reduced cost, and common, cheap and widely available plant sources.    DETAILED DESCRIPTION - 5 alpha -Androstanedione of formula (I) is prepared by taking androst-4-ene-3,17-dione of formula (II) and borohydride salt, reducing in alcohol to prepare androst-4-ene-3,17-diol of formula (III), hydrogenating using palladium-carbon catalyst in alcohol to prepare tetracyclic hormone of formula (IV), and performing Jones oxidation in organic solvent.
NOVELTY - 17~a-acetoxy-11~b-(4-(N,N-dimethylamino)phenyl)-19-norpregna-4,9-dien-3,20-dione is prepared by taking 11~b-(4-(N,N-dimethylamino)phenyl)-17~a-hydroxy-19-norpregna-4,9-dien-3,20-dione, and acetylating in presence of strong base and excess acid.    USE - Method for preparing 17~a-acetoxy-11~b-(4-(N,N-dimethylamino)phenyl)-19-norpregna-4,9-dien-3,20-dione(claimed).    ADVANTAGE - The synthesis reduces reaction container volume, product cost, wastewater discharge and carbon dioxide emission.
NOVELTY - An amphiphilic surfactant-containing poly siloxane segment modifier is prepared by reacting vinyl silicone and polyethylene glycol-methoxy polypropylene-polyethylene glycol block copolymer, in presence of cerium salt as initiator under the protection of nitrogen, by aqueous phase interfacial polymerization to obtain polyvinyl silicone-polyethylene glycol-methoxy polypropylene-polyethylene glycol-polyvinyl silicone.    USE - Amphiphilic surfactant-containing poly siloxane segment modifier is used for preparation of filler-containing membrane for separation and purification of biomass (all claimed).    ADVANTAGE - The membrane containing amphiphilic surfactant-containing poly siloxane segment modifier has favorable separating property and long-term stability.    DETAILED DESCRIPTION - An amphiphilic surfactant-containing poly siloxane segment modifier is prepared by reacting vinyl silicone and polyethylene glycol-methoxy polypropylene-polyethylene glycol block copolymer, in presence of cerium salt as initiator under the protection of nitrogen, by aqueous phase interfacial polymerization to obtain polyvinyl silicone-polyethylene glycol-methoxy polypropylene-polyethylene glycol-polyvinyl silicone having structure of formula (I). The average molecular weight of polyvinyl silicone-polyethylene glycol-methoxy polypropylene-polyethylene glycol-polyvinyl silicone is 14000-25000.    n=1-8.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of amphiphilic surfactant-containing poly siloxane segment modifier, which involves mixing polyethylene glycol-methoxy poly propylene-polyethylene glycol block copolymer and vinyl silicone oil, adding deionized water to form an emulsion, slowly dripping initiator, stirring, reacting, and vacuum drying; and    (2) preparation of filler-containing membrane.
NOVELTY - Biomass multifunctional integrated furnace comprises shell (29), biomass gasification device, biomass gas burner and blower shell. Biomass gasification device gasification device comprises shell set with charging barrel (20). The lower barrel is set with furnace cavity (34). The furnace cavity through gasification agent nozzles (37) and pipeline is connected to blower. The gasification device shell wall is fixed with upper material pullout tooth (26). The charging barrel is set with cover. The biomass gas burner includes burner shell.    USE - Biomass multifunctional integrated furnace.    ADVANTAGE - The furnace is energy-efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass multifunctional integrated furnace.    Charging barrel (20)    Material pullout tooth (26)    Shell (29)    Furnace cavity (34)    Gasification agent nozzles (37)
NOVELTY - Processing of garbage and sludge comprises preprocessing garbage, dehydrating and drying sludge, mixing garbage and sludge, forming, carbonizing to generate oil product, solid product and gas product, separating gas product, sorting tar and sewage, separating char, storing and purifying gas product, and post-processing and recycling sewage, tar and char.    USE - Method for processing garbage and sludge (claimed).    ADVANTAGE - The method improves process efficiency, reduces cost and reduces environmental pollution caused by garbage and sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for garbage and sludge processing system comprising garbage preprocessing device, dehydrating device, drying machine, extrusion forming device, storage hopper, belt machine, carbonizing furnace, storage bin, condensing device, tar separating device, air storage tank, purifying device, and post-processing and recycling device.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of processing of garbage and sludge (Drawing includes non-English language text).
NOVELTY - A biomass cracking device comprises double-spiral feeder (1-10), pyrolysis reactor (1-1), cyclone separator (2-1), material returning room (2-2), bottom discharge hopper (1-8), ball valve, inlet orifice, air access port, heating resistance (1-9), distributing plate, guide tube, tapered steady flow baffle plate, discharge port, and fluidized air inlet.    USE - Biomass cracking device.    ADVANTAGE - The device has improved efficiency, and reduced dosage of catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass cracking device (Drawing includes non-English language text).    Pyrolysis reactor (1-1)    Discharge hopper (1-8)    Heating resistance (1-9)    Cyclone separator (2-1)    Material returning room (2-2)
NOVELTY - The device has a reaction tower (1) provided with a bracket. A top part of the reaction tower is provided with a catalyst inlet (7) and a reaction gas exit (8). A bottom part of the reaction tower is provided with a cooling gas inlet (4). A side wall of the reaction tower is provided with a biomass raw oil inlet. A catalyst regeneration device (6) is fixed with the catalyst inlet by using a pipeline. The biomass raw oil inlet is fixed to a transfer pump (12). A control end of a primary electromagnetic valve (V-1) is connected with a connecting end of a secondary electromagnetic valve (V-2).    USE - Biomass oil catalytic hydrogenation device.    ADVANTAGE - The device avoids catalytic hydrogenation process difficulty and deactivated catalyst regeneration difficulty and realizes heat removing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass oil catalytic hydrogenation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a biomass oil catalytic hydrogenation device.    Primary electromagnetic valve (V-1)    Secondary electromagnetic valve (V-2)    Reaction tower (1)    Cooling gas inlet (4)    Catalyst regeneration device (6)    Catalyst inlet (7)    Reaction gas exit (8)    Transfer pump (12)
NOVELTY - A biomass carbon gas cogeneration system comprises pyrolysis and gasification furnace (11), gas outlet (111), switching parts (21, 22), inner chamber (31, 32), tar filter element (311, 321), first pressure detecting part, second pressure detecting part, tar purifier, and valve.    USE - Biomass carbon gas cogeneration system.    ADVANTAGE - The system is simple, has high efficiency and high quality, and can adjust carbon gas ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass carbon gas cogeneration system.    Pyrolysis and gasification furnace (11)    Switching part (21, 22)    Inner chamber (31, 32)    Gas outlet (111)    Gas outlet (111)    Tar filter element (311, 321)
NOVELTY - The reformer has a kiln furnace (1) arranged in a furnace container (2) through a multicatalyzing bed (3). The multicatalyzing bed is provided with an upper gas-guide tube (10). The multicatalyzing bed is arranged with a lower gas-guide tube (11). The kiln furnace is fixed on a combustion room (6). A lower side of the kiln furnace is fixed with a waste cigarette pneuma exit part (13). A middle part of the kiln furnace is installed with a multi-gas burner (7). An upper part of the multicatalyzing bed is fixed with a feeding cover plate (8).    USE - Biomass fuel gas catalytic reformer.    ADVANTAGE - The reformer has simple structure, low investment and high cracking efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass fuel gas catalytic reformer.    Kiln furnace (1)    Furnace container (2)    Multicatalyzing bed (3)    Combustion room (6)    Multi-gas burner (7)    Feeding cover plate (8)    Upper gas-guide tube (10)    Lower gas-guide tube (11)    Waste cigarette pneuma exit part (13)
NOVELTY - A special synthetic fuel formulation comprises 92-93 wt.% methanol, 0.12-0.15 wt.% triethanolamine, 0.6-0.8 wt.% hydrogen peroxide, 3-4 wt.% water, 0.03-0.05 wt.% iron naphthenate, and balance essence.    USE - Special synthetic fuel formulation.    ADVANTAGE - The fuel formulation has heating value of about 7000 kcal. It is non-toxic and tasteless, has no residual liquid, and can be used at normal pressure. It has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special synthetic fuel formulation comprising dissolving triethanolamine in hydrogen peroxide-water solution, adding all remaining raw materials, mixing uniformly, and filling.
NOVELTY - Preparing movable straw granule fuel comprises stacking single stack to reserve 500-3000 tons, and naturally dehydrating till the water content is less than 35%; crushing dehydrated straw, carrying out fragmentation of less than 1 cm, delivering to the gas stream with water, and naturally dehydrating till the water content is less than 25%; crushing, conveying air flow, where the particle size is less than 2 mm; and secondary molding the material directly into the molding machine for forming a particle size of 20-30 mm and a product bulk density of 1000 kg/m3.    USE - Method for preparing movable straw granule fuel (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for preparing movable straw granule fuel (Drawing includes non-English language text).
NOVELTY - Molding a crushed straw biomass comprises crushing a straw biomass, feeding the crushed material into the extrusion molding machine for roll extrusion molding, introducing hot air, generating hot air from the first hot air source squeeze rollers and heating the crushed material, drying and screening crushed material.    USE - Method for molding crushed straw biomass (claimed).    ADVANTAGE - The method can improve efficiency and quality of the material after crushing.
NOVELTY - Preparing a composite derived fuel comprises crushing the kitchen garbage, sorting the food waste metal, single or double screw press dewatering the material for crushing; dehydrating, and high temperature drying, sterilizing, removing material in excess of water and a pathogenic microorganism, crushing the dried material, removing inorganic material in raw material, sieving, adding combustion improver, mixing the raw material and combustion improver at high temperature, and shaping.    USE - Method for preparing a composite derived fuel (claimed).    ADVANTAGE - The method has safe operation, low cost, small floor area, and short production period, does not need to add additional series of problems of caking agent, improves combustion efficiency of solid fuel, and is energy-saving and environment-friendly.
NOVELTY - A straw mixed fuel sludge production line comprises a sludge belt conveyor (20), a straw crusher (30), a straw pneumatic conveyer (40), a sludge straw granulating drying machine (10), a sleeve, a pelletizer, a gear box, a motor, an auger shaft, a bearing, and a microwave generator.    USE - A straw mixed fuel sludge production line.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the straw mixed fuel sludge production line.    Sludge straw granulating drying machine (10)    Sludge belt conveyor (20)    Straw crusher (30)    Straw pneumatic conveyer (40)
NOVELTY - Production of a renewable fuel comprises uniformly mixing solid wastes comprising 20-40% waste paint residue, 15-35% waste toner, 10-30% waste resins, 5-25% oil sludge, 5-20% waste organic coatings, 5-15% waste activated carbon, and 0.5-3% desulfurizing agent; and molding, and drying.    USE - Method for the production of a renewable fuel (claimed).
NOVELTY - Treatment of kitchen garbage comprises sorting kitchen garbage; removing metal, plastic, and glass debris; and dehydrating, and drying.    USE - Method for the treatment of kitchen garbage used as a solid fuel (claimed).    ADVANTAGE - The method is short, and has no side effects.
NOVELTY - Aspergillus niger strain MZ is new, which preserved in China general microbiological culture collection center under preservation number CGMCC No: 7464.    USE - Aspergillus niger strain MZ used as decomposing agent for fermenting crop straw for preparing biological fertilizer, and improving mushroom yield (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing Aspergillus niger strain MZ involves culturing Aspergillus niger in potato dextrose agar culture medium at 28 degrees C for 4 days, scraping flat surface of hyphae and cottonseed spores using sterile toothpick, inoculating scraped material into culture medium at 28 degrees C for 4-8 days to obtain product; and    (2) method for preparing biological fertilizer involves drying crop straw, crushing crop straw into fragments of less than 3 cm, inoculating Aspergillus niger strain MZ into crop straw fragments, where water content is 30-45%, fermenting inoculated mixture in trapezoidal chamber for 18-21 days, drying fermented product at 65 degrees C until the water content is less than 5%, crushing obtained product and sieving obtained product to obtain desired product.
NOVELTY - An Acinetobacter baumannii (YNWH 226), is new.    USE - Acinetobacter baumannii used for aerobic decolorizing and purifying congo red azo dye-containing wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the decolorization of congo red azo dye-containing wastewater comprising placing wastewater into aerobic tank, adding inorganic salt culture medium, performing colony separation and purifying.
NOVELTY - Microalgae flocculation involves collecting microalgae, and then glycine and microalgae are mixed with continuous stirring, and then cultured in culture medium. The pH of obtained solution is adjusted, and solution is transferred into glass vessel containing liquid, and then obtained solution is kept for 4-24 hours. The obtained layers are separated to collect lower layer of microalgae biomass after dehydration.    USE - Method for flocculating microalgae (claimed).    ADVANTAGE - The method enables to flocculate microalgae by reducing cost of microalgae cultivation.
NOVELTY - Organic fertilizer preparation involves utilizing peat gasket material, animal manure, anaerobic active sludge and marsh gas, where the pH of the mixture is adjusted to 6.5-7.5. The obtained mixture is fermented at 28-50 degrees C for 7-40 days. The fermented product is added with auxiliary material and water and then fermented for 10-40 days to obtain desired product.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The method enables to prepare organic fertilizer in a cost-effective manner.
NOVELTY - Fermenting sludge involves dissolving surface active agent into sludge and then precipitating sludge particle. Sludge is fermented in anaerobic condition to obtain clear liquid and volatile fatty acid.    USE - Method for fermenting sludge (claimed).
NOVELTY - A photoelectrochemical hydrogen production device combined with primary cells and photoelectrochemical cells comprises anode, electrode, electrolyte, counter electrode, connecting wire, conductive substrate and semiconductor thin film.    USE - Photoelectrochemical hydrogen production device combined with primary cells and photoelectrochemical cells.
NOVELTY - Rapid dehydration and deodorization of sludge comprises uniformly mixing urban sewage treatment plant sludge with moisture content of 78-82% and dispersant ash at weight ratio of 10:6 for 3-5 hours; adding mixture with 0.05-0.09 wt.% heat- and alkali-resistant side strain solution and 0.03-0.06 wt.% Efficient Microbes (EM) bacteria liquid; uniformly mixing and fermenting mixture at normal temperature for 36-48 hours; and paving fermented mixture to dry naturally for 2 hours to complete process.    USE - Rapid dehydration and deodorization of sludge.    ADVANTAGE - The method has simple processing steps and operation, and has low production cost.
NOVELTY - Biomass baking comprises crushing the biomass raw material of maximum thickness of not greater than 5 mm and a length of not greater than 20 mm; drying and crushing biomass raw material, direct contacting the hot flue gas and biomass raw material, controlling dryer temperature at 150-180 degrees C, where the water content of the biomass raw material is less than 3%; baking biomass material in a reactor at 280-350 degrees C and 0.9-1 atm for 10-25 minutes and 0.9-1 atmospheric pressure; and baking the biomass at 60-80 degrees C.    USE - A biomass baking method.    ADVANTAGE - The method improves the yield and quality of baked biomass.
NOVELTY - An additive composition comprises 18-31 mass% 4-fluorobenzyl chloride, 15-29.5 mass% diethyl diselenide, 15-24.5 mass% phenylphosphonic acid, 13-24 mass% vanadate-tripropanolamine, 10-20.5 mass% boron trifluoride diethyl etherate, and 9-19.5 mass% 2-(tributylstannyl)furan.    USE - An additive composition used for improving nitrogen oxide emissions of methanol and gasoline mixture (M85) (claimed).    ADVANTAGE - The additive composition reduces nitrogen oxide emission by more than 30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the additive composition, comprising stirring 4-fluorobenzyl chloride, 2-(tributylstannyl)furan, and phenylphosphonic acid at room temperature; and sequentially adding diethyl diselenide, vanadate-tripropanolamine, and boron trifluoride diethyl etherate.
NOVELTY - A humic acid-based fertilizer comprises 60-80 wt.% carbon bio-organic fertilizer, 6-20 wt.% urea, 8-17 wt.% monoammonium phosphate, 3.5-5.5 wt.% potassium sulfate, and 0.005-0.015 wt.% trace element.    USE - A humic acid-based fertilizer used for rapeseed (claimed).    ADVANTAGE - The fertilizer provides necessary nutrients for rapeseed growth, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the carbon bio-organic fertilizer, comprising:    (A) clearing impurities from cattle and sheep manure, and crushing at 100-mesh sieve to obtain a moisture content of less than 50%;    (B) refining rapeseed oil to obtain a cake material, steaming, and crushing into 100 mesh powder;    (C) crushing fresh wheat straw to obtain powder;    (D) carrying out wheat straw powder fermentation by adding 0.05% urea and 0.01% sugar to the straw powder, and mixing at 20-40 degrees C fir 25-35 days;    (E) preparing fermentation agent comprising 30 kg of 100 mesh corn flour and 20 kg rapeseed oil cake powder, and mixing;    (F) mixing 10-30% cattle manure powder, 60-80% sheep manure powder, 3-7% fermented wheat straw powder, 3% of 100-mesh superphosphate, 1.5% urea, and 0.5% fermentation agents;    (G) carrying out natural fermentation to obtain a moisture content of 50-60%;    (H) carrying out aerobic fermentation at 55 degrees C for 10 days; and    (I) crushing carbon bio-organic fertilizer, to 100 mesh sieve, naturally drying to obtain a moisture content of 10-12%, and packaging.
NOVELTY - A mesh bag seedling container comprises 40-60 pts. wt. peat soil, 2-5 pts. wt. sawdust, 2-5 pts. wt. mushroom waste, 10-20 pts. wt. fermented rice husk, 10-20 pts. wt. carbonized rice hull, 2-5 pts. wt. corn cob, weight, 2-5 pts. wt. dogwood bark, 3-8 pts. wt. peanut skin, and 2-5 pts. wt. yellow soil.    USE - A mesh bag seedling container.    ADVANTAGE - The mesh bag seedling container is prepared using raw material sources that are wide and easy to obtain, and is inexpensive. The dogwood promotes plant growth and development. The seedling container is easy to prepare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the mesh bag seedling container, comprising:    (A) preparing fermented rice husk by mixing biological straw, rice hull, and water at a weight ratio of 1:400:80, uniformly mixing, fermenting for 30 days at 60 degrees C, and drying;    (B) drying corn cob, dogwood bark, and peanut peel until moisture content is 10-20%, and crushing by 40 sieve;    (C) mixing the fermented rice husk, the powder, peat soil, sawdust, mushroom waste, carbonized rice hull, and yellow soil, sieving, and drying; and    (D) adding 3-8 kg slow release fertilizer, uniformly mixing, and preparing a cylinder having a height of 10 cm and a diameter of 6 cm.
NOVELTY - An organic matrix comprises 900-1100 pts. wt. pine bark, 40-60 pts. wt. dry chicken manure, 10-20 pts. wt. urea, 1-2 pts. wt. lime, 2-3 pts. wt. rice bran, 1-2 pts. wt. brown sugar, 1-2 pts. wt. fermentation additive, 75-150 pts. wt. EM bacteria liquid, and 100-200 pts. wt. water.    USE - An organic matrix used for vegetable soilless cultivation.    ADVANTAGE - The organic matrix increases vegetable soilless cultivation to 5-15%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic matrix, comprising:    (A) naturally stacking 2 cm2 pine bark for 7-10 days;    (B) adding chicken manure and urea to the pine bark, regulating carbon nitrogen ratio to less than 40, adding lime, regulating pH value to 5-5.5, adding EM bacteria liquid and clean water, uniformly mixing, covering for 2-3 days to obtain a moisture content of 50 plus minus 5%;    (C) preparing incremental agents by fermenting fermentation additive, rice bran, and brown sugar;    (D) spreading the incremental agents in the bark mixture, piling, covering, standing for 6-12 hours, and carrying out reprocessing fermentation;    (E) carrying out first time fermentation for 25-30 days, strengthening heat preservation, moisturizing, promoting saccharification of fermentation, after 5-7 days, adjusting ferment temperature to 45-50 degrees C, fermentation time, surface, and entering a second fermentation when the accumulated temperature reached 800-900 degrees C;    (F) maintaining moisture content at 60%, and stopping fermentation when accumulated temperature reaches 800-1000 degrees C; and    (G) spreading fermentation product, drying to make water content reach 40 plus minus 5%, sieving, and packing.
NOVELTY - This utility new type provide the one aerobic composting a bucket, the bucket bottom of the bucket upper body side wall is provided with a vent hole, the bucket upper side wall air hole of upper part is provided with an annular bulge, bucket body is provided with hole of honeycomb cushion plate, a honeycomb pad plate is placed on said annular bump up. This utility new type of aerobic compost bucket, because oxygen in of decomposition, can make the microorganism organic matter is completely decomposed, the final product is organic fertilizer, water and carbon dioxide, compost has no odour, no greenhouse gas produce methane, up to a greater extent protect the environment, rhizome of rehmannia, relative closed compost, use aerobic composting compost bucket, the whole composting process is shortened by 1 months, and the bucket cover is screwed design, simple and easy operation, can be the kitchen is added.
NOVELTY - This utility new type claims a one a powdery or granular microorganism fertilizer of production system, which include mix device, granulating device, a sieving, wherein is provided with a storage device, the storage device before the granulation device set with the finished product exit and up and exit, exit connecting granulating device, granulating device and sieving device connect. This utility new type can be a powder microbial fertilizer, also can be a granular microbial fertilizer, a wide range, the process is simple, operation is convenient.
NOVELTY - This utility new type belongs to environmental protection device field, especially claims a high property one hydrogen internal combustion engine oil tail pneuma purifier, comprise shell, a gas tube, a water inlet, a electrode, electrode connecting bolt and electrolytic groove, gas tube and the throttle valve is connected with the water tank water inlet is connected with electrode connecting bolt and the automobile electric source is connecting, the inner shell is provided with a multi-mutually independently of electrolytic groove, each electrolytic groove are set with one air tube, a water inlet and electrode of said electrolytic groove and electrode are module, can be according to any combination of the internal combustion engine, upper gas tube is further set with pneuma water separator. This utility new type of electrolytic obtain beneficial effect of the hydrogen and oxygen gas of high purity, through entering into automobile air throttle in gasoline or diesel engine of combustion, hydrogen as a fuel and oxygen as combustion improver, which ensures the full combustion of fuel, increasing automobile power, at the same time reduces the automobile tail pneuma, it can save fuel oil 18-30 %.
NOVELTY - This utility new type claims a biomass granule one production system, aiming to provide one has simple structure, a low cost and a high product consistency and good property of biomass granule production system. A separating the biomass production system comprise in turn a set of raw material feeding device (1), through first conveying device (2) is connected with a raw material feeding device (1) of connecting with the discharging port of the raw material (3), through second conveying device (4) is connected with a raw material (3) of connecting with the discharging port of the spiral vibration device (5), through packing auger feeding device (6) and a spiral vibration device (5) of connecting with the discharging port of the biomass granule forming device (7), through third conveying device (8) and a biomass granule forming device (7) of discharge hole of connecting device (9). This utility new type can be widely applied to manufacturing field of biomass granule.
NOVELTY - A one aeration undercurrent wetland anti-clogging system, include wetland pool, fill of wetland filler in wetland material tank and a through hole is set on the tube screen of a wetland filling the bottom of the wetland tank is further set with a false bottom drain. This utility new type provide subsurface flow wetland aeration anti-clogging system of the following beneficial effects: This utility new type through the wetland tank bottom part is drainage false bottom, the wetland stuffing a time reverse washing, which not only can reduce the reverse washing resistance, at the same time, it can save energy consumption and reduce cost, through reverse washing of uplink form micro-bubble, filling a to make sediment of filling up a fall off and drain through the bottom into artificial wetland pool bottom part rear, valid from wetland stuffing block, the stuffing valid porosity, at the same time, this utility new type has simple structure, low cost and convenient maintenance and management.
NOVELTY - This utility new type provide the one using a shale porcelain granule is aritificial wetland substrate filling of the matrix top to bottom of shale porcelain granule of different particle size. Using shale porcelain granule of 3-5 mm grain diameter in the lower layer of vegetation, surface micro-pore has compact structure, large specific surface area and so on, which is good for better fixing of rhizosphere microorganism. The utility model is new in type, shale pore distribute uniformity, penetrating ability is strong, the entering into the wetland system of water and matrix of sufficient contact surface, improves the sewage purification ability of substrate, the blocking of wetland, prolongs the use life of wetland.
NOVELTY - This utility new type relates to one a mud turner, comprise machine frame, the upper part of rack set with operating room, the left and right two rack lower part between the side set with walking device, the walking device set with turning device, the left and right two side rack set with two set for a lifting turning device of transmission device, upper rack is further equipped with a driving device, upper rack part set with liquid tank and liquid pump, liquid pump connecting liquid tank, turning device rack above the outer side is installed with a spraying device, the spraying device connecting the liquid pump. This utility new type is installed with a spraying device on the upper rack of machine, spraying in the process of turning can be valid to avoid the dust flying everywhere to pollute the environment and personal safety, adding deodorant in the liquid can reduce valid compost in produce process of odour.
NOVELTY - This utility new type claims a one flue gas in hot recycling type biomass carbonizing furnace, carbonizing furnace comprise, further comprise of combustion chamber is set in the carbonizing furnace combustion room at the bottom of one secondary air inlet passage connected with the combustion room and connected filling channel, the bottom of the furnace body and the combustion room is coking carbonization room, combustion of the top room through the chimney with the carbonization furnace connected, a combustion chamber is set at the lower part with a cross flue gas recycling pipeline, the combustion room upper part is provided with a cross-shaped second air inlet pipeline, a combustion room outer wall connecting with a hot plate. This utility new type operation is simple, raw material has strong adaptability for the raw material is cheap, it can realize local carbonization local processing, reduce the transportation and processing cost of biomass raw material, for the environmental pollution is small, and it has good application prospect.
NOVELTY - One a mobile straw gasification furnace, comprise a furnace body, the top of the furnace body set with a feeding port, lower part of one side set with opening, the bottom set with idler wheel, a furnace body set with upper tapered hopper, upper cone upper port and a feeding port, upper tapered lower opening connecting a gas generating room, lower lower gas generating room is connected with oxidation room, room lower tapered hopper, a lower tapered hopper lower port set with rotary vane, rotary wind ring set with air store room. This utility new type is reasonable in design, simple in structure, convenient to move, by using biomass through sealed, using the sliding hot solution and hot chemical oxidation rear produce gas, the fuel cost is low, the hot utilization rate high, little pollution to the environment.
NOVELTY - This new type utility claims one three double-structure of a biomass gasification furnace, comprise a furnace body, upper clapboard, lower clapboard, upper furnace bridge, furnace bridge, lower pneuma upper room and lower room pneuma, upper combustion chamber, a lower combustion chamber, a dust depositing chamber, air tube, an air tube, a stirring rod, a spiral feeding tube, an ignition port and tube vents. Double pneuma room is a set on the two sub pneuma room furnace body upper part and lower part of. The wind is composed the pneuma and jet nozzle spray room of upper part by the air flow of upper to lower of vertical direction and several branch injection nozzle around the center gas-guide tube of upper lower layer number and is installed around of injection of the radial air flow. Double-furnace bridge is set in the hearth of double-layer furnace bridge can make the whole hearth form module of three-level. Through said three double-structure of the biomass gasification gas convert the lifting efficiency of low, it has simpler structure, so that the production cost of the biomass gas furnace, property.
NOVELTY - A biomass gasification furnace one furnace bottom structure, comprise of gasification furnace pedestal is set in the gasification furnace, a gasification furnace centre of the pedestal is provided with a slag storage chamber, a gasification furnace top part is provided with a porous sieve plate cover of said slag storage cavity, a gasification furnace outer wall is provided with a slag storage cavity of a slag discharging port, a gasification furnace outer wall is provided with an inclined extending to emergency slag discharging passage of the gasification furnace top part. This utility new type biomass fuel in the high temperature in the gasification process can realize the lower slag can be discharged successfully melted state slag low in an emergency even solid slag, an emergency discharging operation is convenient and reliable for the furnace body small damage, pneuma furnace by rotating along the line time is short, the gasification furnace to ensure long-term stable operation.
NOVELTY - A one plasma de-hydrogen high-efficient energy-saving boiler burner, which is composed of an intelligent controller, a high frequency high voltage power supply, a flame sensor, a plasma electric arc catalytic injector, the water evaporator, water pump, water valve, temperature sensor, an oil pump, an oil quantity adjusting valve, a lighter, an oil sprayer, a fan, an electromagnetic valve, a flame burner, burner shell and mounting flange. The water is heated to water vapour and then quickly decompose generating hydrogen in the plasma arc catalytic injector, oxygen molecule and hydrogen and oxygen ion, and fuel or fuel gas is sprayed to the boiler from fire burner, so as to increase the fuel or to replace part of the increasing oxygen, greatly saves fuel, energy-saving and emission reduction of index, it is desired in the industry of update upgrading of technology product.
NOVELTY - This utility new type belongs to the cryogenic technology field, specific relates to a synthetic ammonia one chemical tail pneuma of liquefied cryogenic rectification system. This utility new type include nitrogen circulation system and a compressor unit of main heat exchanger in the cold box, supercharged turbo-expander, rectifying tower and the methane rectifying tower, using the system using a different working condition operation, improved technical solution, it not only saves electricity, improves the production efficiency, but also can balance part of liquid nitrogen, as by-product is sold at a low price and high price stage stage.
NOVELTY - Gold/zinc oxide/cerium oxide oxidation catalyst, is claimed. The amount of gold in the catalyst is 3% of zinc oxide/cerium oxide. The atomic ratio of zinc and cerium in zinc oxide/cerium oxide composite oxide is 9/1.    USE - The catalyst is useful for low-temperature oxidation of carbon monoxide (claimed).    ADVANTAGE - The catalyst has high carbon monoxide oxidation activity at low temperature (claimed) and achieves complete conversion of carbon monoxide at 253K.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the gold/zinc oxide/cerium oxide oxidation catalyst, comprising respectively adjusting pH of gold chloride tetrahydrate solution and zinc oxide/cerium oxide composite oxide suspension to a specific value using sodium carbonate solution, high speed stirring and dropping gold chloride tetrahydrate solution into zinc oxide/cerium oxide composite oxide suspension at 343K, aging for 4 hours, washing using deionized water, filtering and drying at 353K for 24h hours, where the zinc oxide/cerium oxide composite oxide is carrier, the gold is active component, and the loading amount of gold chloride tetrahydrate solution (of specific concentration) is 3% of the zinc oxide/cerium oxide composite oxide; and    (2) low-temperature oxidation of carbon monoxide using the gold/zinc oxide/cerium oxide oxidation catalyst, where the low temperature reaction is carried out in U-shaped reactor immersed in liquid nitrogen container, the reaction temperature is controlled by adjusting the distance between the catalyst and the liquid nitrogen, the reactor exit gas is online analyzed using HP-6890 type gas chromatography, a flame ionization detector is installed in front of a nickel converter, carbon monoxide and carbon dioxide are quantitatively converted to methane in a hydrogen atmosphere, and the method utilizes micro normal pressure fixed bed quartz tube reactor.
NOVELTY - Chemical synthesis of 3,5-diiodosalicylic acid, comprises dissolving salicylic acid, iodide of (I), ferrate of (II) in polar solvent, adding protonic acid of (III), stirring and heating, and reacting to obtain 3,5-diiodosalicylic acid, where the reaction temperature is 20-150 degrees C, the reaction time is 20 hours. where the ratio of reaction material of salicylic acid, iodide, ferrate, and proton acid is 1:1-4:1-3:2-15, the polar solvent dosage is 25 times of raw material salicylic acid.    USE - The method is useful for chemical synthesis of 3,5-diiodosalicylic acid (claimed).    ADVANTAGE - The method has high conversion rate, synthesizes product with good purity, is economical, has simple processing technique, and is environmentally friendly.    DETAILED DESCRIPTION - Chemical synthesis of 3,5-diiodosalicylic acid, comprises dissolving salicylic acid, iodide of formula MIm (I), ferrate of formula NnFeO4 (II) in polar solvent, adding protonic acid of formula HxA (III), stirring and heating, and reacting to obtain 3,5-diiodosalicylic acid, where the reaction temperature is 20-150 degrees C, the reaction time is 20 hours. The ratio of reaction material of salicylic acid, iodide, ferrate, and proton acid is 1:1-4:1-3:2-15, the polar solvent dosage is 25 times of raw material salicylic acid.    M = H, Cl, Br, I, NH4, Li, Na, K, Ca, Ni, Cu, Zn, Ge, Y, Pd, Ag, Cd, Sn(IV), Cs, Pb, or Bi;    m = 1, 2, 3, or 4;    N = Li, Na, K, Ca, Ni, Sr, or Ba;    n = 1 or 2;    A = Cl, SO4, PO4, or HCOO-, CH3COO-, CH3CH2COO-, HOOCCOO-, CF3COO-, CF3SO3, PhCOO-, or TsO; and    x = 1, 2, or 3.
NOVELTY - Synthesizing agmatine sulfate comprises taking 1,4-butanediamine as raw material, cyanamide aqueous solution as guanidine reagent, carrying out addition reaction to obtain agmatine, then salifying using sulfuric acid.    USE - The method is useful for synthesizing agmatine sulfate (claimed).    ADVANTAGE - The method has mild reaction condition, is easy to control, causes less pollution, thus environmentally friendly, is economical, and suitable for industrial large-scale production.
NOVELTY - Preparing natural high purity (2 alpha ,3 beta )2,3-dihydroxy-olean-12-en-28-oic acid comprises drying Myrtaceae plant Eugenia caryophyllata Thunb clove buds.    USE - The method is useful for preparing natural high purity (2 alpha ,3 beta )2,3-dihydroxy-olean-12-en-28-oic acid (claimed).    ADVANTAGE - The method uses rich, cheap and easy to obtain raw material sources, has simple extracting, separating and purifying technique, is economical and environmentally-friendly, produces high yield, and repeatedly reuses organic solvent.
NOVELTY - Making fatty acid methyl ester (FAME) immiscible with oil, involves making the oil much more polar than the FAME using (i) polyethylene glycol (PEG) or similar polyether oil, (ii) a polar oil (as used in the cosmetics industry) or (iii) an ionic liquid.    USE - The method is useful for making FAME (i.e. biodiesel) immiscible with oil.    ADVANTAGE - The method is capable of efficiently making FAME immiscible with oil, thus preventing dilution of the lubricant and a subsequent loss in oil viscosity, reducing a detrimental effect in a number of engine performance areas, oxidation control, cold flow properties, wear-control, sludge deposit control and component interaction, and cutting down costs for the consumer or fleet operator.
NOVELTY - A Streptomyces tenebrarius 318 ( Delta aprK+ Delta tobZ) (GMCC 8285) capable of producing tobramycin, is new.    USE - The S. tenebrarius 318 is useful for producing tobramycin (claimed).    ADVANTAGE - The S. tenebrarius 318 is used for simple, low cost, environment-friendly and practical tobramycin production with improved quality and high yield.
NOVELTY - An additive is prepared by mixing 75-90 pts. wt. corncob, 150-180 pts. wt. straw e.g. corn, Sorghum or rice, 30-50 pts. wt. sawdust, 85-95 pts. wt. rice hull, 80-110 pts. wt. fresh vegetable leaf, 105-135 pts. wt. gelatine, 35-55 pts. wt. maltogenic amylase, 3-8 pts. wt. xylose, 5-10 pts. wt. cellulase and 2-7 pts. wt. protease, and grinding to obtain powder with less than or equal to 5 cm particle diameter.    USE - Preparation of additive for biofuel (claimed).    ADVANTAGE - The preparation method is fast, environment-friendly, consumes small amount of energy, and does not generate methane.
NOVELTY - A synthesis gas is prepared by feeding hydrogen gas (H2), carbon monoxide (CO), carbon dioxide (CO2) and water in high temperature methanation reactor comprising greater than or equal to 2 n stages with greater than or equal to 2 m catalyst bed layers in every stage to produce outlet stream which is fed to 1st section of catalyst bed layer of another reactor, feeding effluent stream Vn produced from final stage of reactor, converting to outflow stream Vn', compressing, recycling, and feeding back to 1st stage of reactor.    USE - Preparation of synthesis gas for natural gas alternative (claimed).    ADVANTAGE - The method consumes less energy and has controllable conditions, and synthesis gas has good quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of synthesis for natural gas alternative using double high temperature methanation reactor comprising catalyst bed layers.    Raw gases (1)    High temperature methanation reactor feed synthesis gas (2)    Double high temperature methanation reactor feed synthesis gas (3)    High temperature methanation catalyst bed layer feed gas (4)    High temperature methanation catalyst bed layer secondary feed gas (5)
NOVELTY - A synthesis gas is prepared by feeding hydrogen gas (H2), carbon monoxide (CO), carbon dioxide (CO2) and water in high temperature methanation reactor comprising greater than or equal to 2 n stages to produce outlet stream which is fed to another reactor, feeding effluent stream Vn produced from final stage of reactor, converting to outflow stream Vn', compressing, recycling, and feeding back to 1st stage of reactor.    USE - Preparation of synthesis gas for natural gas alternative (claimed).    ADVANTAGE - The method consumes less energy and has high conversion and recycling rates, and gas has good quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of synthesis for natural gas alternative using double high temperature methanation reactor.    Raw gases (1)    High temperature methanation reactor feed synthesis gas (2)    Double high temperature methanation reactor feed synthesis gas (3)    High temperature methanation reactor feed mixture (4)    High temperature methanation reactor feed gas (5)
NOVELTY - This utility new type claims a solar auxiliary heating one aerobic compost system, include the aerobic compost cabin body, said aerobic compost cabin body is set with a feeding port and a discharging port, said feeding port is connected with one feeding machine is connected, said aerobic compost cabin body futher set with one water inlet and one cabin water outlet cabin, wherein the solar auxiliary heating aerobic compost system futher comprise one solar cabin outlet is connected with a solar heat collecting plate of hot water inlet are connected, a cabin body inlet of the water inlet and the water outlet of the solar heat-collecting hot plate connected. This utility new type through using solar energy heat collecting plate for aerobic compost process auxiliary heating cabin body, which can greatly shorten the life garbage aerobic compost of time period, and through accurate control ventilation quantity, the compost process is more reasonable and more efficient. Using solar energy and shorten the aerobic compost of period, energy-saving and environment-friendly, fertilizer mass of aerobic compost is produced. At the same time, the whole system device operation is simple, safety and reliable and practical.
NOVELTY - Fertilizer contains 20-30 pts. wt. biogas residue, 10-12 pts. wt. bean residue, 2-9 pts. wt. bone powder, 3-6 pts. wt. nitro-humic acid, 5-9 pts. wt. potassium chloride, 0.002-0.003 pts. wt. nitrogen-fixing bacterial powder, 0.001-0.002 pts. wt. potassium bacteria powder, 3-6 pts. wt. powdered rock phosphate, 2-6 pts. wt. potassium mineral powder, 15-20 pts. wt. cotton straw powder, 3-9 pts. wt. boric acid, 2-6 pts. wt. ammonium citrate, 3-7 pts. wt. magnesium sulfate, 2-6 pts. wt. manganese sulfate, 1-4 pts. wt. zinc sulfate, and 15-20 pts. wt. urea.    USE - The fertilizer is useful for cultivating tea (claimed).    ADVANTAGE - The fertilizer satisfies the growth requirement of tea, suitable for tea growth, administered before winter, and increase yield and quality of the tea.    DETAILED DESCRIPTION - Fertilizer comprises 20-30 pts. wt. biogas residue, 10-12 pts. wt. bean residue, 2-9 pts. wt. bone powder, 3-6 pts. wt. nitro-humic acid, 5-9 pts. wt. potassium chloride, 0.002-0.003 pts. wt. nitrogen-fixing bacterial powder, 0.001-0.002 pts. wt. phosphorus bacterial powder, 0.001-0.002 pts. wt. potassium bacteria powder, 3-6 pts. wt. powdered rock phosphate, 2-6 pts. wt. potassium mineral powder, 15-20 pts. wt. cotton straw powder, 3-9 pts. wt. boric acid, 2-6 pts. wt. ammonium citrate, 3-7 pts. wt. magnesium sulfate, 2-6 pts. wt. manganese sulfate, 1-4 pts. wt. zinc sulfate, and 15-20 pts. wt. urea.
NOVELTY - Organic fertilizer comprises biogas residue, bean dregs, bone powder, nitrate base humic acid, potassium chloride, nitrogen-fixing bacteria powder, phosphorus bacteria, potassium bacteria powder, powdered rock phosphate, shell powder, vine green straw pole powder, clam shell powder, Cunninghamia lanceolata, Platycladus orientalis sawdust and actinomycetes powder.    USE - The organic fertilizer is useful for planting tea leaf (claimed).    ADVANTAGE - The organic fertilizer has strong specificity.    DETAILED DESCRIPTION - Organic fertilizer comprises 20-30 pts. wt. of biogas residue, 10-12 pts. wt. of bean dregs, 2-9 pts. wt. of bone powder, 3-6 pts. wt. of nitrate base humic acid, 5-9 pts. wt. of potassium chloride, 0.002-0.003 pts. wt. of nitrogen-fixing bacteria powder, 0.001-0.002 pts. wt. of phosphorus bacteria, 0.001-0.002 pts. wt. of potassium bacteria powder, 3-6 pts. wt. of powdered rock phosphate, 11-20 pts. wt. of shell powder, 15-20 pts. wt. of vine green straw pole powder, 15-20 pts. wt. of clam shell powder, 5-9 pts. wt. of Cunninghamia lanceolata, 5-9 pts. wt. of Platycladus orientalis sawdust and 0.001-0.002 pts. wt. of actinomycetes powder.
NOVELTY - Use method of dead branches and fallen leaves comprises converting dead branches and fallen leaves into a product by direct-combustion or briquetting, carrying out steam explosion-hot pressing, carrying out solid state fermentation to prepare into a fertilizer, classifying into multiple products including hydrolysis and extraction for cogeneration of cellulose monosaccharide and lignin product, carrying out steam explosion, washing, cellulase enzymolysis extraction, carrying out steam explosion, washing with water, extracting for cogeneration of hemicellulose, cellulose and lignin products.    USE - The dead branches and fallen leaves are useful in preparing fertilizer and in cogeneration of hemicellulose, cellulose and lignin products. The hemicellulose monosaccharide and cellulose monosaccharide are useful in fermentative preparation of small organic molecules including biogas, ethanol or butanol (all claimed).    ADVANTAGE - The method ensures conversion of dry branches and fallen leaves biologically, chemically and physically with high-efficiency to produce different products based on the requirement.    DETAILED DESCRIPTION - Use method of dead branches and fallen leaves comprises converting dead branches and fallen leaves into a product by carrying out direct-combustion or briquetting to prepare into a solid fuel to carry out combustion to generate power, carrying out steam explosion-hot pressing to prepare into plate, carrying out solid state fermentation to prepare into a fertilizer, classifying into multiple products including hydrolysis and extraction for cogeneration of cellulose monosaccharide and lignin product, carrying out steam explosion, washing, cellulase enzymolysis extraction, extraction for cogeneration of hemicellulose monosaccharide, cellulose monosaccharide, and lignin product, carrying out steam explosion, washing with water, extracting for cogeneration of hemicellulose, cellulose and lignin products.
NOVELTY - Preparation of ortho-aminophenol by using continuous catalytic hydrogenation technique involves continuous catalytic hydrogenation of ortho-nitro phenol in presence of palladium supported alumina catalyst in the fixed bed reactor, separating and purifying to obtain ortho-aminophenol.    USE - For preparation of ortho-aminophenol (claimed).    ADVANTAGE - The process is short, has high degree of automation, has low device investment, provides high yield of ortho-aminophenol i.e. up to 97% with high purity i.e. greater than 99%; has no material discharge; has good economic and social benefit; and not only reduces the labor strength, but also makes the whole scene environment clean.
NOVELTY - This utility new type one a preprocessing plant oil deodorized distillate ultrasonic reinforced extraction device VE, referring to natural VE extraction technology field. By ester exchange reaction groove, an ultrasonic reactor, crystallization reaction groove and distilling device in series through optimizing a process parameter of external circulating ultrasonic pre-processing rape seed deodorizing distillate, include frequency, time and pump flow rate and so on, strengthening ester exchange biological diesel and sterol crystal process, VE extraction time is shortened, the preparation efficiency is improved by more than 15%, and the VE, sterol and bio-diesel of continuous production.
NOVELTY - A biomass solid fuel is obtained by steam blasting and molding biomass into biomass blocks and heating the blocks at 150-400 degrees C, and has fuel ratio of 0.2-2.5, moisture-free maximum heating value of 5000-7500 kcal/kg, molar ratio of oxygen and carbon of 0.1-0.6 and molar ratio of hydrogen and carbon of 0.5-1.35.    USE - Biomass solid fuel e.g. wood-type and herbs.    ADVANTAGE - The biomass solid fuel has excellent handleability, reduced chemical oxygen demand of waste water during storage, and is obtained with reduced powdering.
NOVELTY - Carbonizing cellulosic materials comprises: (a) granulizing the cellulosic material; (b) heating the cellulosic material to above the steam point; and (c) combining the heated cellulosic material with heated liquid acid solution in a weight ratio of at least 0.5:1 liquid acid to cellulosic material to create a mixture at a temperature above a steam point to strip hydroxyl groups from the cellulosic material in a catalytic reaction with the heated acid and to outgas resulting water as steam to produce a low water content char.    USE - The method is useful for carbonizing cellulosic material (claimed) for the production of char, e.g. activated carbon.    ADVANTAGE - The method rapidly converts the cellulosic materials to high carbon content char in an open atmosphere with reduced tar formation in a cost-effective manner.
NOVELTY - Producing a composition comprising ammonia and/or ammonium from a bioreactor wastewater stream, comprises (a) providing an acid-treated wastewater steam from a bioreactor to an evaporation system, where the acid-treated bioreactor wastewater stream comprises ammonia and/or ammonium at a first concentration, a portion of the acid-treated bioreactor wastewater stream is vaporized to form a bottoms liquid comprising a dewatered, more concentrated solution of the ammonia and/or ammonium; and (b) collecting the bottoms liquid.    USE - The method is useful for producing a composition comprising ammonia and/or ammonium from a bioreactor wastewater stream (claimed), where the composition is useful as a fertilizer product to improve crop yield, and the bioreactor is an anaerobic digester. No biological data given.    ADVANTAGE - The method is capable of simply and economically producing the composition with improved fertilizer performance and reduced energy consumption, and reduces the total nitrogen discharge of the wastewater treatment plant. The composition can be used as the fertilizer product without substantial further processing.    DETAILED DESCRIPTION - Producing a composition comprising ammonia and/or ammonium from a bioreactor wastewater stream, comprising (a) providing an acid-treated wastewater steam from a bioreactor to an evaporation system, where the acid-treated bioreactor wastewater stream comprises ammonia and/or ammonium at a first concentration, a portion of the acid-treated bioreactor wastewater stream is vaporized to form a bottoms liquid comprising a dewatered, more concentrated solution of the ammonia and/or ammonium, and the bottoms liquid has a second concentration of ammonia and/or ammonium which is greater than the first concentration; and (b) collecting the bottoms liquid.
NOVELTY - Improving the reduction of carbon footprint of biofuel produced in a biomass (2)-to-liquid (BtL) plant comprises employing a syngas purification apparatus of the BtL process in a carbon capture and storage (CCS) process.    USE - The method is useful for improving the reduction of carbon footprint of biofuel produced in a BtL plant (claimed).    ADVANTAGE - The method economically reduces the carbon footprint of biofuel produced in the BtL plant using the CCS process with high efficiency and reduced energy consumption thus improving the purity of the biofuel in an eco-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) use of the BTL plant for improving the reduction efficiency of carbon footprint of fuel produced in the plant by virtue of utilizing in a CCS process apparatus intended for purification of the syngas in the BtL process; and    (2) an apparatus for improving the reduction efficiency of carbon footprint of fuel produced in the BtL plant, where the apparatus intended for purification of the syngas produced in the BtL process is integrated with the CCS process.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for improving the reduction of carbon footprint of biofuel produced in a BtL plant.    Biomass (2)    Carbon dioxide flows (20, 21, 22)    Exhaust gas (23)    Non-liquefying fractions (26)    Thermal energy. (29)
NOVELTY - A biodiesel emulsion comprises 40-70 pts. wt. biodiesel, 1-6 pts. wt. emulsifier and 20-50 pts. wt. water.    USE - Biodiesel emulsion used as diesel substitute.    ADVANTAGE - The environment-friendly biodiesel emulsion has natural raw materials.
NOVELTY - A hydrodeoxygenation catalyst comprises 10 %mass acetic acid solution pre-treated silicoaluminopihosphate molecular sieve (SAPO-11), zeolite (ZSM-5), and ( gamma )-aluminum oxide as carrier, 0.1-5 %mass zinc as auxiliary agent, and 0.1-35 %mass nickel, dinickel phosphide, iron, palladium, platinum and molybdenum phosphide as activity component.    USE - Hydrodeoxygenation catalyst is used for preparing castor oil biodiesel.    ADVANTAGE - The hydrodeoxygenation catalyst having high activity and selectivity with respect to castor oil is manufactured by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of hydrodeoxygenation catalyst.
NOVELTY - The apparatus (10) has an electrolysis chamber (110) to generate gas, and electrolyte tank (120) that defines a reservoir of electrolyte to supply electrolyte to electrolysis chamber. A gas collection chamber collects a gas generated by electrolysis chamber. The gas generated in electrolysis chamber is to pass through reservoir of electrolyte in electrolyte tank before entering gas collection chamber. Electrolyte permeable gas bubble baffle arrangement is provided in reservoir against movement of bubbles of gas generated in electrolysis chamber back into electrolysis chamber.    USE - Gas generating apparatus e.g. electrolysis gas generating apparatus (claimed) for generating useful gases such as hydrogen for use in internal combustion engine mounted in automotive, ships or other vehicles, and/or oxygen used for medical applications or for providing breathing air inside vehicles or buildings.    ADVANTAGE - The gas baffle blocking arrangement facilitates a more effective, or even maximized, use of the volume of the rigid housing as an electrolyte reservoir. The gas collection chambers are integrally formed with the electrolyte tank as a single unit such that a single housing can define both electrolyte reservoir and gas collection chambers, and thus such integration is advantageous in providing more compact gas generating apparatus while at the same time the electrolyte contained inside the electrolyte reservoir can serve as a fire isolator or fire separator for enhanced safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of the gas generating apparatus.    Gas generating apparatus (10)    Electrolysis chamber (110)    Gas delivery pipe (112)    Electrolyte tank (120)    Rigid housing (150)
NOVELTY - Biodiesel production involves performing chemical reaction between wet biomass of microalgae and water vapor for generating products, such as crude glycerin and fatty acids. The humid biomass of microalgae is added into a heat exchange device through a supply line. The humid biomass of microalgae is heated in heat exchange equipment by introducing steam through a steam line. The heated wet biomass of microalgae is introduced into a hydrolysis column through supply line from the heat exchange device.    USE - Method for producing biodiesel from wet biomass of microalgae for use as biofuel in compression ignition.    ADVANTAGE - The method enables producing biodiesel at industrial level in a simple and easy manner.    DETAILED DESCRIPTION - Biodiesel production involves performing chemical reaction between wet biomass of microalgae and water vapor for generating products, such as crude glycerin and fatty acids. The humid biomass of microalgae is added into a heat exchange device through a supply line. The humid biomass of microalgae is heated in heat exchange equipment by introducing steam through a steam line. The heated wet biomass of microalgae is introduced into a hydrolysis column through supply line from the heat exchange device. Steam is introduced to the top of hydrolysis column, where hydrolysis reaction is performed for resulting crude glycerin and fatty acid. The fatty acid is removed from top of the hydrolysis column through a product line. The crude glycerin is removed from hydrolysis column by using another product line. The crude glycerin is entered into a separator for separate water. The biodiesel is removed from bottom of the esterification column through a line of products.
NOVELTY - Method for decoloring dyeing wastewater colored by azo dye by activated sludge method, involves adsorbing the azo dye by adsorption agent, collecting the adsorption agent after the adsorption process, performing first decoloring process by an activated sludge method using an aerator, and performing second decoloring process under facultative anaerobic condition using azo reductase secreting azo dye decomposition microorganism with respect to the dye adsorption-completed adsorption agent.    USE - The method is useful for decoloring dyeing wastewater colored by azo dye (claimed).    ADVANTAGE - The method is cost-effective, simple, rapid and requires less time.
NOVELTY - Plant is operated by supplying composite fuel containing mixture of biomass and treated sewage sludge to entrained bed gasification furnace which manufactures gasification gas used as fuel by internal combustion engine to obtain motive power.    USE - Method of operating plant (claimed).    ADVANTAGE - Plant operating costs can be reduced, and electric power generation can be efficiently performed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of composite fuel; and    (2) plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the step which calculates blend ratio of composite fuel. (Drawing includes non-English language text).    Step of inputting calculated amount of biomass and treated sludge into computer (S1)    Step of setting blend ratio of biomass and treated sludge (S2)    Step of calculating melting point of ash in composite fuel (S3)    Step of calculating combustor temperature (S4)    Step of calculating emitted heat amount of gasification gas (S5)
NOVELTY - A saccharide from lignocellulosic biomass is manufactured by preparing reaction mixture containing lignocellulosic biomass feedstock, enzyme and water, and starting saccharification reaction, adding lignocellulosic biomass feedstock and water to reaction mixture and restarting saccharification reaction after collecting a part of saccharified liquid from reaction mixture during saccharification reaction advancing, advancing saccharification reaction, collecting saccharified liquid from reaction mixture, and completing saccharification reaction.    USE - Manufacture of saccharide from lignocellulosic biomass (claimed).    ADVANTAGE - Enzyme cost is reduced and productivity is improved.
NOVELTY - The device comprises a bulk material container (21) that comprises a conveyor tube (3) which is provided on a discharge opening and a lateral supply opening (12) of a gasification reactor (1). A mechanical conveying apparatus (4) is arranged in the conveyor tube. The conveying apparatus comprises a hydraulically driven plunger (10) which is displaceably guided in the conveying direction of one cylindrical axial portion (19) of the conveying tube, and a compression cone (11) in the conveying direction of other axial portion (20) of the conveying tube for continuously decreasing the fuel.    USE - Device for conveying biogenic fuels into gasification reactor (claimed).    ADVANTAGE - The maintenance costs are reduced and a uniform dosage is allowed.The good mixing is ensured in the fluidized bed, and pulsations in the gasification chamber are avoided.The fuel is conveyed to the feed at a constant speed continuously.The return of the plunger is carried out at a fast speed and a next feed cycle is reached without much interruption. The installation and removal of the conveyor tube is facilitated.The fitting is expandable in the radial direction of the conveyor tube. The overall length of the plunger or the displacement drive of the piston forming the hydraulic cylinder is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gasification reactor.    Gasification reactor (1)    Conveyor tube (3)    Mechanical conveying apparatus (4)    Plunger (10)    Compression cone (11)    Supply opening (12)    Axial portion (19,20)    Bulk material container (21)
NOVELTY - A nickel-type methane reformation catalyst of gas-permeable sheet form or plate shape is arranged in the latter stage of a gasifier or methane reformation installation gasifier and heated to 900 degrees C or more. Methane in the gas which gasifies solid substances such as biomass and coal with a gasifying agent, is reacted with the catalyst in presence of water vapor and modified.    USE - Methane reformation method (claimed).    ADVANTAGE - The reformation of hydrocarbons such as methane is carried out stably at more than 900 degrees C or more for a long time by installing the nickel-type methane modification catalyst. The steam reformation effect is improved by improving the nickel and gas contact by using the nickel mesh catalyst. The use of roll-shaped catalyst, the occlusion by solid residue byproduced at the time of gasification is prevented and the gasification can be carried out stably by enabling smooth flow of the gas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) methane reformation catalyst; and    (2) gasifier, which consists of the nickel-type methane reformation catalyst.
NOVELTY - The apparatus (100) has a modifier (1) that generates hydrogen-containing-gas using raw material. Hydrodesulfurization device (2) removes sulfur compound in raw material. Recycle flow path (3) supplies hydrogen-containing-gas to desulfurization device. Drainage channel (4A) discharges water condensed in condenser (4). Thermal-medium flow path (5) passes thermal medium for collecting heat of condenser. Sending device (6) pours medium. Controller (7) operates sending device while hydrogen-containing-gas is not flowed through to recycle flow path, when starting and stop.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The quantity of water vapor condensed from recycle gas can be reduced without condensed with condenser. The flow-path obstruction by downstream gas flow path can be suppressed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Hydrodesulfurization device (2)    Recycle flow path (3)    Condenser (4)    Drainage channel (4A)    Thermal-medium flow path (5)    Sending device (6)    Controller (7)
NOVELTY - Providing hydrogen gas and syngas in separate streams involves: (a) heating a metal and/or metal salt with water to produce a metal oxide and hydrogen gas; (b) extracting the hydrogen gas; (c) heating the metal oxide with a biomass feedstock to produce a mixture comprising syngas and a metal vapor; and (d) hydrogenating the syn-gas to produce synthetic crude.    USE - The process is useful for providing hydrogen gas and syngas in separate streams (claimed).    ADVANTAGE - The advantage of the process is that the need for a further purification step to separate the stream is not required, making the process more cost effective and environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an assembly for providing hydrogen gas and syngas in separate streams, comprising a first reaction chamber for producing hydrogen gas; a first outlet for discharging the hydrogen gas; a second reaction chamber for producing syngas and metal vapor; a separating unit to separate the syngas from the metal vapor; and a second outlet for discharging the syngas; and    (2) a method which involves decomposing a metal salt at a relatively low temperature to form an acid, reacting the acid with a metal pair, and extracting resultant hydrogen gas.
NOVELTY - The unit (20) has water container (21) that contains hydrogen/oxygen separator defining oxygen chamber and hydrogen chamber, hydrogen outlet (22) connecting hydrogen chamber to internal combustion engine (50), and oxygen vent (23) venting oxygen chamber to atmosphere. Water electrolysis conductor (24) is placed in water container to electrolyze water in water container based on flow of current (I) through conductor such that electrolysis of water produce flow of hydrogen as positive catalyst through hydrogen outlet to engine and flow of oxygen through oxygen vent to atmosphere.    USE - Electrolysis unit for producing hydrogen as positive catalyst for internal combustion engine, used in hydronic catalyst device (claimed).    ADVANTAGE - The efficient operation of internal combustion engine is achieved, since the hydrogen is used as positive catalyst in electrolysis based system for combustion of fuel-air mixture within cylinder of internal combustion engine.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a hydronic catalyst device for producing hydrogen as positive catalyst for internal combustion engine; and    (2) a system for producing hydrogen as positive catalyst for internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydronic catalyst device.    Electrolysis unit (20)    Water container (21)    Hydrogen outlet (22)    Oxygen vent (23)    Water electrolysis conductor (24)    Internal combustion engine (50)    Current (I)
NOVELTY - The system has a hydroxygen-gas generation unit with electrolytic cell that electrolyzes water and generates hydroxygen gas. A mixer generates composite fuel which bubble-ized hydroxygen gas and mixed with liquid fuel. A circuit supplies composite fuel in mixing tank to mixer with circulation pump and returns fuel to mixing tank. A gas path supplies hydroxygen gas emitted in generation unit to mixer. A flow control valve arranged in gas path adjusts flow volume of gas in gas path. A gas meter displays flow volume value of gas in gas path.    USE - Fuel improvement system used in combustion apparatus such as boiler.    ADVANTAGE - The flow control valve adjusts flow volume of gas in gas path, and gas meter displays flow volume value of gas in gas path, so that the fluctuation of flow volume value of hydroxygen gas and mixing rate of the hydroxygen gas with respect to liquid fuel can be grasped easily and correctly and can be adjusted and consumption of fuel and electric power is reduced. The combustion efficiency can be improved and the generated hydroxygen gas is effectively utilizable.
NOVELTY - The apparatus (10) has a shift catalyst layer (33) which is arranged in one reaction flow path (S5) to pass fuel gas passed through a regeneration flow path (S4), and remove carbon monoxide from fuel gas. A methanation catalyst layer (34) is arranged in one reaction flow path to pass raw fuel gas passed through shift catalyst layer, and remove carbon monoxide from fuel gas by a methanation reaction. A hydrodesulfurization catalyst layer (35) is provided in a desulfurization flow path (S6) to desulfurize the raw fuel gas goes to an evaporation passage (S2).    USE - Hydrogen production apparatus of fuel cell system (claimed).    ADVANTAGE - Since the fuel gas cooled appropriately is supplied to the methanation catalyst layer, the accelerating temperature rise can be suppressed. The manufacturing cost and size of the hydrogen production apparatus can be reduced. The temperature of the methanation catalyst layer in radial direction can be made uniform, and the methanation reaction can be performed favorably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen production apparatus.    Hydrogen production apparatus (10)    Shift catalyst layer (33)    Methanation catalyst layer (34)    Hydrodesulfurization catalyst layer (35)    Evaporation passage (S2)    Reaction flow paths (S3,S5)    Regeneration flow path (S4)    Desulfurization flow path (S6)
NOVELTY - The residue discharging apparatus (10) has cylindrical casing (90) which is installed in inner side of saccharification reaction chamber (20). A residue discharge port (96) is formed in other edge portion of cylindrical casing to discharge the residue from cylindrical casing. A screw portion (98) is configured to move the residue in cylindrical casing and taken in from intake port (92) to residue discharge port. An axial portion (100) is provided with the inclination portion (102) for narrowing interval with internal peripheral surface of cylindrical casing.    USE - Residue discharging apparatus of biomass such as lignocellulosic biomass, sugarcane, maize, rice straw, stalk of plant and leaf, construction waste material, and coppiced timber, used in ethanol manufacturing system.    ADVANTAGE - The biomass residue and saccharification solution are separated into solid and liquid reliably, so that the saccharification efficiency of the residue discharging apparatus can be increased by simple and compact structure of residue discharging apparatus. The size of the residue discharging apparatus can be reduced. The cost of the apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the reaction apparatus.    Residue discharging apparatus (10)    Saccharification reaction chamber (20)    Cylindrical casing (90)    Intake port (92)    Residue discharge port (96)    Screw portion (98)    Axial portion (100)    Inclination portion (102)
NOVELTY - A photochemical reaction apparatus consists of a laminate comprising an oxidation catalyst layer (19) which oxidizes water to generate oxygen and protons, a reduction catalyst layer (20) which reduces carbon dioxide to generate a carbon compound, and a semiconductor layer which is formed between the oxidation catalyst layer and the reduction catalyst layer and which performs charge separation by means of light (AA) energy, and an ion transfer path for transferring ions between the oxidation catalyst layer side and the reduction catalyst layer side.    USE - Photochemical reaction apparatus is used for synthesizing cellulose and saccharide.    ADVANTAGE - The photochemical reaction apparatus has excellent photochemical reaction efficiency, and photoreduction efficiency of high-carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining operation of photochemical reaction apparatus. (Drawing includes non-English language text)    Substrate (11)    Solar cells (14,15,16)    Oxidation catalyst layer (19)    Reduction catalyst layer (20)    Light (AA)
NOVELTY - The organic acid generation apparatus comprises a tank, a food leachate supply unit to supply food leachate to the tank, a microorganism supply unit that supplies useful microorganism into tank to ferment the food leachate within the tank and to produce organic acid, an organic acid supply unit for supplying the organic acid within the tank to a bioreactor of a sewage treatment apparatus, and a control unit that controls the supply of the organic acid supply unit from the organic acid supply unit based on biochemical oxygen demand and chemical oxygen demand of the sewage.    USE - The organic acid generation apparatus is useful in a sewage treatment apparatus (claimed).    ADVANTAGE - The organic acid generation apparatus enhances the performance of the sewage treatment apparatus in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - The organic acid generation apparatus comprises a tank, a food leachate supply unit to supply food leachate to the tank, a microorganism supply unit that supplies useful microorganism into tank to ferment the food leachate within the tank and to produce organic acid, an organic acid supply unit for supplying the organic acid within the tank to a bioreactor of a sewage treatment apparatus, and a control unit that controls the supply of the organic acid supply unit from the organic acid supply unit based on biochemical oxygen demand and chemical oxygen demand of the sewage introduced into the sewage treatment apparatus. An INDEPENDENT CLAIM is included for a sewage treatment apparatus.
NOVELTY - Controlling (M1) unwanted bacteria in fermentation processes involves contacting reactants of the process with an effective amount of bacteriocin.    USE - For producing bacteriocin; and for controlling or reducing unwanted bacteria in fermentation processes (claimed), especially biofuel-bioethanol fermentation processes.    ADVANTAGE - The method effectively control or reduce unwanted bacteria. The bacteriocin produced and added to bacteria containing media for bacterial control or bacteriocin-producing bacteria, may be added under conditions promoting bacteriocin production with the efficacious bacteriocins being produced in-situ.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a process (M2) for control of unwanted bacteria in fermentation product process involving: identifying unwanted bacteria; locating and isolating bacteriocin virulent for some or all of the identified unwanted bacteria; contacting the unwanted bacteria with an effective amount and for an effective time to destroy an identifiable amount of some or all of the unwanted bacteria; and    (2) producing (M3) bacteriocin for use in reducing unwanted bacteria in fermentation processes involving producing bacteriocin with native expression systems in native bacterial host strains, including bacteriocin-producing LAB strains; producing bacteriocin with heterologous expression systems utilizing bacteria hosts selected from Escherichia coli, species of Lactococcus, Enterococcus, Lactobacillus and Pediococcus; utilizing bacteriocin-producing bacteriophage including bacteriophage into which generic bacteriocin determinants have been engineered; and utilizing bacteriocin-producing eukaryotic cells including yeast cells.
NOVELTY - Producing gas from sweet leaf of Chrysanthemum residue by anaerobic digestion, comprises preparing residue and adjusting the water content, preparing additives comprising alkyl glycoside and alkaline ammonium salt additives, adding residue and water to a mixing tank with stirring, adding alkaline ammonium salt to the slurry with stirring, adjusting the pH value, adding alkyl glycoside to the tank with stirring, and conveying the slurry to an anaerobic digestion tank.    USE - The method is useful for producing gas from sweet leaf of Chrysanthemum residue (claimed).    DETAILED DESCRIPTION - Producing gas from sweet leaf of Chrysanthemum residue by anaerobic digestion, comprises preparing residue and adjusting the water content to 65-75%, preparing additives comprising alkyl glycoside and alkaline ammonium salt additives, where purity of alkyl glycoside is greater than 98%, adding 50 pts. wt. of residue and 950 50 pts. wt. of water to a mixing tank with stirring, adding 1 pts. wt. of alkaline ammonium salt to the slurry with stirring, adjusting the pH value to 6.8-7.2, adding 0.01-0.05 pts. wt. of alkyl glycoside to the tank with stirring, and conveying the slurry to an anaerobic digestion tank, where the mass ratio of slag, alkyl glycoside, alkaline ammonium salt and water is 50:0.01:0.05:1:950.
NOVELTY - The device (300) has storage unit that is provided to send out electrolyte solution to hydrogen generation cell (310). An electrolyte solution supply tube (15) is provided with more than one branch to connect with electrolyte solution supply hole (10) of cell. A gas-liquid discharge pipe (19,21) is provided with more than one branch to connect with gas liquid discharge hole of cell. The flow volume of electrolyte solution is made same, by reducing flow path resistance of solution. The water is decomposed and hydrogen is generated by irradiating light to optical semiconductor electrode.    USE - Hydrogen generation device for use in energy system (claimed).    ADVANTAGE - Since the electrolyte solution supply hole exists in position higher than gas-liquid discharge hole, the electrolyte solution supply hole is kept inevitable in position always higher than electrolyte level. Thus the electrolyte solution in each cell can be isolated from the electrolyte solution in electrolyte solution service main and each electrolyte solution supply tube.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an energy system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of hydrogen generation device.    Electrolyte solution supply hole (10)    Electrolyte solution supply tube (15)    Gas-liquid discharge pipe (19,21)    Hydrogen generation device (300)    Hydrogen generation cell (310)
NOVELTY - Preparation of carbon adsorption straw decomposition agent involves decomposing isolated and identified strains; production decompose microbial inoculum; and verifying decomposition effect of agent.    USE - For preparation of carbon adsorption straw decomposition agent (claimed).    ADVANTAGE - The process is simple, has low device requirement, is low cost and large scale production, and effectively avoids the traditional straw processing method that causes environmental pollution.
NOVELTY - Processing 1,4-dioxane containing waste water, comprises (i) introducing 1,4-dioxane containing waste water into anaerobic reactor to process high concentration organic components and to remove organic matter under anaerobic condition; and (ii) introducing the anaerobically treated water into aerobic tank and removing remaining organic matter under aerobic conditions, where 1,4-dioxane and other high concentration organic components in the waste water are removed simultaneously and the step (i) utilizes expandable granular sludge layer (EGSB) or upflow anaerobic sludge blanket (UASB).    USE - The method is useful for processing 1,4-dioxane containing waste water (claimed).    ADVANTAGE - The method converts high concentration organic matter into bio-gas and methane sources for energy production; and can process waste water from chemical plant, petrochemical factory, electronics manufacturing plant, paint manufacturing plant, cosmetic raw material manufacturing plant and polyester fiber chemical plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for waste water treatment apparatus, comprising anaerobic reactor including expandable granular sludge layer (EGSB) or upflow anaerobic sludge blanket for storing waste water; a buffer tank, formed with treated water discharging unit at its upper part, waste water discharging unit at one side of lower part to supply waste water and sludge into the bottom of the anaerobic reactor and waste water inlet portion at the other side of lower part, where the anaerobically treated water and pH adjusting agent are added from the upper part of the anaerobic tank; and aerobic tank, which receives anaerobically treated water discharged from the buffer tank.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic process flow for processing waste water (Drawing includes non-English language text).    Anaerobic treatment step (S1)    Aerobic treatment step (S2)
NOVELTY - An electrode-supporting-type gas-separation membrane module has porous scaffold, gas separation membranes (22) formed in order to contact outer side of porous scaffold, interconnector (30) positioned between the gas separation membranes in order to contact with gas separation membrane, and porous electrode active layer (40) formed on outer side of gas separation membrane and porous scaffold.    USE - Electrode-supporting-type gas-separation membrane module e.g. tubular structure of electrode-supporting-type gas separation membrane module is used for reforming hydrocarbon e.g. methane gas (all claimed).    ADVANTAGE - The electrode-supporting-type gas-separation membrane module having excellent chemical and mechanical durability economically and selectively passes gas via electron exchange reaction due to coupling-material layer and gas exchange via ion-conducting separation layer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrocarbon reforming method;    (2) tubular structure of electrode-supporting-type gas separation membrane module; and    (3) manufacture of tubular structure of electrode-supporting-type gas separation membrane module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tubular structure of electrode-supporting-type gas separation membrane module.    Porosity conductive support (10)    Gas separation membrane (22)    Interconnector (30)    Porous electrode active layer (40)
NOVELTY - Producing biogas and/or methane involves providing a slurry comprising at least one solid spent cereal produce; and subjecting the slurry to an anaerobic digestion comprising methanogenisis at a pH of pH 6.6-7.6, to obtain a biogas and a liquid digestate.    USE - For producing biogas and/or methane (claimed).    ADVANTAGE - The process runs in a continuous or semi-continuous manner; allows high-bicarbonate alkalinity to be provided to the slurry; and also serves to bring the slurry to the desired pH.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic digestion system as given in Figure 2 of the specification.
NOVELTY - A mulch or potting soil composition comprises: (a) mulch or potting soil as component I; and (b) at least one microorganism, or a cell-free extract or at least one metabolite, and/or a mutant of the at least one microorganism having all the identifying characteristics of the respective microorganism or extract of the mutant, as component II.    USE - The mulch or potting soil composition is useful for enhancing plant growth, water use efficiency of the plant, plant appearance, or the population of beneficial microorganisms or the content of metabolites beneficial to plant health produced by the beneficial microorganisms in the mulch or soil around the plant (claimed).    ADVANTAGE - The composition can be efficiently used to conserve moisture, improve fertility and health of the soil, reduce weed growth, and enhance visual appeal of the area.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of making the composition, comprising: providing at least one microorganism in a dry powder spore preparation, a concentrated liquid form, or a formulated carrier; and mixing a mulch or a potting soil and the least one microorganism into the composition; and    (2) a method for enhancing plant growth, water use efficiency of the plant, plant appearance, or the population of beneficial microorganisms or the content of metabolites beneficial to plant health produced by the beneficial microorganisms in the mulch or soil around the plant, comprising: applying a layer of the mulch composition to soil in the vicinity of a plant or a in the vicinity of a location where a plant is to be grown.
NOVELTY - Substrate comprising organic carbon and biomass such as algae, is claimed. The substrate is obtained by processing the substrate at high temperature under hydrogen atmosphere (reducing) to separate and collect organic components comprising carbon, hydrogen, oxygen, and nitrogen, blown dispersing the organic components and biomass without adding catalysts, to decay and spontaneously collect the product, controlling the addition of external hydrogen, and cooling the reactive constituents such as carbon and hydrogen to form methane and other hydrocarbons.    USE - The substrate is useful in electrical energy devices for storing electrical energy from renewable energy sources such as wind and solar power in the form of methane.    DETAILED DESCRIPTION - Substrate comprising organic carbon and biomass such as algae, is claimed. The substrate is obtained by processing the substrate at high temperature under hydrogen atmosphere (reducing) to separate and collect organic components comprising carbon, hydrogen, oxygen, and nitrogen, blown dispersing the organic components and biomass without adding catalysts for decaying and spontaneously collecting the product with self-ignition temperatures in a collection tank in a hot zone, controlling the addition of external hydrogen, from electrolysis stream of e.g. Wind and solar electricity are provided, cooling the reactive constituents such as carbon and hydrogen to form methane and other hydrocarbons.
NOVELTY - Integrated type ethanol fermentation comprises (i) fermenting sugar to form ethanol and wet fermentation residue; (ii) producing fuel gas through conversion of fermentation residue; (iii) combusting fuel gas in an engine or a fuel turbine to produce electricity and heat or steam; and (iv) utilizing heat or steam in the step (i) and (ii) for providing energy.    USE - The method is useful for integrated type ethanol fermentation (claimed).
NOVELTY - A ethylene cracking raw material selective hydrogenation method involves using lanthanum ion modified molecular sieve desulfurizing agent, transferring raw material to fixed bed with hydrogenation catalyst to carry out hydrogenation reaction in presence of hydrogen and to convert unsaturated hydrocarbons to saturated hydrocarbons, followed by returning a part of hydrogenation reaction product as solvent to the fixed bed with hydrogenation catalyst by mixing with the raw material and desulfurizing agent through fixed bed to carry out desulfurization.    USE - Method for selective hydrogenation of ethylene cracking raw material.    DETAILED DESCRIPTION - A ethylene cracking raw material selective hydrogenation method involves using lanthanum ion (La3+) modified molecular sieve desulfurizing agent, transferring raw material to fixed bed with hydrogenation catalyst to carry out hydrogenation reaction in presence of hydrogen and to convert unsaturated hydrocarbons to saturated hydrocarbons, followed by returning a part of hydrogenation reaction product as solvent to the fixed bed with hydrogenation catalyst by mixing with the raw material and desulfurizing agent through fixed bed to carry out desulfurization by controlling volume liquid hourly space velocity of 3.0-16.0 hr-1, system pressure of 0.4-0.8 MPaG, feeding temperature at 5-60 degrees C, where the ratio of raw material and hydrogenation reaction product is 1:6-10, the lanthanum ion (La3+) modified molecular sieve desulfurizing agent has particle size of 3-6 mm and lanthanum molecular sieve content of 1.0-5.0 wt.%.
NOVELTY - An ethylene raw materialselective hydrogenation method involves subjecting ethylene raw material to hydrogenation in a fixed bed in presence of hydrogenation catalyst to convert unsaturated hydrocarbon into saturated hydrocarbon. The reaction product is mixed with a solvent in a ratio of 1: 6-10 followed by adding desulfurizing agent, carrying out desulfurization and processing resulting product through cerium ion (Ce3+) modified molecular sieve to achieve grain diameter of 3-6 mm.    USE - Method for selective hydrogenation of ethylene raw material.    DETAILED DESCRIPTION - An ethylene raw materialselective hydrogenation method involves subjecting ethylene raw material to hydrogenation in a fixed bed in presence of hydrogenation catalyst to convert unsaturated hydrocarbon into saturated hydrocarbon. The reaction product is mixed with a solvent in a ratio of 1: 6-10 followed by adding desulfurizing agent, carrying out desulfurization and processing resulting product through cerium ion (Ce3+) modified molecular sieve to achieve grain diameter of 3-6 mm, where the desulfurization process is carried out at a volume liquid hourly space velocity of 3-16 hr-1 under pressure of 0.4-0.8 MPaG at 5-60 degrees C and the molecular sieve comprises 1-5 wt.% cerium ion.
NOVELTY - Acidifying a marsh gas in a fermenting system to recover gas of liquid composite biological preparation, involves: preparing thermophilic acid methanogen, and oxidizing acetic acid bacteria nutrient and trace element, where the thermophilic acid producing methane is Methanobacterium espanolae, Methanobrevibacter acididurans, Methanoregula boonei and Methanosphaerula.    USE - For processing the organic waste such as crop straw, livestock and poultry cultivation waste, waste water and waste residue, household organic garbage, and sewage sludge.    ADVANTAGE - The marsh gas ferment system recover normal production. The acidification of marsh gas fermenting system quickly recover normal gas, does not need to add alkaline matter or large discharge of a large change, and has continuous stable production of marsh gas fermenting system.    DETAILED DESCRIPTION - Acidifying a marsh gas in a fermenting system to recover gas of liquid composite biological preparation, where the preparation contains thermophilic acid methanogen, acetic acid oxidizing bacteria nutrient and trace element, where the thermophilic acid producing methane is Methanobacterium espanolae, Methanobrevibacter acididurans, Methanoregula boonei and Methanosphaerula; where the cell number ratio of four bacteria is (0.5-2):(0.5-2):(2-4):(1-3), where nutrient acetic acid oxidizing bacteria is Tepidanaerobacter acetatoxydans, Syntrophaceticusschinkii and Clostridium ultunense, where cell number ratio of three bacteria is (1-3):(3-5):(2-4), and the trace element is cobalt (Co), nickel (Ni) and selenium (Se).
NOVELTY - Industrial sewage treatment agent comprises polyacrylamide, silicon dioxide, persulfate, sodium carbonate and composite microorganism, where the composite microorganism include 2 pts. wt. Bacillus licheniformis, 3 pts. wt. Pseudomonas aeruginosa, 2 pts. wt.Bacillus subtilis, 4 pts. wt. Candida lipolytica, 3 pts. wt. nitrifying bacteria and 2 pts. wt. denitrifying Paracoccus.    USE - As industrial sewage treatment agent (claimed).    ADVANTAGE - The industrial sewage processing agent can make the sewage suspended substance with biological oxygen demand (BOD) at rate of more than 99.8%, chemical oxygen demand (COD) at rate of more than 98.7%, and sludge amount of 98%, with no secondary pollution, with stable treatment effect and is environmental friendly.    DETAILED DESCRIPTION - Industrial sewage treatment agent comprises 10-15 pts. wt. polyacrylamide, 8-15 pts. wt. silicon dioxide, 3-5 pts. wt. persulfate, 2-3 pts. wt. sodium carbonate and 15-20 pts. wt. composite microorganism, where the composite microorganism include 2 pts. wt. Bacillus licheniformis, 3 pts. wt. Pseudomonas aeruginosa, 2 pts. wt.Bacillus subtilis, 4 pts. wt. Candida lipolytica, 3 pts. wt. nitrifying bacteria and 2 pts. wt. denitrifying Paracoccus. An INDEPENDENT CLAIM is included for preparation of the composite microorganism involving: strain activating and expanding culture; inoculating rear strain amplification culture to a volume percentage 1-5 % inoculating mixed strain culture medium in mixed culture temperature of 28 degrees C, time of 36 hours to obtain composite bacteria solution; and drying the composite bacterial liquid through drying obtain composite microorganism.
NOVELTY - Preparation of memantine hydrochloride, involves: reaction of 1-bromo-3,5-dimethyl adamantine and urea at 25-200 degrees C in organic solvent for 2-48 hours; completely evaporating solvent, where the dimethyl adamantine and urea mol ratio is 1:1-8; (2) adding sodium hydroxide to step (1) residue, at 50-200 degrees C in lower alcohol solution, and then concentrating and extracting hydrochloric acid to form salt to obtain the memantine hydrochloride crude product; and (3) obtaining from step (2) memantine hydrochloride crude product, memantine hydrochloride.    USE - For preparation of memantine hydrochloride (claimed).    ADVANTAGE - The method for preparation of memantine hydrochloride provides high yield product; is simple; has easy operations; is environment-friendly; and is suitable for industrial scale production of memantine hydrochloride.
NOVELTY - Preparation of pitavastatin calcium intermediate involves hydrolysis of ester compound with metal compound in lower hydrolysis condition to form carboxylic acid compound, where hydrolysis medium is alcohol; and treating the carboxylic acid compound with a reducing agent under lower condition to form pitavastatin calcium intermediate, where step includes taking reducing agent under the protection of nitrogen, stirring, at room temperature adding carboxylic acid compound and raising the temperature to 70-100 degrees C to form the pitavastatin calcium intermediate compound.    USE - For the preparation of pitavastatin calcium intermediate (claimed), where pitavastatin calcium is used as hypolipidemic drug.    ADVANTAGE - The method is more favorable for hydrolysis reaction as compared to hydrolysis used in existing technology, has aqueous solution hydrolysis time of 3-4 days, and has hydrolysis time of less than 20 hours. The method provides product in high yield; has short reaction time; has low energy consumption and device cost; and has low production cost. The method uses two-step method to prepare pitavastatin calcium intermediate, uses inexpensive reducing agent, is low cost, has low cost of preparation, has process flow that is easy to control, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of pitavastatin calcium intermediate of formula (I) involves hydrolysis of ester compound of formula (II) with metal compound in lower hydrolysis condition to form carboxylic acid compound of formula (III), where hydrolysis medium is alcohol; and treating the carboxylic acid compound (III) with a reducing agent under lower condition to form pitavastatin calcium intermediate, where the step of reaction with reducing agent includes taking reducing agent under the protection of nitrogen, stirring, then at room temperature adding carboxylic acid compound (III), and then raising the temperature to 70-100 degrees C to form (I).
NOVELTY - The apparatus has a pair of rollers that is pressurized and drawn out, while interposing and heating the electrolytic membrane (1) and electrode element in the state made to mutually contact. The conveyance path conveys the electrolytic membrane on a pair of roller, and transfers from the gravitational direction downward direction between a pair of rollers. The electrode element is conveyed to pair of rollers and equipped with secondary conveyance path transferred between pair of rollers.    USE - Joining apparatus for joining electrolytic membrane and membranous electrode element for fuel cells during manufacturing process of membrane electrode assembly.    ADVANTAGE - The generation of wrinkle on electrolytic membrane is suppressed, the bondability of electrolytic membrane and catalyst electrode is improved, the size of the apparatus is reduced, the usability of the manufacturing apparatus of membrane electrode assembly is improved and cost of the apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for joining electrolytic membrane and membranous electrode element for fuel cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the joining apparatus. (Drawing includes non-English language text)    Electrolytic membrane (1)    Catalyst layer (3)    Heated roller (23)    Sheet peeling portion (30)    Junction portion (40)
NOVELTY - One a comminuted straw material continuous mixing heating multifunctional packing auger, comprising a shell and a through packing auger rotating shaft, one end of said shell are respectively provided with a feeding port and of steam inlet and the other end is provided with a discharging port and are to be mixed liquid material inlet. This utility new type working time, material feeding port entering into moving to the discharging direction of the push packing auger, in the process, the material is pre-heated and access to be mixed liquid material, and then entering into in subsequent reaction device through the discharging port. This utility new type of beneficial effects: it realizes the integrated pre-treated, pre-heating and mixing of comminuted straw material and improves the production efficiency, reduces the working amount of worker, can be suitable for large-scale industrial production of.
NOVELTY - Method for preparing fertilizer using bait fish residual excrement involves collecting bait fish residual excrement, filtering the collected excrement using 180-220 meshes sieve, removing waste and harmful substance from the obtained excrement using tap water, drying the residues of bait excrement, crushing, uniformly mixing, and sieving the dried residues, and measuring nitrogen and phosphorus ratio and adjusting to 8:1-12:1.    USE - The method is useful for preparing fertilizer using bait fish residual excrement (claimed).    ADVANTAGE - The method enables to prepare product cost-effectively and environmentally-friendly.
NOVELTY - 2,3,20-trihydroxy-29-dihydroxyolean-12-en-28-oic acid (I) and its salts are new.    USE - In the preparation of antidiabetic medicine for treating II type diabetes.    ADVANTAGE - The compound is stable and easy to store, improves the economic benefit, and is environment-friendly.    DETAILED DESCRIPTION - 2,3,20-trihydroxy-29-dihydroxyolean-12-en-28-oic acid (I) and its salts are new. INDEPENDENT CLAIMS are included for the following:    (1) preparing esterified derivatives of the compound (I), involving: esterifying at least one of the hydroxyl groups at the 2nd, 3rd, and 20th positions and the carboxyl group at the 28th position of the compound (I) with an organic acid or an organic alcohol; and    (2) preparing the compound (I).
NOVELTY - The method involves removing solid granules from a granulator (1) and feeding the solid granules into a granulate cooler (2). Dust-containing gas (D8) is removed from the granulator and feed into a first washer. The first washer is filled with substance-containing gas. Purified gas stream (D10) is removed from a first scrubber (9) and passed into a second scrubber (14) from a second washer. A third scrubber (11) is filled with aqueous liquid and non-aqueous liquid that includes a raw material, where working temperature of the second washer is lower than that of the first washer.    USE - Method for manufacturing granules e.g. urea and ammonium nitrate, from liquid and a source material i.e. fertilizer, using granulation process.    ADVANTAGE - The method enables reducing ejection of submicron dust into an atmosphere in an energy-efficient, flexible and reliable manner without increasing pressure drop across the scrubbers and recycling solid products at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing granules from e.g. liquid.    Purified gas stream (D10)    Dust-containing gas (D8)    Granulator (1)    Granulate cooler (2)    Scrubbers (9, 11, 14)
NOVELTY - The purifier has a blower (10) that feeds biogas from an anaerobic digester (2) to a main cooling device (31) of a refining module (20). The refining module refines impurity contained in biogas from blower. A sensor (61,62) detects temperature and concentration of bio-methane in biogas. The main cooling device cools concentration of bio-methane in biogas supplied in the digester. An adsorption module (40) separates bio-methane from biogas refined in the refining module. A control module reduces cycle time of adsorption module based on the sensed concentration of methane.    USE - Purifier for purifying biogas generated from biomass waste such as food waste, livestock excretion, and slaughter waste, energy crop, sewage sludge and high-concentrated organic waste.    ADVANTAGE - The operation of adsorption module can be controlled effectively by the control unit. The quality of bio-methane can be improved. The degradation in purification performance of purifier due to change of ambient temperature or biogas can be prevented. The productivity of bio-methane can be improved. The bio-methane can be collected and re-circulated easily. The driving range of purifier can be expanded. The moisture contained in biogas can be removed efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a control method of purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the purifier. (Drawing includes non-English language text)    Anaerobic digester (2)    Blower (10)    Refining module (20)    Cooling device (31,32)    Adsorption module (40)    Sensor (61,62)
NOVELTY - Co-production of liquid ammonia and methane comprises introducing ammonium phosphate solution or suspension in a tube-type reactor at 60-100 degrees C and 10-50 KPa for 15-50 minutes to obtain diammonium phosphate and hydrogen chloride gas; carrying out heat decomposition at 130-190 degrees C and 10-50 KPa, and decomposing ammonia gas to obtain mixture of phosphoric acid and sodium hexametaphosphate; compressing, and condensing to obtain liquid ammonia; and reacting hydrogen chloride gas and methanol gas at 150-600 KPa and 180-340 degrees C to obtain methane.    USE - Method for the co-production of liquid ammonia and methane (claimed).    DETAILED DESCRIPTION - Co-production of liquid ammonia and methane comprises:    (A) pre-mixing 30-98 wt.% ammonium chloride and phosphoric acid at normal pressure, where the ratio of ammonium chloride and phosphoric acid is 1:1.5-1:2.5, to obtain a ammonium phosphate solution or suspension;    (B) introducing ammonium phosphate solution or suspension in a tube-type reactor at 60-100 degrees C and 10-50 KPa for 15-50 minutes to obtain diammonium phosphate and hydrogen chloride gas;    (C) carrying out heat decomposition of diammonium phosphate and hydrogen chloride gas at 130-190 degrees C and 10-50 KPa, and decomposing ammonia gas to obtain mixture of phosphoric acid and sodium hexametaphosphate;    (D) compressing, and condensing to obtain liquid ammonia; and    (E) drying hydrogen chloride gas in a drying tower, introducing hydrogen chloride gas and methanol gas in a fluidized bed reactor at 150-600 KPa and 180-340 degrees C to obtain methane.
NOVELTY - A heterogeneous fatty acid methyl ester biodiesel is prepared by reacting fatty acid methyl ester biodiesel feedstock and gaseous hydrocarbon at mol ratio gaseous hydrocarbon:fatty acid methyl ester of 10-40:1, adding 2-10 wt.% supported catalyst, and reacting by alkylation process at 6-8 MPa and 90-130 degrees C for 2-4 hours.    USE - Preparation of heterogeneous fatty acid methyl ester biodiesel (claimed).    ADVANTAGE - The biodiesel has excellent oxidative and hydrolytic stability, low pour point and high quality, and is safe.
NOVELTY - A urea formaldehyde compound fertilizer is prepared by mixing 100-120 Kg urea and 30-33 Kg formaldehyde, reacting at 85-90 degrees C, taking 6-50 wt.% urea, 1-50 wt.% monoammonium phosphate, 0-50 wt.% potassium sulfate, 5-40 wt.% organic matter, 5-40 wt.% ammonium sulfate and 1-20 wt.% bentonite, mixing, pelleting, drying at 180-200 degrees C, conveying, drying at 130-150 degrees C, screening, cooling, refining, film coating cylinder anti plate structure processing, adding beta -bacteria, and packing.    USE - Method for preparing urea formaldehyde compound fertilizer (claimed).    ADVANTAGE - The fertilizer utilization rate is up to 70%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of beta -bacteria comprising:    (A) taking bacteria, washing, cleaning, sterilizing, coating at 30 degrees C, culturing for 24 hours, inoculating, scraping, separating beta strain, and culturing for at 30 degrees C for 24 hours;    (B) weighing 3 mL of 30 wt.% beef extract, 2 mL of 50 wt.% peptone and sodium chloride, adding water, diluting to 200 mL, agitating with glass rod, heating, adding alkaline, adjusting pH to 7.4, adding 4 g agar, heating, melting, agitating with glass rod, filtering, transferring in sterile test tube, sterilizing at 120 degrees C for 30 minutes, cooling, inoculating, and shaking; and    (C) taking beta bacteria, heating at 100-150 degrees C, sterilizing, lowering temperature to 50 degrees C, pumping, injecting water, filtering, culturing for 12-24 hours, centrifuging, drying, crushing into 200 mesh, and packing.
NOVELTY - A multifunctional microbial organic fish fertilizer comprises 25-30 wt.% high protein substance, 2-5 wt.% composite microbial bacteria, 8-10 wt.% amino acid, 5-8 wt.% fulvic acid, 25-30 wt.% inorganic nitrogen fertilizer, 15-20 wt.% inorganic phosphate fertilizers, 2-4 wt.% inorganic fertilizer, 0.5-2 wt.% microelement and 3-6 wt.% zeolite powder, where high protein substance comprises livestock manure, crop waste and promoting rot fungi through fermentation process.    USE - Multifunctional microbial organic fish fertilizer.    ADVANTAGE - The fertilizer can improve water quality and increase dissolved oxygen in water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of multifunctional microbial organic fish fertilizer comprising mixing high protein and composite microbial bacteria, stirring, fermenting for 7-10 days, adding amino acid, fulvic acid, microelement, inorganic nitrogen fertilizer, inorganic phosphate fertilizer, inorganic fertilizer and zeolite powder, stirring, mixing, and crushing.
NOVELTY - A corn biological wettable powder pesticide fertilizer comprises 0.5-1 Kg polyglutamic acid, 100-180 Kg attapulgite powder, 30-90 Kg Bacillus subtilis, 25-50 Kg moroxydine hydrochloride, 25-55 Kg amino oligosaccharin, 15-30 Kg matrine mother liquid, 30-50 Kg Bacillus thuringiensis, 30-90 Kg zinc sulfate, 30-70 Kg borax, 10-20 Kg lignin, 150-250 Kg activated carbon and balance additive.    USE - Corn biological wettable powder pesticide fertilizer.    ADVANTAGE - The pesticide fertilizer is effective against corn borer, spider mites, caterpillars, aphids and midge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of corn biological wettable powder pesticide fertilizer comprising taking matrine mother liquid, adding water, diluting, adding lignin and activated carbon, drying, taking zinc sulfate, borax, attapulgite powder, polyglutamic acid and moroxydine hydrochloride, mixing, drying, combining mixtures, adding Bacillus subtilis, Bacillus thuringiensis and amino oligosaccharin, mixing, adding 1000 Kg additive, and crushing.
NOVELTY - Production of organic fertilizer comprises crushing fresh tobacco into 1-2 cm, putting into fermentation tank, adding 1.0% probiotic, covering top layer, and fermenting for 30 days to obtain dark brown; mixing 40% tobacco dreg, 40% peat, 10% oil cake and 10% flower dreg and performing stacking fermentation; adding water in 0.5% probiotic, mixing, stacking for 35 days; and decompositing organic material for 5 days, and fermenting for 15 days.    USE - Method for producing organic fertilizer (claimed) used for tobacco leaf reuse resources.    ADVANTAGE - The fertilizer reaches NY525-2012 standard for organic fertilizer, improves fertility of organic fertilizer, and reduces chemical pesticides applied for safety of crops.
NOVELTY - The burner has a feeding machine that is connected with automatic rotary pre-heating bucket (3) through a feeding screw (2). The automatic rotary preheating bucket is arranged with upper water processor and is connected with heat exchanger (4). A rotary carbonization cracking machine (5) is connected with cracking bucket through feeding screw. A bucket cooling screw rod is connected with a cooling tank through cooling screw (7). The automatic packaging carbonization cracking machine is connected with cracking heater (6) and water processor.    USE - Automatic burner for biomass pellet production line.    ADVANTAGE - The production efficiency of biomass can be improved while reducing the usage of manpower and material resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic burner.    Feeding screw (2)    Automatic rotary pre-heating bucket (3)    Heat exchanger (4)    Rotary carbonization cracking machine (5)    Cracking heater (6)    Cooling screw (7)
NOVELTY - A fischer-tropsch (FT) diesel-methanol-biodiesel fuel contains 82-62 vol.% FT diesel, 5-10 vol.% methanol, 10-20 vol.% biodiesel and 3-8 wt.% latent solvent, 70-47 vol.% FT diesel, 10-20 vol.% methanol, 10-20 vol.% biological diesel and 10-13 vol.% latent solvent, or 59-32 vol.% FT diesel, 20-30 vol.% methanol, 10-20 vol.% biodiesel and 11-18 vol.% latent solvent.    USE - A fischer-tropsch (FT) diesel-methanol-biodiesel fuel for engines (claimed).    ADVANTAGE - The method is simple, and fuel is stable, clean, and has excellent performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of FT diesel-methanol-biodiesel fuel which involves adding FT diesel, latent solvent, methanol and biodiesel in container, and stirring for 5-10 minutes to obtain uniform solution.
NOVELTY - A microbial compound fertilizer comprises 20-50 pts. wt. Aspergillus niger (CGMCC No.7927), and 20-35 pts. wt. Bacillus subtilis (CGMCC No.7926).    USE - A microbial compound fertilizer used for grains and vegetables.    ADVANTAGE - The fertilizer improves grain yield to 8-30% and vegetable yield to 10-40%, and improves vegetable quality and flavor of grain.
NOVELTY - Preparation of a microbial composite fertilizer comprises fermenting Aspergillus niger culture and Bacillus subtilis culture.    USE - Method for the preparation of a microbial composite fertilizer (claimed) used for grains and vegetables.    ADVANTAGE - The fertilizer improves grain yield at 8-30%, vegetable yield at 10-40 %, vegetable quality, and flavor of food.
NOVELTY - A microbial fertilizer comprises 18-26 pts. wt. Aspergillus niger (CGMCC No.7927), 3-5 pts. wt. Bacillus megaterium, 10-20 pts. wt. Lactobacillus plantarum (CGMCC No.7928), and 25-36 pts. wt. Bacillus subtilis microbial inoculum (CGMCC No.7926).    USE - A microbial fertilizer used for crops.    ADVANTAGE - The fertilizer improves micro-ecological environment of soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for preparing B. subtilis microbial inoculum (CGMCC No.7926) by using inclined plane strain cultivation to gradually obtain B. subtilis culture broth, fermenting, liquid separating, and drying; preparing L. plantarum (CGMCC No.7928) by concentrating L. plantarum fermentation broth in vacuo at low temperature to 45% of the original volume to obtain a concentrated bacteria solution, adding vector, uniformly mixing, adding a carrier comprising 25 pts. wt. calcium carbonate and 12 pts. wt. dextrin, and fluidized bed drying at 50 degrees C; and preparing A. niger (CGMCC No.7927) by fluidized bed drying solid fermentation culture medium at 60 degrees C to obtain a moisture content of less than 10%, and crushing to a mesh aperture of greater than or equal to 60 meshes.
NOVELTY - Microecological fertilizer comprises 20-28 pts. wt. Bacillus subtilis Li-2013-02 (CGMCC 7926), 15-25 pts. wt. Aspergillus niger culture, and 8-15 pts. wt. Lactobacillus plantarum agent.    USE - Microecological fertilizer.    ADVANTAGE - The microecological fertilizer can improve soil microecological environment, thus providing favorable conditions for crops growth while enhancing crop resistance to pests and diseases.
NOVELTY - Microecological compound fertilizer comprises 5-10 pts. wt. Aspergillus niger (CGMCC 7927) culture, 3-8 pts. wt. glial bacterium Bacillus spores, 3-8 pts. wt. large solubilizing bacterium Bacillus spores, 5-12 pts. wt. Bacillus subtilis culture, 4-7 pts. wt. Aspergillus awamori culture, and 2-4 pts. wt. Lactobacillus agent.    USE - Microecological compound fertilizer.    ADVANTAGE - The microecological compound fertilizer can improve soil microecological environment, while providing favorable conditions for crops growth.
NOVELTY - Preparation of composite biological fertilizer comprises respectively culturing and fermenting Aspergillus niger, solubilizing Bacillus megaterium, and Bacillus subtilis; and taking 20-50 pts. wt. A. niger culture, 5-10 pts. wt. solubilizing B. megaterium culture, and 10-30 pts. wt. B. subtilis culture as raw material for fertilizer.    USE - Preparation of composite biological fertilizer.    ADVANTAGE - The composite biological fertilizer can increase food production by 8-30% and vegetable production by 10-40%, and improves vegetables and food quality and flavor. It is highly-efficient and can be applied at 50-100 g/acre of land.
NOVELTY - Preparation of organic fertilizer involves taking livestock manure as raw material; preprocessing to adjust moisture content to 55-65%; adding pretreated material with fermenting bacteria A; fully stirring and turning into fermentation stack pile in fermentation reactor; fermenting at 50 degrees C with turning to obtain fermented organic fertilizer with moisture content reduced to 35-45%; transferring fermented organic fertilizer into disc granulator; adding fermentation bacteria B and clay; and granulating to obtain organic fertilizer.    USE - Preparation of organic fertilizer (claimed).    ADVANTAGE - The method produces organic fertilizer that is suitable for winter, can increase greenhouse temperature by 3-6 degrees C, and promotes robust development of plant roots and stems.    DETAILED DESCRIPTION - Preparation of organic fertilizer comprises taking livestock manure as raw material; preprocessing to adjust moisture content to 55-65%; adding pretreated material with fermenting bacteria A; fully stirring and turning into fermentation stack pile in fermentation reactor; fermenting at 50 degrees C with turning to obtain fermented organic fertilizer with moisture content reduced to 35-45%; transferring fermented organic fertilizer into disc granulator; adding fermenting bacteria B and clay; and granulating to obtain organic fertilizer, in which fermenting bacteria A or B are mixed strain of Azotobacter chroococcum, large Bacillus megaterium spores, and Streptomyces microflavus.
NOVELTY - Production of organic fertilizer comprises milling collected plant straw to obtain 1-2 cm granules; preparing first pre-dipping solution, adjusting pH value to 9-10, and soaking obtained granules at solid-liquid ratio of 1:4 at 60-90 degrees C for 20-40 minutes; adding mixed Aspergillus strains and second dipping solution, adjusting pH value to 9, and fermenting for 7-10 days; extruding, adding residue to step 3 while filtering liquid, and discharging residue; and concentrating filtrate, granulating. The second dipping solution is nitrogen-containing weak alkaline.    USE - Method for production of organic fertilizer (claimed).    ADVANTAGE - The method shortens fertilizer production time and increases its valid nutrition content.
NOVELTY - A trace element-containing water-soluble fertilizer comprises 5.5-6 pts. wt. magnesium, 0.7-1 pt. wt. calcium, 0.05-0.15 pts. wt. boron, 2-2.3 pts. wt. manganese, 3-3.5 pts. wt. zinc, 1.25-1.5 pts. wt. iron, 0.5-0.8 pts. wt. molybdenum, 3.6-3.9 pts. wt. ammonium, 0.3-0.7 pts. wt. sodium, 9-11.5 pts. wt. sulfur, 0.3-0.6 pts. wt. silicon, 0.5-0.8 pts. wt. aluminum, and 0.7-0.9 pts. wt. iodine.    USE - Trace element-containing water-soluble fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by adding sugarcane molasses as carbon source biogas system (BS) decomposition bacteria and trace element ore powder as growth nutrient source into open-type fiber reinforced plastic (FRP) aerobic fermentation barrel to carry out biochemical metabolism to obtain aerobic growth while simultaneously performing aerobic fermentation to obtain organic acid, and lowering pH value; performing biological acid hydrolysis, mixing, releasing trace element in acidic environment to carry out co-existing of ions in liquid mixture, adding different ore powder, and stirring for 5-6 days to obtain trace elements-containing liquid mixture; and automatically filling into bottles, sealing, and storing.
NOVELTY - A peanut biological wettable powder fertilizer comprises 35-90 Kg humic acid, 30-80 Kg diethyl aminoethyl hexanoate, 30-80 Kg Bacillus subtilis, 20-50 Kg amino-oligosaccharin, 60-250 Kg minerals, 50-100 Kg borax, 200-500 Kg silica, 30-80 Kg chelated calcium, 20-80 Kg dispersing agent and additive.    USE - Peanut biological wettable powder fertilizer used for crop seedlings.    ADVANTAGE - The fertilizer activates soil, improves crop quality, reduces fruit deformity and increases fruit yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of peanut biological wettable powder fertilizer comprising mixing humic acid, diethyl aminoethyl hexanoate, Bacillus subtilis, amino oligosaccharin, minerals, borax, silica, chelated calcium and dispersing agent, adding 1000 Kg additive, drying, and crushing.
NOVELTY - A mushroom cultivation material comprises 55-60 pts. wt. chestnut branch, 25-30 pts. wt. chestnut shell, 20-22 pts. wt. wheat bran, 10-12 pts. wt. sunflower seed oil slag, 15-17 pts. wt. citric acid residue, 15-18 pts. wt. black soil, 1-1.5 pts. wt. iron ore powder, 3-5 pts. wt. boric sludge, 10-12 pts. wt. mung bean powder, 5-7 pts. wt. ginseng, 4-5 pts. wt. straight ladybell root, 3-5 pts. wt. Ganoderma lucidum, 6-7 pts. wt. glutinous rice, 7-8 pts. wt. Abrus cantoniensis, 1-2 pts. wt. lime powder, 0.1-0.2 pt. wt. yeast and 6-7 pts. wt. nutritional additive.    USE - Mushroom cultivation material.    ADVANTAGE - The cultivation material is low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivation material comprising taking chestnut branch and chestnut shell, sun drying for 18-20 hours, crushing, taking wheat bran, sunflower seed oil slag and citric acid residue, adding, soaking for 2-3 hours, adding mung bean powder, mixing, adding yeast, fermenting at 30-40 degrees C for 2-3 hours, mixing lime powder and water, stirring, taking ginseng, straight ladybell root, Ganoderma lucidum and glutinous rice, crushing, adding remaining raw materials, mixing, adding water, stirring, and steaming at 100 degrees C.
NOVELTY - A mushroom cultivation material comprises 40-44 pts. wt. sawdust, 30-32 pts. wt. tea seed shell, 18-20 pts. wt. wheat bran, 7-8 pts. wt. rapeseed dregs, 15-18 pts. wt. corn, 10-12 pts. wt. hay, 3-4 pts. wt. tuckahoe, 4-5 pts. wt. semen raphani, 2-3 pts. wt. rose, 3-4 pts. wt. chicken rib, 8-10 pts. wt. zeolite powder, 7-9 pts. wt. iron ore slag, 6-7 pts. wt. shell powder, 22-25 pts. wt. buckwheat flour, 0.2-0.3 pt. wt. yeast, fish soup, 1-1.5 pts. wt. lime powder and 4-5 pts. wt. nutritional additive.    USE - Mushroom cultivation material.    ADVANTAGE - The culture material has good ventilation property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mushroom cultivation material comprising mixing lime powder and fish soup, stirring, taking sawdust, tea seed shell, wheat bran, rapeseed dregs and corn, sun drying for 20-22 hours, adding water, soaking for 2-3 hours, adding buckwheat, mixing, adding yeast, fermenting at 30-40 degrees C for 3-4 hours, taking hay, tuckahoe, semen raphani, rose and chicken rib, crushing, adding remaining raw materials, mixing, adding water, stirring, and steaming at 100 degrees C.
NOVELTY - A mushroom cultivation material comprises 40-44 pts. wt. peanut shell, 35-38 pts. wt. soybean straw, 17-19 pts. wt. corn meal, 10-12 pts. wt. vinegar, 1-2 pts. wt. lime powder, 1-2 pts. wt. gypsum powder, 0.2-0.3 pt. wt. monopotassium phosphate, 0.4-0.5 pt. wt. chitosan, 4-5 pts. wt. Cordyceps sinensis, 4-5 pts. wt. mint, 3-4 pts. wt. burdock root, 5-6 pts. wt. holly root, 20-22 pts. wt. rabbit manure, 0.2-0.3 pt. wt. effective microorganism, 12-15 pts. wt. beef soup and 5-6 pts. wt. nutritional additive.    USE - Mushroom cultivation material.    ADVANTAGE - The cultivation material is low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivation material comprising sun drying rabbit manure for 15-18 hours, mixing beef soup and effective microorganism, fermenting for 19-23 days, mixing lime powder, monopotassium phosphate and chitosan, adding water, stirring, taking peanut, soybean straw, Cordyceps sinensis, mint, burdock root and holly root, adding remaining raw materials, stirrer, adding water, and steaming at 100 degrees C.
NOVELTY - A mushroom cultivation material comprises 50-55 pts. wt. corn cob, 20-22 pts. wt. rice bran, 18-20 pts. wt. shrimp bran, 1-2 pts. wt. gypsum powder, 2-3 pts. wt. white sugar, 1-2 pts. wt. sulfur powder, 7-8 pts. wt. coal gangue, 3-4 pts. wt. coal slurry, 7-8 pts. wt. hoof powder, 12-15 pts. wt. blood meal, 5-7 pts. wt. ginseng flower, 6-8 pts. wt. large-headed atractylodes rhizome, 4-5 pts. wt. Cassia seed, 6-7 pts. wt. radix paeoniae alba, 5-6 pts. wt. oat grass, 4-5 pts. wt. black root, 10-12 pts. wt. onion juice and 5-6 pts. wt. nutritional additive.    USE - Mushroom cultivation material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivation material comprising mixing corn cob and coal gangue, adding onion juice, standing for 22-24 hours, adding water, soaking for 2-3 hours, mixing white sugar and water, heating, stirring, taking ginseng flower, large-headed atractylodes rhizome, Cassia seed, radix paeoniae alba, oat grass and black root, crushing, adding remaining raw materials, mixing, adding water, stirring, and steaming at 100 degrees C.
NOVELTY - A mushroom cultivation material comprises 55-60 pts. wt. apple branch, 30-33 pts. wt. wheat bran, 18-20 pts. wt. crab shell, 15-18 pts. wt. cassava dregs, 10-12 pts. wt. kiryu sand, 12-13 pts. wt. kaolin, 8-9 pts. wt. blood meal, 7-8 pts. wt. feather powder, 10-11 pts. wt. corn syrup, 11-12 pts. wt. glutinous rice flour, 4-5 pts. wt. dried orange peel, 3-4 pts. wt. endothelium corneum gigeriae galli, 4-5 pts. wt. fructus ligustri lucidi, 5-6 pts. wt. nutgrass flatsedge, 2-3 pts. wt. Colquhounia, 1-2 pts. wt. lime powder and 5-6 pts. wt. nutritional additive.    USE - Mushroom cultivation material.    ADVANTAGE - The cultivation material has improved air permeability and moisture retention.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mushroom cultivation material comprising taking apple branch and crab shell, crushing, adding wheat bran and cassava residue, adding water, soaking for 2-3 hours, adding blood meal, feather powder, corn syrup and glutinous rice flour, mixing, adding yeast, fermenting at 30-40 degrees C for 2-3 hours, mixing dried orange peel, endothelium corneum gigeriae galli, fructus ligustri lucidi, nutgrass flatsedge and Colquhounia, adding remaining raw materials, mixing, adding water, stirring, and steaming at 100 degrees C.
NOVELTY - The detector has an infrared light source unit connected with a pulse electro-modulation infrared light source module. A pre-amplification circuit is connected with an infrared sensor and a narrow band filter circuit. The pre-amplification circuit receives gas concentration signal, where the pre-amplification circuit is connected with a measurement and control system. The infrared sensor is connected with an upper part of a packaging module that is connected with a narrow band interference filter. The measurement and control system receives infrared receiving signal.    USE - Non-dispersive infrared gas detector.    ADVANTAGE - The detector is easy to detach a pneumatic room, and reduces infrared sensor in an efficient manner and improves detecting precision and carbon dioxide, carbon monoxide, nitrogen oxide, methane and sulfur dioxide gas measuring speed and efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a non-dispersive infrared gas detector.'(Drawing includes non-English language text)'
NOVELTY - This utility new type claims a one for flue gas denitration urea hot solution made of ammonia reactor, include reactor main body, lower part of reactor main body is provided with a used for the upper part of gas inlet, a reactor main body of air or gas is provided with a reaction product outlet, side of reactor main body is provided with multiple opening used for the reactor main body into the urea solution of solution inlet, the outer side of reactor main body up to down with multiple groups of heating resistance wire, and each group of heating resistance wire connecting with a corresponding temperature control device. This utility new type is provided for the urea solution of solution inlet on the side of reactor main body, at the same time, outside the reactor main body side is mounted to the reactor for heating of heating resistance wire, it can make the urea pyrolysis conversion in the reactor, so the utility model is new type low cost, simple control, it will not produce second pollution.
NOVELTY - This utility new type of anaerobic ammonia oxidation reactor, include clapboard, ammonia oxidation chamber, rear ammonia oxidation room, a water distributor, a water outlet weir groove, combination filler, a water inlet tube, a water pipeline, a water outlet tube, a marsh gas outlet, a manhole, a safety packing, discharging valve. This utility new type of anaerobic ammonia oxidation reactor process is simple and practical, used for processing cultivation sewage, which not only can be valid for removing organic matter, but also can enrich large amount of anaerobic ammonia oxidizing bacteria, there is no need to newly-added carbon source, it can realize good ammonia oxidation process, valid to remove ammonia nitrogen. Device is simple in structure, low in cost, it can module manufacturing and scale production, convenient transportation, fast, small floor area, low investment cost is low.
NOVELTY - This utility new type processing one provide a municipal sludge resource treatment of device, include sintering brick tunnel kiln device, that is, include stirrer, brick, moulding workshop factory building, and include drying section, pre-heating section, a high temperature roasting section, tunnel kiln of cooling section, cooling section tunnel kiln is equipped with waste heat boiler, the waste heat boiler connect with a waste heat utilization system, wherein it further comprise a municipal sludge anaerobic nitration system, a municipal sludge anaerobic nitration system comprise in turn connecting of sludge raw material tank, the anaerobic nitrifying tank and biogas residue tank of machine, an anaerobic nitrifying tank through waste heat boiler of biogas pneuma fan and the sintering brick tunnel kiln device connect, slag tank through the slag slurry pump and the sintering brick tunnel kiln device of stirrer connecting. This utility new type realizes harmless, decrement and resource treatment of municipal sludge.
NOVELTY - This utility new type claims a one capable of heating type aerobic composting cabin body, include the aerobic compost cabin body, said aerobic compost cabin body set with feeding port and discharging port, said feeding port and one feeding machine is connected, said aerobic compost cabin body futher set with one cabin body water inlet and one water outlet cabin, wherein the heating type aerobic composting cabin body futher comprise one solar cabin outlet is connected with a solar heat collecting plate of hot water inlet are connected, said cabin body is connected with the water outlet of solar heat-collecting hot plate connected. This utility new type through using solar energy heat collecting plate for aerobic compost process auxiliary heating cabin body, which can greatly shorten the life garbage aerobic compost of time period, and through accurate control ventilation quantity, the compost process is more reasonable and more efficient. Using solar energy and shorten the aerobic compost of period, energy-saving and environment-friendly, fertilizer mass of aerobic compost is produced. At the same time, the whole system device operation is simple, safety and reliable and practical.
NOVELTY - This utility new type relates to one suitable for a livestock and poultry excrement stack fertilizer volatile gas recovery of system. The system of compost fermentation storehouse, gas conveying pipeline, a centrifugal fan and a gas absorbing chamber. Ammonia absorbing chamber include gas distribute pipeline, and absorbing material. Livestock and poultry excrement stack fertilizer in process, the centrifugal fan of the compost fermentation storehouse all ammonia gas, and ammonia gas into the absorbing chamber, rear gas through gas distribute uniformity distribute pipeline, in turn entering into padding layer and absorption material layer, the ammonia gas is absorbed and the microorganism a material absorption and conversion process and the absorption material of in contact so as to realize recovery of ammonia gas. Conveying to the absorption material at the bottom of the system by centrifugal fan and of the ammonia gas, and rear gas distribute pipeline by the gas distribute uniformity ammonia recovery process, which greatly improves the recovery efficiency of. At the same time, the system has simple structure, makes full use of agricultural resource, it has low cost, high efficiency and no second pollution and so on.
NOVELTY - A composite graphene catalyst comprises graphene and perovskite catalyst in which amount of graphene is 0.5-10 mass% of amount of pervoskite catalyst.    USE - A composite graphene catalyst for methane production (claimed).    ADVANTAGE - Catalyst has improved catalytic activity and increased specific surface area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite graphene catalyst which involves adding graphene oxide to aqueous alcohol solution, stirring, adding perovskite catalyst to obtain mixed solution in which volume ratio of water and alcohol is 1:1, 12-25 ml aqueous alcohol solution is added per g of perovskite catalyst, and amount of graphene oxide is 0.5-10 mass% of amount of perovskite catalyst, magnetically stirring, refluxing at 100 degrees C for 2 hours, adding reducing agent in which weight ratio of graphene oxide and reducing agent is 1:3-5, stirring for 6 hours, vacuum filtering, drying, and grinding.    DESCRIPTION OF DRAWING(S) - The drawing shows a curve of composite graphene catalyst catalytic activity. (Drawing includes non-English language text).
NOVELTY - A waste oil and dried mud mixed fuel restaurant kitchen waste environment-friendly treatment system comprises kitchen waste preprocessing system, hopper preheating system, waste oil preprocessing system, combustion system, drying system, cooling system, packaging system, and waste heat circulation system.    USE - Waste oil and dried mud mixed fuel restaurant kitchen waste environment-friendly treatment system.    ADVANTAGE - The reliable system changes waste into treasure, saves energy, and does not produce secondary pollution. It has strong operability, low operation cost, and good economical benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of waste oil and dried mud mixed fuel restaurant kitchen waste environment-friendly treatment system (Drawing includes non-English language text).
NOVELTY - A municipal solid waste is agglomerated by crushing municipal solid waste (S100), mixing with bentonite (S200), and performing extrusion molding (S300).    USE - Agglomeration of municipal solid waste (claimed).    ADVANTAGE - Agglomeration process reduces load pressing, reduces power consumption, and saves operation cost, and raw material has very strong swelling resistance, adhesion property, water absorption effect, and catalytic property.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for agglomeration of municipal solid waste. (Drawing includes non-English language text).    Crushing municipal solid waste (S100)    Mixing with bentonite (S200)    Extrusion molding (S300)
NOVELTY - A fuel-reforming hydrogen generator comprises fuel reaction room (1), heat exchanger (8), electrolysis room, flow pump (2), pressure gauge (4), thermometer (3), complete circulation system, electrolytic anode, and system controller.    USE - Fuel-reforming hydrogen generator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high purity hydrogen comprising mixing catalyst solution and fuel solution at 20-200 degrees C with pressure of 0.1-20 MPa, and reducing valence state of fuel solution, carbon dioxide and water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fuel-reforming hydrogen generator.    Fuel reaction room (1)    Flow pump (2)    Thermometer (3)    Pressure gauge (4)    Heat exchanger (8)
NOVELTY - A hydrogen production device comprises preprocessing system (1), heat exchange system (2), steam power boiler, hydrogen compression and refrigeration system (6), primary separator (4), and liquefied natural gas storage tank (3).    USE - Hydrogen production device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen production device (Drawing includes non-English language text).    Preprocessing system (1)    Heat exchange system (2)    Gas storage tank (3)    Primary separator (4)    Refrigeration system (6)
NOVELTY - Producing bone charcoal powder comprises choosing materials, degreasing, degumming, high temperature heating and sorting; where the step of choosing materials includes taking livestock bone mixture, and crushing in a crushing machine; and the high temperature heating includes adding the bone residues into feeding inlet of furnace via conveyor belt, calcining at 800 degrees C for 3-4 hours; and then cooling in a rotary drum.    USE - The method is useful for producing bone charcoal powder (claimed).    ADVANTAGE - The method is simple and easy to control, maintains the bone charcoal powder to remain at the bottom when odor is produces, and can maintain clean work.
NOVELTY - Recycling municipal wastewater for reuse at low energy, by (a) treating municipal sewage, (b) taking pump sewage into microbial fuel cells (MFC), performing anaerobic treatment of anode chamber, (c) passing the water into membrane bioreactor (MBR) by 0.5-1 cm thick carbon after anaerobic effluent treatment, performing aerobic treatment, (d) dividing two units MFC and MBR using 0.5-1 cm thick carbon, and (e) collecting water after aerobic wastewater treatment by MBR unit outlet, draining pump, and discharging piping for reuse.    USE - The method is useful for recycling municipal wastewater for reuse at low energy (claimed).    ADVANTAGE - The method consumes low energy.    DETAILED DESCRIPTION - Recycling municipal wastewater for reuse at low energy, involves (a) treating municipal sewage, where chemical oxygen demand of water is 100-500 mg/l and ammonia concentration of water is 10-50 mg/l at pH 6-9, (b) taking pump sewage into microbial fuel cells (MFC), performing anaerobic treatment of anode chamber for 10-14 hours hydraulic residence time (HRT) at 15-35 degrees C, where the anode material is carbon, graphite, and modified material, (c) passing the water into membrane bioreactor (MBR) by 0.5-1 cm thick carbon after anaerobic effluent treatment, performing aerobic treatment for 6-12 hours HRT at 15-35 degrees C, where dissolved oxygen concentration is 2-6 mg/l, and materials for conductive polymer-modified stainless steel mesh is non-woven, and carbon, (d) dividing two units MFC and MBR using 0.5-1 cm thick carbon, and (e) collecting water after aerobic wastewater treatment by MBR unit outlet, draining pump, and discharging piping for reuse.
NOVELTY - A modification of fungus-type biological absorption material is processed by modifying configuration of modifying liquid which is ferric trichloride to 0.08-0.1 M solution, dipping fungus-type aerobic sludge particle in modified liquid, performing vibration reaction at 25-35 degrees C constant temperature for 18-24 hours to obtain modified fungi-type sludge, repeatedly washing using deionized water until supernatant liquid is clear, colorless, and transparent, dipping in deionized water overnight, repeatedly washing until pH is stable, and storing.    USE - Modification process of fungus-type biological absorption material for improving antimony salt adsorption and removal.    ADVANTAGE - The process is simple, has short operation time, does not produce secondary pollution, saves resources, and obtains product with good sedimentation property, stable biocompatibility, and high removing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of removing rate of modified fungus-type biological absorption material to antimony and iron in solution at different pH conditions in which at 4.3 pH value, 35 degrees Celsius temperature and 175 rpm rotating speed, initial concentration is 20 mg/L. (Drawing includes non-English language text).
NOVELTY - Method for modifying the bacterial-type biological particle adsorbent material, involves modifying the configuration of 0.08-0.1 M modifying liquid, immersing bacterial type aerobic granular sludge in modifying liquid at 25-35 degrees C for 18-24 hours to obtain bacterial aerobic granular sludge materials, repeatedly washing using deionized water until the supernatant is clear, colorless and transparent, immersing the materials in deionized water for overnight, repeatedly washing using deionized water until the pH is stable, and storing the product.    USE - The method is useful for modifying bacterial-type biological particle adsorbent material (claimed).    ADVANTAGE - The method efficiently removes antimony, is simple, convenient and cost-effective to perform, performed rapidly, is environmentally-friendly, and modifies product which exhibits good biocompatibility and stability.    DETAILED DESCRIPTION - Method for modifying the bacterial-type biological particle adsorbent material, involves modifying the configuration of 0.08-0.1 M modifying liquid, immersing bacterial type aerobic granular sludge in modifying liquid at 25-35 degrees C for 18-24 hours to obtain bacterial aerobic granular sludge materials, repeatedly washing using deionized water until the supernatant is clear, colorless and transparent, immersing the materials in deionized water for overnight, repeatedly washing using deionized water until the pH is stable, and storing the product, where the modified liquid is ferric trichloride.
NOVELTY - Producing bacteria for decomposing straw involves performing fermentation by using liquid media containing bacteria, amino acid and peptides. The obtained product is dried at low temperature. The dried product containing bacteria is planted in soil for decomposition of straw.    USE - Method for producing bacteria for decomposing straw (claimed).    ADVANTAGE - The method enables to produce bacteria for decomposing straw quickly and efficiently in eco-friendly manner, and ensures sustainable development of country.
NOVELTY - Nutrient fertilizer comprises 50-60 pts. wt. tea, 20-30 pts. wt. plant ash, 10-15 pts. wt. egg shell powder, 10-15 pts. wt. soybean curb residue, and 180-200 pts. wt. water.    USE - The nutrient fertilizer is useful for planting flowering plants (claimed).    ADVANTAGE - The fertilizer utilizes domestic waste, can be prepared easily, and is convenient to use, cost-effective, green and pollution-free.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned components, and performing immersion of the mixture in water at 10-20 degrees C for 10-15 days or at 21-30 degrees C for 5-7 days.
NOVELTY - Degrading sulfa antibiotics in livestock and poultry excrement involves utilizing an anaerobic composting process. Raw compost manure is mixed with sawdust or rice straw, where carbon/nitrogen value is 20-30. Humidity of the compost is adjusted so that moisture content is reached 60-70%. The compost heap is fermented by utilizing a fermentation device, which has bucket, bucket bottom is processed with sand and stone, has 10 cm thickness. The compost is crushed in the bucket bottom part, which is connected with liquid outlet. The liquid outlet is coated by using a glass fiber cloth pipe.    USE - Method for degrading sulfa antibiotics from livestock and poultry manure (claimed).    ADVANTAGE - The method enables to degrade sulfa antibiotics from livestock and poultry manure is eco-friendly and safe for human body, and ensures to large-scale production.    DETAILED DESCRIPTION - Degrading sulfa antibiotics in livestock and poultry excrement involves utilizing an anaerobic composting process. Raw compost manure is mixed with sawdust or rice straw, where carbon/nitrogen value is 20-30. Humidity of the compost is adjusted so that moisture content is reached 60-70%. The compost heap is fermented by utilizing a fermentation device, which has bucket, bucket bottom is processed with sand and stone, has 10 cm thickness. The compost is crushed in the bucket bottom part, which is connected with liquid outlet. The liquid outlet is coated by using a glass fiber cloth pipe. Exhaust hole is present on upper region of bucket, where top of the bucket is sealed by using a plastic film. The compost process liberates gases once every two days. The compost process is continued for 35 days.
NOVELTY - Method for degrading sulfa antibiotics present in livestock and poultry manure, by mixing livestock and poultry manure with sawdust or rice straw, and adjusting carbon/nitrogen value, adjusting humidity and water content, adding processed mixture into fermentation device, and performing composting by providing ventilation for 1-2 weeks at a rate of 0.050 m3, later at rate of 0.030 m3, blasting for 5 hours 30 minutes and composting for 14 days, and turning the mixture once, until the water content reaches 60-70%, and composting for 35 days to obtain the product.    USE - The method is useful for degrading sulfa antibiotics present in excrement (claimed).    ADVANTAGE - The method is simple and suitable for industrial production and prevents pollution.    DETAILED DESCRIPTION - Method for degrading sulfa antibiotics present in livestock and poultry manure, involves (a) mixing livestock and poultry manure with sawdust or rice straw, and adjusting carbon/nitrogen value to 20-30, (b) adjusting humidity and water content to 60-70%, (c) adding processed mixture into fermentation device, where the device has barrel, and bottom of the barrel contains layer of cloth as gas reservoir, which is provided with gravel, and bamboo sieve is placed top of the mixture, and sieve is paved with rice straw for maintaining heat and moisture content, and ventilation pipe is connected to the lower side of the cloth and vent tube connected to blower for controlling ventilation rate, power and time, and (d) performing composting by providing ventilation for 1-2 weeks at a rate of 0.050 m3, later at rate of 0.030 m3, blasting for 5 hours 30 minutes and composting for 14 days, and turning the mixture once, until the water content reaches 60-70%, and composting for 35 days to obtain the product.
NOVELTY - Fertilizer comprises (in pts.wt.): biogas residue (20-30), coal (25-30), bamboo charcoal powder (15-30), photosynthetic bacteria powder (0.0001), Rhizopus stolonifer powder (0.0001), Bacillus licheniformis powder (0.0001), duck manure (25-30), cotton straw powder (15-20), oilseed straw powder (25-30), goose dung (15-20), Sarcandra glabra (15-20), cortex fraxini (3-6), radix stemonae (3-5), potassium sulfate (11-20), sodium chloride (10-20), boric acid (3-9), ammonium citrate (2-6), magnesium sulfate (3-7), manganese sulfate (2-6), zinc sulfate (1-4) and urea (15-20).    USE - Fertilizer used for planting tea tree (claimed).    ADVANTAGE - The fertilizer increases yield and improves quality of tea.
NOVELTY - Mountain tea tree fertilizer comprises 15-20 pts. wt. tea powder, 10-12 pts. wt. stone powder, 20-25 pts. wt. charcoal powder, 30-40 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 15-20 pts. wt. wheat bran, 10-20 pts. wt. rice straw powder, 10-15 pts. wt. corn straw powder, 0.001-0.002 pts. wt. silicate bacterial powder, 0.002 pts. wt. Bacillus cereus powder, 3-6 pts. wt. calcium superphosphate, 1-5 pts. wt. potassium sulfate, 3-6 pts. wt. calcium nitrate, 6-9 pts. wt. ammonium sulfate, 5-8 pts. wt. ammonium citrate, and 2-6 pts. wt. humic acid.    USE - As mountain tea tree fertilizer.    ADVANTAGE - The fertilizer is rich in organic and inorganic nutrient and cost-effective and trace element, improves soil, supplies nutrient to the tea, and improves quality of tea.
NOVELTY - Biofertilizer comprises (in pts.wt.): urea (35-40), ammonium chloride (11-16), diammonium hydrogen phosphate (15-26), weathered coal (25-30), bamboo charcoal powder (15-30), photosynthetic bacteria powder (0.0001), Rhizopus stolonifer powder (0.0001), Bacillus licheniformis powder (0.0001), duck manure (25-30), cotton straw powder (15-20), oil seed straw powder (25-30), goose dung (15-20), Sarcandra glabra (15-20), calcium superphosphate (3-6), potassium sulfate (1-5), nitric acid (3-6), ammonium sulfate (6-9), ammonium molybdate (5-8) and humic acid (2-6).    USE - Biofertilizer used for planting tea tree (claimed).    ADVANTAGE - The biofertilizer is cost-effective and improves soil nutrients for improving quality of tea.
NOVELTY - Biofertilizer comprises (in pts.wt.): humic acid containing fermentation liquid (100) and urea (15-20).    USE - Biofertilizer used as a foliar fertilizer and seed soaking agent (all claimed).    ADVANTAGE - The biofertilizer improves plant growth and development, prevents crops from diseases and improves yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biofertilizer, which involves:    (A) dissolving urea in fermentation liquid containing humic acid;    (B) preparing fermentation liquid involves utilizing (in pts.wt.): humic acid (100), soybean powder (10), fish meal (10), glucose (10), inorganic salt (0.1) and water (500), where inorganic salt is monopotassium phosphate, manganese sulfate or calcium chloride;    (C) sterilizing culture medium at 121 degrees C using steam for 20 minutes;    (D) cooling culture medium;    (E) inoculating microbial inoculum in 3% of culture medium under aerobic conditions:    (F) fermenting culture medium with continuous stirring at 180 revolutions/minute;    (G) maintaining culture medium at 0.05 megapascal;    (H) changing dissolved oxygen value to 20-40%;    (I) fermenting inoculum at 32-35 degrees C for 36-48 hours; and    (J) fermenting inoculum under anaerobic conditions at 32-35 degrees C for 48-60 hours with continuous stirring for 1-6 hours by adjusting pH value of fermentation liquid to 4.0-4.5 to obtain product.
NOVELTY - Composite fertilizer comprises (in pts.wt.):ammonium dihydrogen phosphate (20-30), EDTA calcium fertilizer (0.0001-0.0004),EDTA magnesium fertilizer (0.0001-0.0002), magnesium sulfate (0.0002-0.0008), EDTA iron fertilizer (0.0168-0.0766), EDTA zinc fertilizer (0.0001-0.0125), zinc sulfate (0.0001-0.0161), EDTA copper fertilizer (0.0054-0.0182), EDTA manganese fertilizer (0.0021-0.0294), manganese sulfate (0.0011-0.0177), boric acid (0.1054-0.1998) and ammonium sulfate (0.0001-0.0005).    USE - Composite fertilizer used for leafy crops (claimed).    ADVANTAGE - The composite fertilizer reduces mutual antagonism of microorganisms, and has high yield value.    DETAILED DESCRIPTION - Composite fertilizer comprises (in pts.wt.):ammonium dihydrogen phosphate (20-30), EDTA calcium fertilizer (0.0001-0.0004),EDTA magnesium fertilizer (0.0001-0.0002), magnesium sulfate (0.0002-0.0008), EDTA iron fertilizer (0.0168-0.0766), EDTA zinc fertilizer (0.0001-0.0125), zinc sulfate (0.0001-0.0161), EDTA copper fertilizer (0.0054-0.0182), EDTA manganese fertilizer (0.0021-0.0294), manganese sulfate (0.0011-0.0177), boric acid (0.1054-0.1998), ammonium sulfate (0.0001-0.0005), humic acid (0.2), Aloe juice (2), soybean protein (1), seaweed (0.4), Bacillus thuringiensis liquid, (43.2-48.6), Bacillus megaterium liquid (21.5-26.3), Bacillus mucilaginosus liquid (20.5-25.3) and Streptomyces jingyangensis liquid (2.8-4.2).
NOVELTY - Composite manure comprises (in wt.%): peat (25-35), biogas residue (25-35), plant ash (20-30), bacteria (0.2-0.5), boron-magnesium manure (2-5), zinc sulfate (2-5), ammonium molybdate (1-3), chaulmoogra (1-3), pomegranate bark (1-3), ningnanmycin (8%) (1-3), Bacillus subtilis (0.5-1.5), Verticillium (1-3) and choline chloride (60%) (0.5-1.5), and prepared by drying, crushing and mixing peat, biogas residue and plant ash to obtain mixture of powder (20-60 meshes). Bacteria with water is added to mixture and then tightly covered by plastic film layer.    USE - Composite manure used for treating watermelon continuous cropping wilt diseases (claimed).    ADVANTAGE - The composite manure improves quality and yield of watermelon.    DETAILED DESCRIPTION - Composite manure comprises (in wt.%): peat (25-35), biogas residue (25-35), plant ash (20-30), bacteria (0.2-0.5), boron-magnesium manure (2-5), zinc sulfate (2-5), ammonium molybdate (1-3), chaulmoogra (1-3), pomegranate bark (1-3), ningnanmycin (8%) (1-3), Bacillus subtilis (0.5-1.5), Verticillium (1-3) and choline chloride (60%) (0.5-1.5), and prepared by drying, crushing and mixing peat, biogas residue and plant ash to obtain mixture of powder (20-60 meshes). Bacteria with water is added to mixture and then tightly covered by plastic film layer for 10-15 days at 60-65 degrees C. The material is uncovered and turned and again covered by film for 10-15 days at 70-80 degrees C. The obtained material is dried, crushed and sieved through 20-60 meshes sieve. Chaulmoogra, pomegranates bark and thunder god vine are crushed and sieved to obtain 20-60 mesh powder. The obtained powder, fermented mixed material, boric acid, zinc sulfate, ammonium molybdate, Bacillus subtilis and Verticillium are mixed. Aqueous dilute choline chloride and ningnanmycin are added to obtained mixture using metering pump atomizer. The obtained mixture is molded and then extruded to obtain desired product.
NOVELTY - Method of preparing organic fertilizer, involves mixing straw with blue algae in a mass ratio of 1-5:10 to obtain mixed material, then adding biomass and microbial biomass inducing material, mixing uniformly, stacking and fermenting for 5-15 days to obtain solid organic fertilizer, mixing the semi-solid organic fertilizer, clay, biomass carbon ash and heavy metal ion chelating agent in a ratio of 1000-50-200:50-150:1-5, mixing and pelletizing the mixture to obtain the product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer has slow-release property, promotes soil fluffy and gas permeability, optimizes soil microelement, and is environmentally-friendly.
NOVELTY - Preparing hydrofluoroether, comprises adding alkaline compound solution containing fluorine-containing alcohol in solvent, then adding fluorinated olefin, heating and stirring to react for obtaining mixed solution, washing mixed solution using water, standing and layering, taking organic phase solution, and rectifying.    USE - The method is useful for preparing hydrofluoroether (claimed).    ADVANTAGE - The method is capable of easily and economically preparing the hydrofluoroether in an eco-friendly manner with high impurity.
NOVELTY - A 1,2-difluorobenzene-containing cyclopropanecarboxylic acid compound (I) is prepared by mixing (E)-3-(3,4-difluorophenyl)prop-2-en-1-ol, zinc-containing compound (Zn(C2H5)2), diiodomethane and (IR, 2R)-2-(3,4-difluorophenyl)cyclopropane as ligand in solvent, reacting at - 15-0 degrees C, adding chromate and orthoperiodic acid, and mixing.    USE - Method for preparing 1,2-difluorobenzene-containing cyclopropanecarboxylic acid compound (claimed).    ADVANTAGE - The method is simple and environment-friendly. It has high product yield.    DETAILED DESCRIPTION - A 1,2-difluorobenzene-containing cyclopropanecarboxylic acid compound of formula (I) is prepared by mixing (E)-3-(3,4-difluorophenyl)prop-2-en-1-ol, zinc-containing compound of formula (Zn(C2H5)2), diiodomethane and (IR, 2R)-2-(3,4-difluorophenyl)cyclopropane as ligand in solvent, reacting at - 15-0 degrees C, adding chromate and orthoperiodic acid, and mixing.
NOVELTY - Purifying oteracil potassium comprises adding oteracil potassium crude product into water and then dissolving to solid alkali and filtering to obtain filtrate and then adding to the organic solvent and stirring to obtain a solid precipitate and then dissolving in water to adjust a pH value to 6-7 using acid, then filtering and drying.    USE - The method is useful for purifying oteracil potassium (claimed).    ADVANTAGE - The method is capable of economically purifying oteracil potassium with high purity of more than 99.95% and yield of more than 80% in an eco-friendly manner.
NOVELTY - Mussaendoside U is prepared by taking Mussaenda pubescens coarse powder, adding 60-95% ethanol at weight ratio of 1:6-10, extracting for greater than or equal to 3 times, combining extracts, vacuum-concentrating, and recovering solvent; adding equal amounts of water and n-butanol, collecting organic layer, and vacuum-concentrating; dissolving in water, filtering, purifying using macroporous resin column, eluting with 0-95% ethanol, recovering ethanol, and evaporating; and dissolving in methanol, performing HPLC separation, detecting with UV light, evaporating, and concentrating.    USE - Method for preparing mussaendoside U (claimed).    ADVANTAGE - The process has simple technique, convenient operation, and high product yield and purity.
NOVELTY - Method for partial extraction of Paris polyphylla saponin involves crushing and drying P.polyphylla, and adding aqueous solution of ethanol, heating and reflux extracting the mixture, filtering the residues, concentrating the filtrate and drying at 50 degrees C, dissolving the dried filtrate using methanol solution, separating the dissolved mixture using silicon glue adsorption column, collecting the eluant, concentrating and drying the collected eluant, performing crystallization on the obtained mixture and re-crystallizing the obtained product.    USE - The method is useful for partial extraction of P.polyphylla saponin (claimed).    ADVANTAGE - The method enables to prepare product simply, rapidly, environmentally-friendly, and cost-effectively, and thus is suitable for preparation of fertilizer.    DETAILED DESCRIPTION - Method for partial extraction of Paris polyphylla saponin involves crushing P.polyphylla using 20 meshes sieve and drying the crushed P.polyphylla, adding aqueous solution of ethanol to the dried P.polyphylla, heating and reflux extracting the mixture at 60-80 degrees C, filtering the residues, concentrating the filtrate and drying at 50 degrees C, dissolving the dried filtrate using 60-80% methanol solution, separating the dissolved mixture using silicon glue adsorption column, collecting the eluant, concentrating and drying the collected eluant, again performing separation process using 35-40% aqueous ethanol solution on dried eluant by macroporous absorption resin X-5 separation, collecting the eluant, concentrating and drying the collected eluant, where the eluant is ethanol or ethanol aqueous solution, adding the concentrated liquid to 70% ethanol aqueous solution and completely dissolving the mixture at 40 degrees C, and then adding 2-4 times water, performing crystallization on the obtained mixture at low temperature overnight to obtain saponin crude product and re-crystallizing the obtained product.
NOVELTY - The system has a carbon making device box main portion (2) that is provided with spiral feeding mechanism (3). The inner wall of spiral feeding mechanism is provided with cooling cavity. The outer wall of spiral feeding mechanism (5) of cooling box main portion (4) is provided discharge hole which is connected with cooling device (7). A gas-making device is connected with carbon making device box main portion through pipeline. The pneuma fan (9), oil separation condenser (10) and gas storage tank (11) are provided in carbon making device.    USE - System for continuously utilizing biomass gas and carbon.    ADVANTAGE - The system has high production efficiency, convenient operation use and low production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous biomass gas and carbon utilization device.    Carbon making device box main portion (2)    Spiral feeding mechanisms (3,5)    Cooling box main portion (4)    Cooling device (7)    Pneuma fan (9)    Oil separation condenser (10)    Gas storage tank (11)
NOVELTY - The biomass double level reactor system comprises a main level reactor provided with a sand inlet and an air outlet, where the air inlet and a discharge hole are connected with a feeding port. The feeding port is provided with a sand falling tube, which is connected with a secondary reactor. An air outlet of the main reactor is connected with a gas-solid separator inlet. The discharge hole of the gas-solid separator is connected the feeding port of a sub-reactor. The sand falling tube of the secondary reactor is connected with the sand inlet of the main level reactor.    USE - Biomass double level reactor system.    ADVANTAGE - The biomass double level reactor system has reasonable in structure, improves biomass carbon combustion, and promotes smooth flow of the quartz sand slag circulation.    DETAILED DESCRIPTION - The biomass double level reactor system comprises a main level reactor provided with a sand inlet and an air outlet, where the air inlet and a discharge hole are connected with a feeding port. The feeding port is provided with a sand falling tube, which is connected with a secondary reactor. An air outlet of the main reactor is connected with a gas-solid separator inlet. The discharge hole of the gas-solid separator is connected the feeding port of a sub-reactor. The sand falling tube of the secondary reactor is connected with the sand inlet of the main level reactor. The secondary reactor is provided with two air inlets. The secondary reactor is arranged in an air reaction chamber. The main reactor and/or secondary reactor are connected with an air cap of an air supply device. An upper end of an air pipe is provided with an air outlet hole. The air supply device is provided with an air distribution plate. The sand falling tube is connected with a center part of the air distribution plate.
NOVELTY - A seaweed dry distillation kiln biomass oil system comprises feeding device (1), circulation fluidized bed combustion furnace (11), combustion furnace returning device (10), bed material spiral feeder (2), cyclone separator (12), first output end furnace, dust remover, steam turbine, mixer, biomass feeding bin, medium chamber, dry carrier storage tank, dry distillation furnace, non-condensable gas storage tank, liquid storage tank, and ash slag bin.    USE - Seaweed dry distillation kiln biomass oil system.    ADVANTAGE - The system has high burnout rate and improves combustion efficiency and performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of seaweed dry distillation kiln biomass oil system.    Feeding device (1)    Bed material spiral feeder (2)    Combustion furnace returning device (10)    Circulation fluidized bed combustion furnace (11)    Cyclone separator (12)
NOVELTY - The device has an oxygen supply unit that is provided with a liquid oxygen storing groove (1). The bottom portion of furnace portion (12) is provided with a furnace gate (11). A driving mechanism is connected with an outer wall of furnace portion. An inner wall of furnace portion is provided with a feeding device. An upper portion of furnace portion is provided with an air outlet (13), while bottom portion is provided with an ash outlet.    USE - Biomass-oxygen gasification device.    ADVANTAGE - The structure of biomass-oxygen gasification device can be simplified. The biomass-oxygen gasification device can be operated conveniently. The gasification conversion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass-oxygen gasification device.    Liquid oxygen storing groove (1)    Liquid oxygen gasifier (2)    Furnace gate (11)    Furnace portion (12)    Air outlet (13)
NOVELTY - The device has furnace shell (1) which is provided with gasification room and synthetic pneuma cooling room. The gasification room is divided into upper section gasification room (7) and lower section gasification room (4). The upper section gasification room top is provided with overhead synthetic pneuma outlet (8). The lower end gasification room is provided with throat section (16). The furnace bottom is provided with slag tank having slag discharging opening (15).    USE - Two section type biomass entrained flow bed gasification device.    ADVANTAGE - The two section type biomass entrained flow bed gasification device can process continuous gasification for pure oxygen gas with the intermittent gasification process compared with increased production rate in efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a two section type biomass entrained flow bed gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the two section type biomass entrained flow bed gasification device.    Furnace shell (1)    Lower section gasification room (4)    Upper section gasification room (7)    Overhead synthetic pneuma outlet (8)    Slag discharging opening (15)    Throat section (16)
NOVELTY - The apparatus comprises a mixer for mixing biomass carbon powder and inferior coal, a crusher connected with a screen, a coal conveyor, an outlet connected with the mixer and a biomass carbon powder feeding device, and a water supply device provided with the mixer. The outlet is connected with a coal pressing machine. The conveyor is installed between the crusher and the mixer, and includes a conveyor belt. The biomass carbon powder feeding device comprises a spiral feeding mechanism.    USE - The apparatus is useful for producing coal briquette (claimed).    ADVANTAGE - The apparatus has simple structure, effectively produces the coal briquette with reduced pollution and high yield, and is convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing coal briquette.
NOVELTY - A biomass granule forming line comprises press (3), crusher (5), selecting sieves (6, 7), drying device (12), cooling and packaging machine, main control system, conveyor, storage hopper, granulating machine (19), transfer warehouse and hoisting machine.    USE - Biomass granule forming line.    ADVANTAGE - The resource-saving production line has simple technique, improved production efficiency and yield, reduced production cost and energy consumption, and convenient use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for granulation of biomass comprising opening control system, conveying raw material to press, pressing, crushing, sieving, hoisting into transfer warehouse, drying, granulating, hoisting to packaging area, and packing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass granule forming line.    Press (3)    Crusher (5)    Selecting sieves (6, 7)    Drying device (12)    Granulating machine (19)
NOVELTY - A constant pressure biogas digester comprises bottomless biogas tank cover (2) set on open-top biogas tank (1) in which bottomless biogas tank cover is slightly smaller than biogas tank, bottomless biogas tank cover freely moves up and down according to the amount of biogas in biogas tank, and bottomless biogas cover contains manure outlet (3), guide pipe (4), and gas-guide pipe (5).    USE - A constant pressure biogas digester (claimed).    ADVANTAGE - Constant pressure biogas digester is lightweight, moveable, fire-proof, explosion-proof, safe and easy to use, and easy to maintain and saves cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of constant pressure biogas digester.    Biogass tank (1)    Bottomless biogas tank cover (2)    Manure outlet (3)    Guide pipe (4)    Gas-guide pipe (5)
NOVELTY - A Pseudoalteromonas sp. DSBS (CCTCC M2013652), is new.    USE - The Pseudoalteromonas sp. is useful for removing cadmium and inorganic phosphorus in sewage (claimed), and removing heavy metals.    ADVANTAGE - The Pseudoalteromonas sp. has cadmium resistance, can grow cadmium-containing wastewater, and reduces the cadmium toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing the Pseudoalteromonas sp., which involves inoculating the Pseudoalteromonas sp. in liquid Luria-Bertin (LB) culture medium at 25 degrees C for 24 hours to obtain the activated bacterial liquid, simulating water using 10% activated bacterial liquid at 25 degrees C by oscillating at 200 revolutions/minute for 24 hours, and centrifuging to obtain the Pseudoalteromonas sp..
NOVELTY - A garbage treatment process is performed by processing garbage in bioreactor to obtain aeration environment in upper layer, setting desired number of times and time needed for aeration treatment, performing aeration on upper layer (S201), stopping aeration when leachate pH detected in bioreactor is greater than or equal to 7 (S202), collecting bioreactor product and produced methane (S203), resetting aeration time and frequency when leachate pH detected is less than or equal to 7 (S204), restarting and executing upper layer aeration treatment, and performing garbage degradation treatment (S205).    USE - Garbage treatment process (claimed).    ADVANTAGE - The process improves degradation speed, aeration mode, and energy-saving effect, accelerates methanation process, shortens organic acid accumulation phenomenon, waste acidification stage, and preprocessing time, and reduces aeration frequency conversion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for garbage treatment system comprising time setting unit for obtaining upper aeration environment in bioreactor upper layer, aeration, detecting unit for finishing set of aeration process, collecting unit for detecting pH value of penetrating fluid, reset unit for resetting aeration time and frequency when pH is greater than or equal to 7, processing unit for restarting upper aeration process, and unit for garbage degradation treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of garbage treatment. (Drawing includes non-English language text).    Garbage processing and upper layer aeration treatment (S201)    Stopping aeration and detecting pH value (S202)    Collecting bioreactor product and methane produced (S203)    Resetting aeration time and number of aeration process (S204)    Restarting aeration and performing garbage degradation treatment (S205)
NOVELTY - Method of preprocessing straw type biomass by anaerobic digestion, involves harvesting straw, naturally drying until the water content is 35-40%, adding fermentation inhibitor, performing acidification and chemical treatment, sealing the straw bundle using plastic thin film for 20-30 days, mixing the straw and inoculation sludge in a weight ratio of 1:10, and performing anaerobic digestion for 15-20 days.    USE - The method is useful for preprocessing straw type biomass by anaerobic digestion (claimed).    ADVANTAGE - The method is cost-effective and increases the yield of product.
NOVELTY - Producing ethanol and methane using straw, comprises (i) pre-processing straw, (ii) adding 0.1% dilute sulfuric acid in preprocessed straw, and mixing, cooking at 121-130 degrees C for 120-150 minutes, (iii) regulating the pH to 6.5-7.5, then inoculating yeast to the material, fermenting for 12-24 hours at 35 degrees C under anoxic environment, then carrying out ethanol distillation after completing fermentation, and (iv) adding remaining ethanol in mash liquid and inoculating anaerobic bacteria to continue the fermentation production.    USE - The method is useful for producing ethanol and methane using straw (claimed).    ADVANTAGE - The method improves the utilization rate of straw; is environmentally friendly and economical; and is safe and reliable.
NOVELTY - Method for preparing concentrated paste of tartary buckwheat, involves (a) cleaning and removing impurities of tartary buckwheat, adding water to the tartary buckwheat, boiling the mixture, and filtering the mixture to obtain filtrate, and (b) concentrating the filtrate to obtain paste.    USE - The method is useful for preparing concentrated paste of tartary buckwheat (claimed) which is used for reducing weight, blood pressure, blood fat, and blood sugar.    ADVANTAGE - The method is simple to perform, cost-effective, environmentally-friendly and easy for industrial production, and maintains original nutrition, color and flavor of tartary buckwheat. The paste provides good mouthfeel, is harmless and suitable for long-term drinking, has high nutritive value, and is suitable for patient with diabetes.
NOVELTY - This utility new type relates to a one industrial sewage processing system is mainly composed of industrial sewage pipeline, sewage treatment tank, a stirrer, a detection device and air blower, said industrial sewage pipeline is arranged on the left side of sewage tank, said device comprise a contamination detector and liquid level detector, a sewage treatment tank is provided with the right side microorganism pipeline, the lower sewage treatment tank is provided with a water discharging pipeline, said upper industrial sewage pipeline, the aerobic microorganism pipeline and drainage pipeline are provided with an electromagnetic valve, said air blower is set on the lower part of sewage treatment tank. The system has simple structure, through air blower is sewage treatment tank provide in air, the aerobic microorganism of reaction condition, improves sewage treatment efficiency.
NOVELTY - A one kitchen garbage production of marsh gas desulphurization device, include a purification tank, the purification tank set with safety device is connected, safety device and non-pressure dry-type marsh gas storage tank is connected, water replenishing tube safety device to provide supplemental, safety device through pipeline with the biological desulfurizing tower is connected between the safety device with the biological desulfurizing tower of upper pipeline is connected with a air pump, circulation liquid in the circulation pump of the biological desulfurizing tower is sent to the biological desulfurizing tower upper part circulation spray, marsh gas output port of the biological desulfurizing tower through pipeline is connected with the air inlet of the dry tower is connected with use of dry-type desulfurizing device connected with the marsh gas through the pipeline of the non-pressure dry-type marsh gas tank by tower lower part input, microorganism decomposing the hydrogen sulphide, air supplied to the injection pump the biological desulfurizing tower in air, to maintain the oxygen concentration of the biological desulphurization tower processing rear of marsh gas directly entering into in dry desulfuration tower and a desulphurization treatment, it has simple structure, low operation cost and high safety of.
NOVELTY - There is no power stirring and fermenting device one of a kitchen garbage, include a solubilized tank, solubilized tank through screw pump is connected with the fermentation tank, waste liquid by the waste liquid pump and sewage treatment device is connected, and it further set with electromagnetic flow meter between the screw pump and the fermentation tank, the fermentation tank inner cavity upper part is upper part room, the lower part is the lower room, a fermentation tank centre set with a stirring shaft, the stirring shaft is set with stirring blade, one set with center guide tube and the lower part room in the upper room, the upper room set with balance valve, set with biogas slurry overflow tube on the upper part of the lower room, the fermentation tank is set with lower part discharging port from the solubilized tank out of slurry screw pump to the fermentation tank, fermenting in biogas generated in the lower room, in tank fermentation liquid along the centre pipe upper part room, the upper room of the fermentation liquid by gravity low, the purpose of the centre pipe to move downwards to realize the fermentation tank liquid stirring, it can save power, it is not easy to produce the characteristics of scum and incrustation.
NOVELTY - The system has a reactor (104) including a molten pool containing sodium carbonate. A softened water supply (200) is in communication with the reactor. Supply of vacuum residuum is in communication with the reactor. A control system is associated with the water supply to maintain the water supply at desired temperature, desired pressure and desired flow rate. A first flow path is provided between the supply of softened water and the reactor. A second flow path is provided between the supply of vacuum residuum and the reactor, where the flow paths accommodate mixing of water.    USE - System for producing syngas and fuel gas e.g. hydrogen and methane.    ADVANTAGE - The system can conserve the water usage and limit loss of sodium from the system, thus improving energy extraction efforts, and providing energy in a more efficient, abundant and environmental friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for producing syngas and fuel gasses.    Alkaline metal reforming system (100)    Reactor (104)    Softened water supply (200)    Water feed (250)    Hydrocarbon source (300)    Hydrocarbon feed (350)
NOVELTY - The plant has a gasifier kettle (1) comprising an air inlet aperture (7) and a product gas suction. A condensation dryer (10) reduces moisture of atmosphere of the gasifier kettle. The gasifier kettle is formed as a fixed bed gasifier kettle. The condensation dryer comprises a drying space (4), which surrounds an upper section of the gasifier kettle, and a coolant spacer (11) surrounding an upper inner space portion of the gasifier kettle. An air inlet pipe (3) projects into interior of the gasifier vessel through the air inlet aperture.    USE - Wood gasification plant i.e. direct current gasifier, for electricity generation in a gas-fired power station.    ADVANTAGE - The condensation dryer reduces moisture of the atmosphere of the gasifier kettle so as to warm the kettle up to 1000 degree Celsius in a reaction zone of the gasifier kettle, so that efficiency of the plant can be increased by separating water vapor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a wood-distilling apparatus plant.    Gasifier kettle (1)    Air inlet pipe (3)    Drying space (4)    Air inlet aperture (7)    Condensation dryer (10)    Coolant spacer (11)
NOVELTY - Burning substance or burning agent comprises either hay and vegetable oil that are pressed together under the influence of heat and then divided into pieces after cooling, or hay and vegetable oil that are chopped and mixed together in a ratio of 1:1.    USE - The burning substance or burning agent is useful for generating heat and power (claimed) that is useful in apartments, houses and large combustion plants.
NOVELTY - Fire substance or fire agent for generating heat and energy, comprises hay and stiorin (hydrogenated vegetable oil) which are compressed under the heat and then cut into pieces after cooling, or the hay and stiorin are mixed in a specified ratio of 1:1.    USE - The fire substance or fire agent is useful for generating heat and energy (claimed) in large combustion plants.
NOVELTY - Burning substance or burning agent comprises either tree leaves and vegetable oil that are pressed together under the influence of heat and then divided into pieces after cooling, or tree leaves and vegetable oil that are chopped and mixed together in a ratio of 1:1.    USE - The burning substance or burning agent is useful for generating heat and power (claimed) that is useful in apartments, houses and large combustion plants.
NOVELTY - Clarifying a gas stream containing tar-like components, comprises contacting the gas with a liquid organic aryl polysiloxane.    USE - The process is useful for clarifying a gas stream containing tar-like components, where the gas comprises at least one of hydrogen, carbon monoxide, carbon dioxide, methane or nitrogen (all claimed).    ADVANTAGE - The process: can be operated below the water dew point; and provides clean and stable scrubbing liquid.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of a gas cleaning system.    Absorption unit (32)    Heater (43)    Outlet (51)    Cooler (56)    Pump (58)
NOVELTY - The method involves formatting electrolyzes tap water using bowl (1) made from unglazed pottery as a diaphragm between anode electrode (5) and cathode electrode (3). Inside of bowl is filled with silica gel, and cathode electrode is installed in center portion, and anode electrodes are made of by gold, platinum, or carbon installed in outer side of bowl. A water head is obtained to a cathode side by the action of electroendosmosis material, liquid level goes up, and liquid overflows outer side from the edge of bowl when direct current is applied between anode and cathode.    USE - Processing method for improving water permeance rate of bowl made from unglazed pottery, for prevention of fluidization phenomenon of sand grain during earthquake and for collection of hydrogen gas used during manufacturing of fuel cell.    ADVANTAGE - Water permeance rate of porous sheet used as electro-endosmosis material for electroosmotic flow pumps made into the subject can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus used for processing bowl made from unglazed pottery. (Drawing includes non-English language text)    Bowl (1)    Silica gel filled layer (2)    Cathode electrode (3)    Cathode side liquid level (4)    Anode electrode (5)
NOVELTY - A solid fuel comprises a baked biomass and a binder.    USE - Solid fuel is used for manufacture of composite fuel (claimed) used as biomass fuel for boiler and cement kiln.    ADVANTAGE - The solid fuel has excellent moldability and grindability, and provides composite fuel having excellent combustion stability. In manufacture process of composite fuel, the biodegradable materials such as paper sludge containing fiber and wood chips are effectively used.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the solid fuel, which involves baking biomass, mixing binder with the baked biomass, and molding the baked biomass with binder; and    (2) manufacture of composite fuel, which involves mixing the solid fuel and coal, and pulverizing the mixed solid fuel and coal.
NOVELTY - This new type utility claims one a sludge dewatering device, the device include orderly connected pipeline of the sludge collecting groove, pre-dehydrating device, a transition tank, the high speed rotating body of mixing reactor, pipeline reactor and strong dehydration device, the device further include medicine tank, the medicine tank and the mixing reactor pipeline connected. This utility new type is more than 8% and adding medicine, greatly reduces drug amount with the loss of water, saves medicine dosage is more than 30%. Low in the same medicine dosage, can improve the sludge dryness is more than 5%. Reducing the residual medicine for environment of two secondary pollution, but also reduces the residual medicine group for damage of dehydration device. The application shows that, this utility new type for dehydration rate of the paper mill sludge can reach more than 55%.
NOVELTY - A biogas utilization system (201A) comprises a compression unit (213) to pressurize biogas, separation-membrane-type dehumidifying apparatus for dehumidifying the pressure-risen biogas, and gas utilization unit (230) to utilize the dry biogas emitted with the separation-membrane-type dehumidifying apparatus. The biogas pressure-risen by compression unit is supplied to the gas utilization unit without increase/decrease of operation of pressure. The dew point of biogas is reduced by 5 degrees C or more with the separation-membrane-type dehumidifying apparatus.    USE - Biogas utilization system is used for dehumidification of biogas (claimed) used as fuel.    ADVANTAGE - The biogas utilization system enables efficient dehumidification of biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas dehumidification method, which involves pressurizing biogas, dehumidifying pressure-risen biogas with separation-membrane-type dehumidifying apparatus, and supplying dry biogas emitted to gas utilization unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas utilization system. (Drawing includes non-English language text)    Biogas utilization system (201A)    Biogas generation source (203)    Elimination apparatus (205)    Compression unit (213)    Cooler (215)    Gas utilization unit (230)
NOVELTY - Reducing (M1) coke deposition on catalyst, comprises: (a) subjecting biomass to torrefaction; (b) pyrolyzing torrefaction-treated biomass, thus generating heated pyrolysis oil vapor; (c) esterifying heated pyrolysis oil vapor or their components, thus providing heated pyrolysis oil vapor having reduced acid and aldehyde content compared to heated pyrolysis oil vapor not esterified; and (d) cracking esterified heated pyrolysis oil vapor, thus generating bio-oil.    USE - The method is useful for reducing coke deposition on catalyst used in cracking of pyrolysis oil vapor and generating a bio-oil product (claimed).    ADVANTAGE - The method reduces yields of reactor char, catalyst coke, and catalyst tar.    DETAILED DESCRIPTION - Reducing (M1) coke deposition on a catalyst used in cracking of a pyrolysis oil vapor, comprises: (a) subjecting a biomass to torrefaction; (b) pyrolyzing the torrefaction-treated biomass, thus generating a heated pyrolysis oil vapor; (c) esterifying the heated pyrolysis oil vapor or their components, thus providing a heated pyrolysis oil vapor having a reduced acid and aldehyde content compared to a heated pyrolysis oil vapor not esterified; and (d) cracking the esterified heated pyrolysis oil vapor, thus generating a bio-oil, where the cracking step comprises contacting the heated pyrolysis oil vapor with a second catalyst, and the catalyst accumulates a reduced coke deposition compared to when the heated pyrolysis oil vapor is generated from a biomass not treated with torrefaction. INDEPENDENT CLAIMS are also included for:    (1) generating (M2) a bio-oil from a biomass, comprising (a)-(d) as above per se;    (2) a bio-oil product generated by the process (M2); and    (3) a system for generating a pyrolysis bio-oil product, comprising a torrefaction unit, a pyrolysis unit, a catalytic esterification unit, a catalytic cracking unit, and optionally a condensation unit.
NOVELTY - Solid fuel comprises 100 pts. wt. of animal waste, 2-5 pts. wt. of molding material, 5-20 pts. wt. of food waste, and 5-10 pts. wt. of combustible powder. The molding material is clay. The food waste and the animal waste are collected from the restaurant.    USE - The solid fuel is useful as a heating source in stove, boilers, incinerators, and power plants.    ADVANTAGE - The solid fuel can be prepared by recycling thrown away resources from the restaurants, so that environmental pollution by processing of waste can be prevented, resources can be saved and production of alternative energy can be enabled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing solid fuel comprising: collecting food waste and animal waste from the restaurant; mixing 100 pts. wt. of animal waste with 2-5 pts. wt. of molding material, 5-20 pts. wt. of food waste and 5-10 pts. wt. of combustible powder; molding the blended mixture; and cooling the molded article.
NOVELTY - A catalyzer sheet (10) consists of a mesh-type or perforated sheet-type supporting structure (10a) at least partially provided with a large surface area coating having catalytic activity with respect to hydrogen evolution reaction.    USE - Catalyzer sheet is used for hydrogen generator device for power supply system (all claimed).    ADVANTAGE - The catalyzer sheet provides economical, efficient and improved hydrogen generator device.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen generator device, which consists of a vessel having gas outlet, hydrogen-developing components which have portions made from magnesium, zinc or aluminum, or their alloys, the catalyzer sheet, and alkaline or saline aqueous electrolyte; and    (2) power supply system, the hydrogen generator device, in which the steam outlet is connected through steam connection control unit, preferably connected to steam machine, and hydrogen outlet is connected through hydrogen connection control unit, preferably connected to hydrogen storing unit, fuel cell and/or hydrogen driven machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view the catalyzer sheet.    Catalyzer sheet (10)    Supporting structure (10a)    Polymer material (10b)    Openings (10d)
NOVELTY - A reinforced soil water fertilizer comprises cation exchange resin, sea buckthorn, Chinese trumpet creeper, chicken manure, powdered rock phosphate, photosynthetic bacteria, ammonium sulfate and fermentation bacteria.    USE - Reinforced soil water fertilizer.    ADVANTAGE - The method is simple. The fertilizer reduces salt content of soil, enhances soil activity of microorganism and enzyme, and promotes plant root system growth. It has improved saline-alkali effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of reinforced soil water fertilizer comprising mixing sea buckthorn, Chinese trumpet creeper, chicken manure and powdered rock phosphate, stirring, adding fermentation bacteria, composting at 30-50 cm height, covering with plastic film cover, fermenting for 10-12 days, adding cation exchange resin, photosynthetic bacteria and ammonium sulfate, adding water until 63-65 vol.% water content, extruding, and drying.
NOVELTY - This utility new type relates to machinery field, especially relates to a one without energy consumption type domestic sewage treatment device. Comprises processing tank, a processing tank water inlet part comprises one end of the water outlet part and the other end of the said water inlet part is a tank bottom further comprises purification part, the bottom of said purification part is set with an aeration device, the aeration device comprises aeration tube a, up with aeration head, the aeration head with an outlet of said more than one, said aeration tube connecting pneuma source. A purification part is divided into two parts, said two part is of separated structure, upper wall is provided with a water passing hole. Beneficial effect of this utility new type sewage purification processor can fermentative continuous water inlet and drainage gap, and can realize good denitrification effect for single tank, automatic control system is simplified, reduces the investment, through front end continuous water inlet and continuous aeration, rear section intermittently draining, interim aeration can be valid denitrification.
NOVELTY - This new type utility claims for manure sewage anaerobic processing of the front end deoxidization device, include excrement sewage temporary storage tank, a metering pump, a oxygen machine, pump, an anaerobic pool, excrement sewage temporary storage tank through metering pump and the oxygen removing machine connecting, removing oxygen machine through pump and the anaerobic tank connect. Wherein the oxygen removing machine comprise the tank body, heating and heat preservation device, stirrer and water outlet, heating heat preservation device to make oxygen removing machine inside temperature is maintained at 28 degrees centigrade to 33 degrees centigrade, stirring speed of stirrer is 80 to 120 r/min, the tank body set with a water outlet, the water outlet is higher than the tank bottom end of one section set distance, the oxygen removing machine is stored with oxygen removing and bacteria,, removing oxygen and with bacteria is Saccharomyces cerevisiae. This utility new type can finish the quantitative excrement sewage deoxidation processing in small space, and stable working.
NOVELTY - This new type utility claims one a hydrogen power device, wherein the device comprise electrolytic groove, water, the water tank and the pneuma tank, connected with a control device, forming one hydrogen group of power device, consumable material is water, electrolytic groove comprise multi-electrolysis unit, the electrolysis unit multi-arranged in parallel, each electrolytic unit comprise six mutually overlapped of stainless steel sheet and the shell of stainless steel sheet, two adjacent stainless steel sheet is provided with insulation, insulation seal pad six stainless steel sheets form one group of electrolytic groove, said six stainless steel sheet in two pieces of stainless steel sheet is arranged on the outer side end and a tail sheet, the upper end is provided with two water tube through hole and post head, and the other one sheet to be the outer side tail sheet is binding post, the other four stainless steel sheet corresponding water tube position are provided with a through hole, forming water flow channel. This utility new type by six mutually overlapped stainless steel sheet obtain working of high efficiency of electrolytic groove and prolongs the use life of the device and the superimposed combination to save space, the gas amount is large, the product mass.
NOVELTY - A Potash fertilizer pelleting device comprises rack (1), granulating bucket (2), water storage tank (4), atomizer (3), conduit, water pump (6) and pressurizing pump.    USE - Fertilizer pelleting device.    ADVANTAGE - The device greatly reduces working temperature, avoids cooling step, saves cost, and preserves fertilizer biological activity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fertilizer pelleting device.    Rack (1)    Granulating bucket (2)    Atomizer (3)    Water storage tank (4)    Water pump (6)
NOVELTY - Treatment of a domestic garbage comprises conveying a domestic garbage in a stirring tank, injecting water, stirring, and treating for 0.5-1 hour to obtain a slurry having a moisture content of 80-90%; processing the slurry in an anaerobic digestion tank, passing through a biogas boiler to produce high temperature steam, and pre-heating digestion residue at 40-70 degrees C for 1-3 hours; carrying out hydrothermal carbonization at 180-350 degrees C for 0.5-6 hours; and drying.    USE - Method for the treatment of a domestic garbage (claimed).    ADVANTAGE - The method is inexpensive, and is environment-friendly.
NOVELTY - Preparation of a biofertilizer comprises mixing 40-50% lignite crushed to 50 meshes, 20-25% corn straw, and 10-15% cotton straw; adjusting moisture content to 30-50%; adding 10% Davidiella tassiana (CGMCC 7440) and Streptomyces griseoplanus (CGMCC 8194), and uniformly stirring; and adjusting material pH value at 6.5-7.5, fermenting at 28 degrees C for 5-7 days, drying, and crushing.    USE - Method for the preparation of a biofertilizer used for producing rice and cotton (claimed).
NOVELTY - A vegetable soil-less growth media preparation involves collecting organic waste alcohol residue, crop straw and coconut husk, drying, crushing, performing water treatment, collecting permafrost, marsh mud, carbonized rice husk ash, vermiculite or perlite, mixing, adding straw powder and coconut shell powder, adjusting pH value, soil electrical conductivity, carbon to nitrogen ratio, and moisture, composting using solar panel, composting, adding leavening agents and materials, mixing, adding fermentation bacteria, adding water, drying coconut powder, crushing, adding alcohol and straw.    USE - Method for preparing vegetable soil-less growth media (claimed).    ADVANTAGE - The growing media is low-cost.    DETAILED DESCRIPTION - A vegetable soil-less growth media is prepared by collecting organic waste alcohol residue, crop straw and coconut husk as raw materials, drying, crushing, performing water treatment, collecting 0.5-1.5 pts. wt. permafrost, 0.5-1.0 pt. wt. marsh mud, 0.5 pt. wt. carbonized rice husk ash, 1.5-2 pts. wt. vermiculite or perlite, mixing, adding 3-5 pts. wt. straw powder and 2-3 pts. wt. coconut shell powder, adjusting pH value, soil electrical conductivity, carbon to nitrogen ratio, and moisture, compositing using solar panel having height of 0.8-1.2 m, length of 5-50 m and width of 1-3 m, composting for 2-3 days, adding leavening agents and materials, mixing, adding fermentation bacteria twice a day, turning once every other day to control temperature at less than or equal to 55 degrees C, adding water to moisture content 55-65%, drying coconut powder, crushing, adding alcohol and straw, sifting, and adjusting vegetable soil-less cultivation substrate moisture to less than or equal to 45%, dry organic matter content to greater than or equal to 40%, total nutrient content to 2.5-3% at dry basis, pH value to 5.5-7, soil electrical conductivity to less than or equal to 2.5 and particle size to less than or equal to 5 mm.
NOVELTY - A fertilizer composition comprises 45-50 pts. wt. straw, 23-26 pts. wt. poplar branches, 12-15 pts. wt. willow leaves, 30-34 pts. wt. cane stalks, 10-12 pts. wt. soybean hulls, 30-34 pts. wt. brewer, 30-34 pts. wt. slow-release urea, 12-14 pts. wt. ammonium sulfate, 23-25 pts. wt. potassium dihydrogen phosphate, 12-15 pts. wt. potassium chloride, 6-8 pts. wt. monoammonium phosphate, 3-4 pts. wt. zinc sulfate, 2-3 pts. wt. polyacrylamide, 3-4 pts. wt. microbial agent, 4-6 pts. wt. film coating agent and balance water.    USE - Fertilizer composition.    ADVANTAGE - The method is simple and easy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of fertilizer composition comprising drying straw, poplar branches, willow leaves, cane stalks and soybean hulls, grinding, standing, mixing slow-release urea, ammonium sulfate, potassium dihydrogen phosphate, potassium chloride and monoammonium phosphate, adding water, stirring, adding zinc sulfate and polyacrylamide, mixing, standing, adding microbial agent, stirring at room temperature, adding remaining raw materials, fermenting for 25-35 days, turning once every 5-6 days, drying, and granulating; (2) composition of film coating comprising 50-60 pts. wt. urethane acrylate, 20-30 pts. wt. ethyl acrylate, 20-22 pts. wt. chlorinated paraffin, 1-2 pts. wt. crosslinking agent, 0.1-0.2 pt. wt. nanocarbon materials, 1-2 pts. wt. barley rice powder and 3-4 pts. wt. glycol; and (3) preparation of film coating comprising mixing all raw materials, grinding, and molding.
NOVELTY - An organic liquid fertilizer comprises 600-700 pts. wt. enzymatic supernatant, 6-9 pts. wt. chitosan, 50-100 pts. wt. nitrogen fertilizer, 40-50 pts. wt. phosphate fertilizer, 50-100 pts. wt. potassium fertilizer, 15-30 pts. wt. trace element and 1-2 pts. wt. natural surfactant.    USE - Organic liquid fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of enzymatic supernatant comprising drying lees to moisture content of 25%, grinding to 80 mesh, adding water at weight ratio of 1:6, adjusting pH value to 8-10, adding alkaline protease, enzymatically reacting at 45 degrees C for 50 minutes; and    (2) preparation of organic liquid fertilizer comprising mixing enzymatic supernatant, chitosan and trace elements, stirring for 5-10 minutes, nitrogen fertilizer, phosphate fertilizer, potassium fertilizer and natural surfactant, stirring for 10-15 minutes, and packaging.
NOVELTY - A fertilizer enhancing agent comprises 55-60 pts. wt. polypeptide, 9 pts. wt. liquid glucose, 1.5 pts. wt. propionaldehyde, 0.5 pt. wt. triethanolamine, 10-15 pts wt. controlled release agent, 10-15 pts. wt. trace elements, 20 pts. wt. softening agent, 3 pts. wt. polyacrylamide, 3 pts. wt. modified starch, 5 pts. wt. polyvinyl alcohol, 6 pts. wt. phosphorus and potassium bacteria, 5 pts. wt. humic acid, 5 pts. wt. potassium, 5 pts. wt. complex enzyme and 3 pts. wt. complex strains.    USE - Fertilizer enhancing agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer enhancing agent comprising mixing polypeptide and liquid glucose, heating to 50-65 degrees C, stirring, adding complex enzyme, reacting for 1 hour, heating to 80-85 degrees C, adding propionaldehyde and triethanolamine, reacting for 1 hour, adding controlled release agent, trace elements and demineralized water, heating to 95-10o degrees C, stirring, reacting for 2 hours, cooling to 65 degrees C, adding polyacrylamide, modified starch and polyvinyl alcohol, stirring for 30 minutes, heating to 85-95 degrees C, standing for 0.5 hour, adding humic acid and potassium, stirring for 30 minutes, cooling to 40-50 degrees C, adding enzyme, stirring, adding phosphorus and potassium bacteria, stirring for 1 hour, cooling to room temperature, stirring for 30 minutes, adding complex enzyme and complex strains, and mixing.
NOVELTY - This utility new type belongs to the field of agricultural technology field, especially relates to a soil improvement for producing a one system, include fermentation area, breeding area, drying area, a fermenting area include stirrer, fermentation chamber, the fermentation chamber is provided with a fermentation, fermentation chamber connected with a liquid storage tank, a fermenting chamber and liquid storage tank is provided with a and topping-up pump, a cultivation area include cultivation bed, a cultivation bed of layer and is provided with a water inlet tube, side surface of said cultivation bed is provided with a temperature sensor, the PH tester, a cultivation bed height is 1 m and the width is 0.8m;, said drying section include crusher, drying platform, a combined drying platform is provided with a heating rod, side surface of said drying platform is provided with a temperature sensor, a humidity sensor, a drying platform of is set on, this utility new type device, operation is simple and has no pollution in production, without adding any chemical substance and for environment;
NOVELTY - This utility new type agricultural heat preservation device, especially relates to compost using heat preservation device. One a compost heat preservation device, comprise first insulating film, second insulating film, wherein the first insulating film and second insulating film seal connecting, forming double layer heat-preserving film, a first insulating film and the second insulating film set with air cavity, set with reinforcing rib in said inflation cavity, first heat preservation of film and a second insulating film with the reinforcing rib fixed connect, set with vent hole on the upper reinforcing rib, set with upper charging port on the double layer insulating film of a. This utility new type can valid improve the outer layer of compost temperature, so that the outer layer and the center as compost completely, so as to shorten compost period, saves operation of turning cost; or with other vent means match use to completely replace the turning operation and improves the compost layer temperature also is good for reducing organic matter consumption, improves fertilizer effect.
NOVELTY - This utility new type relates to fertilizer production field, a one is a movable compost device, movable compost device comprise a movable main control box, monitoring unit and cover film, a main control box set with control unit and control unit and the connecting of the fan, the main control box is further set with a ventilation pipeline, a ventilating pipeline and a fan, a monitoring unit and a control unit connect. This utility new type using movable body device is not limited, it can according to need of compost field be moved at any time, process is simple, it does not need the compost factory, saves the investment of device operation is simple, basically no maintenance, low maintenance cost, and it further can according to temperature and oxygen content in each part of stack, real-time dynamic control for oxygen, ' consumption is low, the processing efficiency is high.
NOVELTY - This utility new type claims a biogas purification controller of one gas filter structure, comprise a shell, a shell is provided with a desulphurization chamber, a connecting, marsh gas outlet tube sulphur upper cavity, and a gas intake tube of marsh gas control valve, wherein a marsh gas outlet tube, gas inlet tube, pneuma pressure measuring device are provided with a filter screen. This utility new type through using a filter net is set in the marsh gas outlet tube, gas inlet tube, pneuma pressure measuring device of the technical solution to prevent desulfurizer granule or other dust entering into to a marsh gas inlet tube and gas outlet tube, pneuma pressure measuring device. Improves the use life of whole device.
NOVELTY - The invention claims a bio-diesel one preparation device, container for methanol alkali catalyst, a feeding device for adding waste oil and acid catalyst, a reaction in the reaction device, the acid catalyst of the pre-esterification reaction, acid catalysis and base catalysis reaction integrated in one of the reaction device in can be suitable for different acid value and water content of waste oil.
NOVELTY - This utility new type claims a one anaerobic fermentation tank, belonging to the field of environmental device technology field. It comprise a tank body, a biogas outlet tube and feeding tube, further comprise a stirring shaft, one end of the stirring shaft connecting to the outer wall of the tank body of said power device, and the other end extends into the inside of the tank body and a support base through connecting at the bottom of said upper tank body, the stirring shaft is fixedly connected with a upper at least one group of stirring paddle. This utility new type has the advantages of producing high efficiency, completely fermenting, resource utilization rate high.
NOVELTY - This new type utility claims one shape of a dry fermentation marsh gas generator aims to the country, mountainous area, area herdsman family provide a one economical and practical, operation is simple, it does not need power supply support of marsh gas generator. The generator shell and shape include heating device, wherein the shell body is one middle insulating layer of a double-layer structure, is equipped with a feed port, a discharge port, a gas transmission tube, pressure meter and temperature meter, wherein feeding hole and discharge hole on the upper shell of the upper using bayonet structure, the seal property is good. fireplace heating device is one combustion furnace, the upper centre position of the shell, passes through the top of the shell is installed on the upper shell, and the upper part is the cover, the combustion furnace is provided with furnace pad, pad lower part passes through the furnace shell is equipped with an ash ash upper is equipped with ash outlet cover is further equipped with marsh gas combustor according to the upper part of the furnace. This utility new type widely used in countryside, mountainous area, herdsman area, provide a one manufacturing beautiful low cost of clean energy.
NOVELTY - A one agricultural processing and domestic waste treatment device, comprise one shell, said shell is a sealed container in the shell arranged with four layer, comprising up to a low water pressure box layer, pneuma layer, filtering layer and fermenting layer, discharging the water pressure of the lower layer storing tank of waste water, water pressure tank layer upper part set with water outlet, the water level over time by the water outlet through the water outlet pipeline for exhausting automatically, water pressure tank lower part layer with pneuma layer connected with the water return pipe, water return pipe of the water pressure tank layer pneuma layer connected with the storage, the storage pneuma layer upper layer is produced by biogas upper float pneuma pneuma layer storage by storage of marsh gas, and the lower layer is the water pressure tank to the connected layer of waste water, set with gas outlet on the top part of the pneuma layer, methane fermentation layer generated through gas outlet conveying out, one of feeding pipeline is directly connected with the feed opening of the ground in the fermentation layer and through, through feeding pipeline into the fermentation layer.
NOVELTY - This utility new type relates to one large biomass pool of a positive-negative pressure protector, belonging to the marsh gas engineering field. One large and medium-sized methane tank of a positive-negative pressure protector, include marsh gas tank and tank connected with the marsh gas of positive and negative pressure protector, a positive and negative pressure protector comprise middle unsealed of inverted concave type container set in the container of inverted U type clapboard, said container is divided into four areas, the top end of container and the bottom of baffle plate with a certain gap, the top end of the clapboard and the container of the bottom there is a certain gap, is convenient to flow of water, bottom end of container with the water injection bucket connected. This utility new type has advantages as follows: a high safety, high degree of automation control.
NOVELTY - This utility new type claims a multifunctional hydrogen-oxygen separating one generator, belonging to oxygen and hydrogen separating device field. The generator at least comprise the base module, the hydrogen and oxygen separating module, a shell, an upper cover module, said upper module base is provided with a hydrogen and oxygen separating module, a shell, a shell top surface is provided with an upper cover module. Is set through hydrogen and oxygen of each channel and collecting pneuma room, a hydrogen and oxygen extraction, through the related pipes in car, ship engine air inlet, combustion of mixed gas in increasing power combustion value, and solves the problem that the use in oxygen in the tempering of the problem, separating the oxygen can through the related pipes of the vehicle, an air conditioner or the cab of ship, the driver and passenger oxygen suction, and separating the oxygen of the air conditioner in oxygen for people. This utility new type is convenient to carry, simple and convenient installation, electrolysis of oxygen can produce immunizing, using is convenient to use oxygen enriching, oxygen therapy and oxygen health care, especially suitable for high altitude, such as mountain hypoxia area use.
NOVELTY - This new type utility claims one hydrogen and oxygen and a water electrolysis device of carbon machine, comprise two closed end of corrugated pipe, a corrugated pipe upper end of upper end surface set with liquid inlet tube, an air outlet tube and two of the electrode column, a corrugated pipe set with electrolytic device, electrolytic device is a multi-electrode of sheet tightly overlapped, said electrode sheets include one block plastic plate, middle part of plastic plate rear hollow embedded metal plate, upper end of said plastic plate set with several first groove, the first groove connecting to the metal plate, a plastic plate of lower end set with connected between said connected hole and the metal plate set with a plurality of second groove, connected through hole groove and the second metal plate connected, the electrolytic device of metal plate in the outermost two of the sheet a is connected with the two electrode of the electrode column upper end end face of the corrugated pipe. This utility new type of electrolysis device of multi-electrode of sheet tightly overlapped, of metal plate in the electrolytic device only through first groove and second groove is connected with the electrolyte, the structure is simple, the cost is low, the anti-explosion property.
NOVELTY - This utility new type claims a multifunctional one hydrogen water oxygen machine, belonging to the water machine field. At least comprise the base module, the hydrogen and oxygen separating module, the shell module, water dispenser module, storage module, said upper module base is provided with a hydrogen and oxygen separating module, a shell module, a module outer shell upper part is provided with a drinking water machine module, a water module upper part is provided with a water storage module. Through hydrogen-oxygen separating module for of water in electrolytic room a, anode electrolytic produce of oxygen through the oxygen output tube of water fountain module is for supplying oxygen, or the air conditioner in improve the indoor air environment, cathode electrolytic produce of hydrogen entering into water module, people provide hydrogenated drinking water, removing free radical, balancing human pH value, improve the micro-circulation of human body, regulating intestines and stomach, enhancing blood flow speed, preventing thrombus, protect heart, improving function of immunity of human body. This utility new type electrolysis of oxygen can produce the immunizing using, use is convenient.
NOVELTY - Discharging biomass carbon comprises placing plant-based synthetic oil gas generated into slurry mixing tank, adding water, mixing, utilizing pressure of the reaction system, and discharging slurry.    USE - Method for discharging biomass carbon (claimed).    ADVANTAGE - The method reduces abrasion valve.
NOVELTY - Separation of phenolic plant based oil and gas comprises passing gaseous products into the water containing raw material biomass carbon at more than 65 degrees C, adsorbing, adding water and biomass charcoal mixture, and continuously discharging.    USE - Method for separating phenolic plant based oil and gas (claimed).
NOVELTY - Solid waste treatment involves drying crop straw in a crusher to crush into small length straw powder, where the straw powder is conveyed in stirring room. The formed straw powder and sludge are mixed according to weight ratio of 3:1to obtain mixed material with stirring. The mixed material is dried in machine to process drying treatment, and then shifted into pyrolysis reactor for fast pyrolysis treatment at 420-600 degrees C for 10-40 minutes.    USE - Method for treating solid waste (claimed).    ADVANTAGE - The method shows enhanced drying efficiency, reduces energy consumption, and increases bio oil yield with good quality.    DETAILED DESCRIPTION - Solid waste treatment involves drying crop straw in a crusher to crush into small length straw powder, where the straw powder is conveyed in stirring room. The formed straw powder and sludge are mixed according to weight ratio of 3:1to obtain mixed material with stirring. The mixed material is dried in machine to process drying treatment, and then shifted into pyrolysis reactor for fast pyrolysis treatment at 420-600 degrees C for 10-40 minutes. The pyrolysis reactor treatment includes high temperature vapor-phase flow and high temperature biological carbon. The formed material is transferred into cooling device for separation to obtain bio-oil. The high temperature charcoal conveying is performed in a sealed cooling chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the solid waste treatment method. (Drawing includes non-English language text).
NOVELTY - A dual-mode fast pelletizer comprises feeding machine, control system, feed hopper (1), proportional-integral-derivative controlled quantitative feed screw auger, variable frequency motor (3), discharging port, granulator, main motor (5), speed reducer (4), forced pressure conveying screw auger, radial compression roller, axial compression roller, annular mold, flat mold (10), electric current transformer, intelligent transmitting ammeter, frequency converter and power supply.    USE - Dual-mode fast pelletizer for chemicals, biomass, food, feed and fertilizer.    ADVANTAGE - The pelletizer has simple structure, high yield, low energy consumption, and less abrasion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of dual-mode fast pelletizer.    Feed hopper (1)    Variable frequency motor (3)    Speed reducer (4)    Main motor (5)    Flat mold (10)
NOVELTY - An adsorbent is cylindrical, and has a micropore size of 0.8 nm or less, a porosity of less than 70%, and a specific surface area of 500-1500 m2/g.    USE - Adsorbent is used in pressure swing adsorption device for purifying marsh gas and coal bed gas.    ADVANTAGE - The adsorbent has rich micropores which enable efficient separation of methane (purity of greater than 97%) and carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of adsorbent, which involves crushing raw materials to less than 15 mu m, mixing all raw materials, molding the mixture into cylindrical shape, carbonizing, and activated using water vapor under nitrogen protection.
NOVELTY - A composite catalyst comprises main agent and additive. The main agent comprises 3-20 wt.% diethylenetriaminepentaacetic acid, 3-20 wt.% ethylenediaminetetraacetic acid, 3-15 wt.% amino trimethylene phosphonic acid, 3-15 wt.% hydroxyethylidene diphosphonic acid, 30-60 wt.% potassium hydroxide and 30-60 wt.% sodium hydroxide. The additive comprises ethanolamine and methanol.    USE - Composite catalyst is used for producing biodiesel (claimed).    ADVANTAGE - The biodiesel is efficiently prepared with high yield using the composite catalyst. The pipeline blockage of the biodiesel caused by fouling is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of composite catalyst, which involves mixing diethylenetriaminepentaacetic acid, ethylenediaminetetraacetic acid, amino trimethylene phosphonic acid, hydroxyethylidene diphosphonic acid, potassium hydroxide, sodium hydroxide, ethanolamine and methanol; and    (2) usage method of composite catalyst in production of biodiesel.
NOVELTY - Degrading gasoline involves performing aerobic reaction, where gasoline as co-metabolism substrate is biodegraded by alkalibacillus Ralstonia eutropha to obtain desired product.    USE - Method for degrading gasoline used for removing contaminants such as trichloroethylene and petrol present in underground water (claimed).
NOVELTY - Treatment of ammonium chloride evaporation-condensation solution is performed by adjusting pH of glycine in ammonium chloride evaporation-condensation solution to 9-11 by adding base, pumping into ammonia stripping device at 20-30 degrees C, air stripping, performing filter pretreatment, removing impurities, performing high anti-pollution reverse osmosis to obtain 1st stage reverse osmosis permeate and 1st reverse osmosis concentrate, and performing reverse osmosis intensive treatment of 1st stage reverse osmosis permeate.    USE - Treatment of ammonium chloride evaporation-condensation solution for recovery of concentrated active ingredients in pesticide production.    ADVANTAGE - Treatment process is simple and easy to control and has strong operability.    DETAILED DESCRIPTION - Treatment of ammonium chloride evaporation-condensation solution is performed by adjusting pH of glycine in ammonium chloride evaporation-condensation solution to 9-11 by adding base, pumping into ammonia stripping device at 20-30 degrees C, air stripping, performing filter pretreatment, removing impurities, performing high anti-pollution reverse osmosis to obtain 1st stage reverse osmosis permeate and 1st reverse osmosis concentrate, performing reverse osmosis intensive treatment of 1st stage reverse osmosis permeate to obtain 2nd stage reverse osmosis permeate and 2nd stage reverse osmosis concentrate, placing 1st stage reverse osmosis permeate and 2nd stage reverse osmosis permeate into tank, recycling into glycine production process, and recycling 2nd stage reverse osmosis concentrate into methenamine glycine production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of a treatment of ammonium chloride evaporation-condensation solution.
NOVELTY - Recovery of nitrogen and phosphorus from anaerobic fermentation broth comprises centrifuging an anaerobic fermentation broth for 3 minutes at 6000-10000 revolutions/minute (rpm); regulating pH value of the broth to 9-11 using sodium hydroxide saturated aqueous solution; adding 80-150 g zeolite/ g ammonia nitrogen in the fermentation broth, where the zeolite has a particle size of 0.5-5 mm;#under the room temperature, oscillating rotating fermentation broth and zeolite at 50-200 rpm for 12-24 hours; and standing 2-5 hours, precipitating, and recovering zeolite.    USE - Method for the recovery of nitrogen and phosphorus from anaerobic fermentation broth (claimed) used as slow release agent of nitrogen fertilizer.    ADVANTAGE - The method recovers more than 90% nitrogen and phosphorus.
NOVELTY - Treating ammonia nitrogen waste water involves feeding waste water into regulating pool and then transporting waste water into acidification tank and then to biological contact oxidation pond, neutralizing and precipitating tank. The waste water is now transported into filtration tank, where filtration tank comprises membrane bioreactor, conventional activated sludge tank, balance tank and nanofiltration and reverse osmosis system. The waste water is transported into hydrolysis acidification pool set with hydrolysis acidification bacteria and pH value 5-6 is maintained.    USE - Method for treating ammonia nitrogen waste water.    DETAILED DESCRIPTION - Treating ammonia nitrogen waste water involves feeding waste water into regulating pool and then transporting waste water into acidification tank and then to biological contact oxidation pond, neutralizing and precipitating tank. The waste water is now transported into filtration tank, where filtration tank comprises membrane bioreactor, conventional activated sludge tank, balance tank and nanofiltration and reverse osmosis system. The waste water is transported into hydrolysis acidification pool set with hydrolysis acidification bacteria and pH value 5-6 is maintained. Dissolved oxygen is maintained to 2-4 in neutralization and precipitation pool. Alkali is added into regulating tank to maintain pH 7-8. The waste water is transported into hydrolysis acidification pool and then biological contact oxidation pond. The waste water is transported into neutralizing and precipitating pool. The waste water is now transported into conventional activated sludge tank, neutralization sedimentation tank and filter tank.
NOVELTY - Covering film comprises a fixed rope (1) and a pile (2). The fixed rope with high strength is installed on a biogas tank (4), where is it surrounded by fixed piles. The covering film is provided with a gas covering film (3), which covers the storage device.    USE - Covering film for a storage device (claimed).    ADVANTAGE - The covering film is cost-effective, convenient and effective in application.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a covering film.    Fixed rope (1)    Pile (2)    Gas covering film (3)    Biogas tank (4)
NOVELTY - A biochemical treatment device comprises a reaction chamber (31) set with a discharge hole, and a door having overlapped part.    USE - A biochemical treatment device used for a kitchen waste (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the biochemical treatment device.    Support frame (2)    Base (16)    Liquid storage tank (18)    Reaction chamber (31)    Spiral stirrer (34)
NOVELTY - A nutrient soil comprises 100-150 pts. wt. plant fiber, 40-60 pts. wt. sand, 20-30 pts. wt. egg shell, 5-8 pts. wt. rice water, 15-20 pts. wt. rotten leaves, and 17-30 pts. wt. poultry manure.    USE - A nutrient soil used as a fertilizer.    ADVANTAGE - The nutrient soil is easy and inexpensive to prepare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the nutrient soil, comprising mixing plant fiber, sand, egg shell, rice water, rotten leaves, and poultry manure in a pot; and fermenting for 2-3 months at 20-30 degrees C.
NOVELTY - A production device comprises a storage device including a storage bin (1), a turnover barrier (2), a barrier frame, and a turning plate; and a fermentation device including a fermentation tank (6), a turbine stirrer (7), and a guide tube (5).    USE - A production device used for producing bio-organic fertilizer (claimed).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the production device.    Storage bin (1)    Turnover barrier (2)    Guide tube (5)    Fermentation tank (6)    Turbine stirrer (7)
NOVELTY - Preparation of tea tree organic composite fertilizer comprises mixing locally produced crop straw and vinegar lees, fermenting with Trichoderma, balancing acid, and adding auxiliary material.    USE - Preparation of tea tree organic composite fertilizer (claimed).    ADVANTAGE - The method uses waste as raw materials with wide sources and provides good quality product.
NOVELTY - Preparation of edible fungi culture material using straw and vinegar lees comprises taking crop straw waste and vinegar lees and straw Trichoderma fermenting and vinegar lees Trichoderma fermenting.    USE - Preparation of edible fungi culture material (claimed).    ADVANTAGE - The method uses crop straw waste as raw materials with wide sources and has reduced production cost.
NOVELTY - A Camellia nitidissima fertilizer comprises 28-32 pts. wt. corn straw, 8-12 pts. wt. bone meal, 4-8 pts. wt. soybean meal, 18-22 pts. wt. cottonseed meal, 18-22 pts. wt. dry chicken manure, 10-14 pts. wt. dry cow dung, 11-15 pts. wt. dry pig manure, 28-32 pts. wt. dry rabbit manure, 8-12 pts. wt. urea, 8-12 pts. wt. potassium sulfate, 4-8 pts. wt. glucose powder, 1-5 pts. wt. auxin, 8-12 pts. wt. trichlorfon, and 18-22 pts. wt. phenolic resin.    USE - Camellia nitidissima fertilizer.    ADVANTAGE - The fertilizer is rich in nutrients needed for fast growth of plants, and has easy to obtain raw materials and simple preparation method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by mixing raw materials, crushing into 40-80 mesh powder, pouring into fermentation tank, adding 1-2 times human excrement water, stirring, covering with plastic cloth, and fermenting for 25-35 hours/first fermentation and for 65-75 hours/second fermentation.
NOVELTY - An organic fertilizer comprises 10-30 pts. wt. animal manure, 10-30 pts. wt. crop residues, 1-3 pts. wt. chitin, 5-15 pts. wt. dead moss, 10-30 pts. wt. cooked larch needles, 10-20 pts. wt. urea, 1-3 pts. wt. enzyme and 1-3 pts. wt. fermentation agent.    USE - Organic fertilizer.
NOVELTY - An orchid microbial fertilizer comprises 20-30 pts. wt. waste residue, 8-15 pts. wt. wood chips, 3-5 pts. wt. coal ash, 5-8 pts. wt. fish feed, 5-10 pts. wt. peat, 5-10 pts. wt. dried animal manure, 3-8 pts. wt. carbonate, 4-6 pts. wt. synergistic agent, 5-10 pts. wt. chitosan, 3-8 pts. wt. fulvic acid, 5-8 pts. wt. Trichoderma, 2-5 pts. wt. Lactobacillus acidophilus, 5-8 pts. wt. Bacillus licheniformis and 2-4 pts. wt. Bacillus subtilis.    USE - Orchid microbial fertilizer.
NOVELTY - A special fertilizer comprises 10-15 pts. wt. urea, 15-25 pts. wt. monoammonium phosphate, 12-20 pts. wt. potassium sulfate, 12-20 pts. wt. potassium chloride, 5-8 pts. wt. zinc sulfate, 10-15 pts. wt. cake fertilizer, 2-4 pts. wt. borax, 2-4 pts. wt. peat, 2-4 pts. wt. enzymatic microorganism and balance additives.    USE - Special fertilizer used for watermelon (claimed).
NOVELTY - A granular fertilizer is prepared by taking amino acid residues, crushing slag powder into small particles, adding 4-8 wt.% potassium hydroxide or 4-10 wt.% slaked lime, mixing, pulverizing, reacting at pH value of 5.5-7.5, stirring using drum granulator to obtain organic acid particles, mixing purple sulfur bacteria and Bacillus subtilis to obtain fermentation broth, air drying or drying organic acid particles, and spraying 0.5-1.5 wt.% fermentation broth to organic acid particles.    USE - Method for preparing granular fertilizer (claimed).
NOVELTY - A humic acid organic-inorganic fertilizer composition from alcohol plant waste comprises active humic acid, inorganic fertilizer, trace element fertilizer, tea saponin and microbial fungicide comprising Bacillus subtilis and/or Bacillus megaterium.    USE - Humic acid organic-inorganic fertilizer composition from alcohol plant waste in the form of solid or liquid used for increasing corn yield and promoting crop roots (all claimed).
NOVELTY - A high-protein bio-organic fertilizer comprises 10-20 pts. wt. Bacillus subtilis, 5-10 pts. wt. protein components, 5-10 pts. wt. wheat bran, 5-10 pts. wt. rice bran, 25-30 pts. wt. chicken manure, 10-15 pts. wt. shale, 12-20 pts. wt. acid mixture, 5-10 pts. wt. herbal ingredients, 5-8 pts. wt. inorganic fertilizer and 3-6 pts. wt. trace elements.    USE - High-protein bio-organic fertilizer used for improving immunity of plants.    DETAILED DESCRIPTION - A high-protein bio-organic fertilizer comprises 10-20 pts. wt. Bacillus subtilis, 5-10 pts. wt. protein components, 5-10 pts. wt. wheat bran, 5-10 pts. wt. rice bran, 25-30 pts. wt. chicken manure, 10-15 pts. wt. shale, 12-20 pts. wt. acid mixture, 5-10 pts. wt. herbal ingredients, 5-8 pts. wt. inorganic fertilizer and 3-6 pts. wt. trace elements. The acid mixture comprises 8-12 pts. wt. humic acid, 2-4 pts. wt. amino acid and 2-4 pts. wt. acetic acid. The herbal ingredients comprise 1-2 pts. wt. Chrysanthemum nankingense, 1-2 pts. wt. Paris yunnanensis, 1-2 pts. wt. Scutellaria barbata, 1-2 pts. wt. Cyrtomium fortunei and 1-2 pts. wt. Hedyotis diffusa. An INDEPENDENT CLAIM is included for the preparation of high-protein bio-organic fertilizer comprising crushing composite shale through 80-100 mesh sieve, flattening, mixing protein components, chicken manure, wheat bran and rice bran with inoculants, stirring, adding flattened shale, fermenting by stacking at 45-50 degrees C and turning once per day for 7-10 days until alcohol fragrance or white mycelium is produced, drying, grinding herbal ingredients through 80-100 mesh sieve, mixing crushed herbs, trace elements, fermented material, Bacillus subtilis and inorganic fertilizer, and packing.
NOVELTY - A device comprises preheater (1) connected to static mixer (2) through pipeline (8), reaction tank (3), centrifuge (4) with inlet and outlets, acidification tank (5), glycerine storage (6), and groove (7).    USE - Device for production of biodiesel from glycerine (claimed).    ADVANTAGE - The device is simple, efficient, and can be easily administered.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of device for production of biodiesel from glycerine.    Preheater (1)    Static mixer (2)    Reaction tank (3)    Centrifuge (4)    Acidification tank (5)    Glycerine storage (6)    Groove (7)    Pipeline. (8)
NOVELTY - Synthesis of allantoin comprises adding glyoxylic acid water solution into a reactor, adding urea, catalyst, methanol, and 0.1-0.2% (based on the amount of glyoxylic acid water solution) sodium dodecyl benzene sulfonate, stirring, heating at 66-68 degrees C, reacting for 4-8 hours, cooling the reaction mixture to room temperature, filtering, washing, and drying to obtain the product.    USE - Synthesis of allantoin (claimed).    ADVANTAGE - The method improves the yield, shortens the reaction time, reduces the risk in the synthesis process, generates waste liquid, which is easy to process, and has environmental protection and high efficiency.
NOVELTY - Synthesis of allantoin comprises adding glyoxylic acid aqueous solution, urea, catalyst, methanol, and 0.1-0.2% (based on the amount of glyoxylic acid aqueous solution) sodium dodecyl benzene sulfonate into a reactor, stirring, heating at 66-68 degrees C, reacting for 5-10 hours, cooling the reaction mixture to room temperature, filtering, washing, drying, and obtaining the product, where catalyst is sodium dihydrogen phosphate or tungsten phosphoric acid.    USE - Synthesis of allantoin (claimed).    ADVANTAGE - The method improves the yield, shortens the reaction time, avoids the use of strong acid, reduces the risk in the synthesis process, generates waste liquid, which is easy to process, and has environment protection and high efficiency.
NOVELTY - Synthesis of allantoin using composite catalyst comprises adding glyoxylic acid aqueous solution, urea, catalyst, methanol, and 0.1-0.2% (based on the amount of glyoxylic acid aqueous solution) sodium laurate into a reactor, stirring, heating at 66-68 degrees C, reacting for 4-8 hours, cooling the reaction mixture to room temperature, filtering, washing, drying, and obtaining the product, where catalyst is ammonium dihydrogen phosphate and phosphomolybdic acid at 1:3-4 mol ratio.    USE - Synthesis of allantoin (claimed).    ADVANTAGE - The method achieves high yield, has short reaction time, reduced risk and production cost, environmental protection, and high efficiency, and generates waste liquid, which is easy to process.
NOVELTY - Synthesis of 2-methyl-4-amino-5-aminomethylpyrimidine comprises adding solvent, acetamidine hydrochloride, 3-acyl-aminopropionitrile (II), and triester orthoformate i.e. triethyl orthoformate or trimethyl orthoformate into a reaction container, dissolving, adding Lewis acid catalyst, heating the reaction container, upon detecting that compound (II) has reacted completely, directly adding the reaction liquid into aqueous solution or alcohol solution of inorganic alkali, and conducting hydrolysis reaction.    USE - Synthesis of 2-methyl-4-amino-5-aminomethylpyrimidine (claimed).    ADVANTAGE - The method is convenient, environment-friendly, and suitable for industrial production, uses inexpensive raw materials, does not require the use of sodium free acetamidine hydrochloride, thus, reducing the decomposition of acetamidine, has high reaction yield, simple and convenient operation, and no wastewater, does not need for separation and purification of product, and does not use carcinogenic o-chloroaniline or other small molecule aniline compound.    DETAILED DESCRIPTION - Synthesis of 2-methyl-4-amino-5-aminomethylpyrimidine comprises adding solvent, acetamidine hydrochloride, 3-acyl-aminopropionitrile of formula (II), and triester orthoformate i.e. triethyl orthoformate or trimethyl orthoformate into a reaction container, dissolving, where solvent is methanol, ethanol, isopropyl alcohol, n-butyl alcohol, sec-butyl alcohol, or tert-butyl alcohol, adding catalytic amount of Lewis acid catalyst, heating the reaction container at 65-105 degrees C, upon detecting that compound (II) has reacted completely, directly adding the reaction liquid into aqueous solution or alcohol solution of inorganic alkali, and conducting hydrolysis reaction at 80-110 degrees C.    R=methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, tert-butyl, phenyl, or alkylphenyl.
NOVELTY - A sulfinyl-1-hydrogen-benzimidazole derivative (I) is prepared by dissolving 2-(1-hydrogen-benzimidazol-2-ylthio methyl)-4-hydroxy-pyridine derivative (II) in solvent under nitrous acid catalyst and additive, and reacting with aqueous hydrogen peroxide solution at 15-45 degrees C for 3-10 hours.    USE - Method for preparing sulfinyl-1-hydrogen-benzimidazole derivative (claimed).    ADVANTAGE - The method is simple, environment-friendly, and has high product yield and purity.    DETAILED DESCRIPTION - A sulfinyl-1-hydrogen-benzimidazole derivative of formula (I) is prepared by dissolving 2-(1-hydrogen-benzimidazol-2-ylthio methyl)-4-hydroxy-pyridine derivative of formula (II) in solvent under nitrous acid catalyst and additive, and reacting with aqueous hydrogen peroxide solution at 15-45 degrees C for 3-10 hours.    R1, R2, R3=H, 1-5C alkyl, 1-5C alkoxy, 1-5C halogenated alkyl or 1-5C alkyl ether; and    R4=H, 1-5C alkyl, 1-5C alkoxy or 1-5C haloalkyl or 2-pyrrol-yl.
NOVELTY - A fasudil hydrochloride is prepared by mixing methyl dichloride and 10-50 mg/ml anhydrous sodium sulfate, stirring for 25-35 minutes, adding isoquinoline-5-sulfonyl chloride hydrochloride and solid sodium bicarbonate, filtering, cooling at not greater than 10 degrees C to obtain mixture A, dissolving homopiperazine in anhydrous ethanol, drying at 50-80 degrees C, cooling to not greater than 10 degrees C, adding dropwise mixture A at not greater than 10 degrees C, stirring for 1-5 hours, adding concentrated hydrochloric acid to adjust pH, filtering, distilling under reduced pressure, dissolving in water, filtering, concentrating, and cooling.    USE - Method for preparing fasudil hydrochloride (claimed).    ADVANTAGE - The method is safe, environment-friendly, low-cost and convenient to operate.    DETAILED DESCRIPTION - A fasudil hydrochloride is prepared by mixing methyl dichloride and 10-50 mg/ml anhydrous sodium sulfate, stirring for 25-35 minutes, adding isoquinoline-5-sulfonyl chloride hydrochloride and solid sodium bicarbonate, filtering, cooling at not greater than 10 degrees C to obtain mixture A, dissolving homopiperazine in anhydrous ethanol, drying at 50-80 degrees C, cooling to not greater than 10 degrees C, adding dropwise mixture A at not greater than 10 degrees C, stirring for 1-5 hours, adding concentrated hydrochloric acid to adjust pH, filtering, distilling under reduced pressure, dissolving in water, filtering, concentrating, cooling at 10 degrees C, crystallizing, washing with water, filtering, dissolving in anhydrous ethanol, adding 0.1-2 g/ml activated carbon, stirring for 25-35 minutes, filtering, cooling at 10 degrees C, crystallizing, filtering, and vacuum drying at 40-90 degrees C.
NOVELTY - A sparteine is extracted by crushing coniferous yellow flower seed, extracting in solvent at room temperature for 30 minutes, adding water, adjusting pH to neutral, extracting with organic solvent, adjusting pH, adding di-tert-butyl carbonate, stirring at 100 degrees C for 30 minutes, extracting with organic solvent, and neutralizing with acid and alkali.    USE - Method for extracting sparteine (claimed).    ADVANTAGE - The method is environment-friendly and has high product purity.
NOVELTY - Ganoderic acids C1 and F are separated by packing column with macroporous resin, dissolving lucid ganoderma extract in 30-60% ethanol, passing through column, eluting with 30-90% ethanol, analyzing by HPLC, taking ganoderic acid rich fractions, and concentrating; mixing petroleum ether, ethyl acetate, methanol and water at volume ratio of 5:3-7:1-6:4-9, shaking, ultrasonically degassing for 15-30 minutes, and cooling; and filling column, pumping mobile phase, adding ganoderic acid samples, eluting, and analyzing by HPLC. Macroporous resin is HZ-801B, HZ-806, HZ-816, HZ-818, HZ-835 or AB-8.    USE - Method for separating ganoderic acids C1 and F for treating tumor (claimed).    ADVANTAGE - The quick and solvent-saving method has high ganoderic acid purity of 95%, high efficiency, and large processing amounts.
NOVELTY - A high-power continuous biomass fuel gas production unit comprises feeding device (1), destructive distillation cracking device (2), gas leading-out device (3), carbon-removing device (4), gas purification device (5), smoke outlet, top cover device, and safety vent valve.    USE - High-power continuous biomass fuel gas production unit.    ADVANTAGE - The unit has short operation procedure at reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dry distillation method of biomass fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of high-power continuous biomass fuel gas production unit.    Feeding device (1)    Distillation cracking device (2)    Gas leading-out device (3)    Carbon-removing device (4)    Gas purification device (5)
NOVELTY - A high speed straw carbonizing device comprises feeding push rod (1), feeding cylinder, carbonization cylinder (3), discharging cylinder (4), combustion heating furnace (5), fan, exhaust gas collecting cylinder, and waste gas exhaust tube (9).    USE - High speed straw carbonizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of high speed straw carbonizing device.    Push rod (1)    Carbonization cylinder (3)    Discharging cylinder (4)    Combustion heating furnace (5)    Exhaust tube (9)
NOVELTY - The method involves filling a hopper (1) with biomass. A spiral feeder (3) is equipped with a pre-bed material of a fast fluidized bed gasification furnace (A). Biomass pyrolysis is performed to obtain combustible gas. The fast fluidized bed gasification furnace is re-entered into a gasification agent inlet to perform fast fluidized bed gasification furnace gasification reaction. Returning device coke and a bed material are entered into another fast fluidized bed gasification furnace (B).    USE - Biomass double fast fluidized bed gasification method.    ADVANTAGE - The method enables reducing sawdust, rice hull and tar content in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass double-fast fluidized bed gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass double-fast fluidized bed gasification method.    Fast fluidized bed gasification furnaces (A, B)    Hopper (1)    Spiral feeder (3)    Cyclone separator (4)    Returning device (5)
NOVELTY - Preparation of biodiesel involves mixing 10-20 pts. wt. peregal, 14-21 pts. wt. rosin, 5-10 pts. wt. unleaded petrol, 1-3 pts. wt. ammonium formate, 2-3 pts. wt. tert-butyl peroxyacetate, 4-7 pts. wt. benzyl alcohol, 5-7 pts. wt. oleic acid and 3-6 pts. wt. paraffin, heating, dissolving, stirring, cooling to room temperature, obtaining additive, mixing 0.5-1 pts. wt. additive, 20-30 pts. wt. diesel fuel, 10-20 pts. wt. cracked kerosene, 10-20 pts. wt. gasoline 70, 40-60 pts. wt. biodiesel, 2-4 pts. wt. co-solvent and 2-4 pts. wt. stabilizer, warming, incubating and cooling.    USE - Preparation of biodiesel is used for high-cold area.    DETAILED DESCRIPTION - Preparation of biodiesel involves mixing 10-20 pts. wt. peregal, 14-21 pts. wt. rosin, 5-10 pts. wt. unleaded petrol, 1-3 pts. wt. ammonium formate, 2-3 pts. wt. tert-butyl peroxyacetate, 4-7 pts. wt. benzyl alcohol, 5-7 pts. wt. oleic acid and 3-6 pts. wt. paraffin, heating to 30-40 degrees C, dissolving, stirring, cooling to room temperature, obtaining additive, mixing 0.5-1 pts. wt. additive, 20-30 pts. wt. diesel fuel, 10-20 pts. wt. cracked kerosene, 10-20 pts. wt. gasoline 70, 40-60 pts. wt. biodiesel, 2-4 pts. wt. co-solvent and 2-4 pts. wt. stabilizer, warming to 40-50 degrees C, incubating under stirring condition for 1-3 hours and cooling.
NOVELTY - Preparation of biomass gasoline involves adding surfactant, mixture of methanol and ethanol in ratio of 1:2 and proper amount of combustion improver into catalytic cracking device for catalytic cracking process, performing dealkalization of generated refined petroleum distillate, and stirring.    USE - Preparation of biomass gasoline (claimed).    ADVANTAGE - The biomass gasoline is safely prepared by environmentally-friendly, energy-saving and simple method.
NOVELTY - Preparation of methanol gasoline corrosion inhibitor involves adding alpha -methylstyrene dimer, maleic anhydride, dicumyl peroxide and dimethylbenzene, heating, cooling, adding octadecyl alcohol, polyethylene glycol, p-toluenesulfonic acid, n-butanol and ethyl acetate, heating, cooling, washing obtained mixture using sulfuric acid solution, sodium hydroxide solution and water, adding obtained mixture in benzotriazole, 2,6-tert-butyl-p-cresol, hexamethylene tetramine, ethanol, propiolic alcohol, trimellitate, surfactant and combustion improver, and stirring uniformly.    USE - Preparation of methanol gasoline corrosion inhibitor (claimed).    ADVANTAGE - The corrosion inhibitor has favorable compatibility with respect to methanol gasoline, and anticorrosion property.    DETAILED DESCRIPTION - Preparation of methanol gasoline corrosion inhibitor involves adding 20-30 pts. wt. alpha -methylstyrene dimer, 15-20 pts. wt. maleic anhydride, 10-15 pts. wt. dicumyl peroxide and 30-40 pts. wt. dimethylbenzene in reactor under nitrogen atmosphere, heating at 130-140 degrees C, maintaining reaction for 4-6 hours, cooling to room temperature, adding 15-30 pts. wt. octadecyl alcohol, 10-30 pts. wt. polyethylene glycol, 2-4 pts. wt. p-toluenesulfonic acid, 5-8 pts. wt. n-butanol and 15-20 pts. wt. ethyl acetate, heating at 140-150 degrees C, maintaining reaction for 8-12 hours, cooling to room temperature to obtain mixture (I), washing the mixture (I) using 1-3 %mass sulfuric acid solution, 1-3 %mass sodium hydroxide solution and water to obtain mixture (II), adding mixture (II) in 5-10 pts. wt. benzotriazole, 6-17 pts. wt. 2,6-tert-butyl-p-cresol, 4-8 pts. wt. hexamethylene tetramine, 20-30 pts. wt. ethanol, 3-8 pts. wt. propiolic alcohol, 4-8 pts. wt. trimellitate, 3-8 pts. wt. surfactant and 4-8 pts. wt. combustion improver, and stirring uniformly.
NOVELTY - Preparation of bamboo base raw material pellet fuel comprises cutting bamboo into sections, drying, filling bamboo in bamboo section at weight ratio of 3-5:1, placing into external dry distillation kettle, distilling, naturally cooling, crushing into fine powder, adding water at weight ratio of 15:1-2, uniformly mixing, pelleting, and drying.    USE - Method for preparing bamboo base raw material pellet fuel (claimed).    ADVANTAGE - The method has high combustion efficiency at more than 17000 J/g.
NOVELTY - A fuel composition comprises 60-70 %mass waste tire granules, 30-35 %mass sugarcane pulp, 2 %mass bleaching powder, 0.5-1.5 %mass sodium carbonate saturated solution, and 0.8-1.5 %mass ammonium bicarbonate saturated solution.    USE - Fuel composition is used for reburning coal-fired boiler in sugar cane industry.    ADVANTAGE - The environmentally-friendly fuel composition reduces nitrogen oxide emission by 70-80% and sulfur dioxide emission by 20-30%, and saves energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of fuel composition, which involves mixing waste tire granules in a drum-type mixer for 10-15 minutes, then adding sugarcane pulp, stirring for 8 minutes, then adding bleaching powder, stirring for 10-15 minutes, spraying sodium carbonate saturated solution and ammonium bicarbonate saturated solution, and aging for 1-3 hours; and    (2) usage method of fuel composition, which involves reburning fuel composition in coal-fired boiler for removing nitric oxide (NOx) at 1200 degrees C for 0.35-0.60 seconds with excess air coefficient of 0.85-0.9, burnout section temperature of 1100 degrees C and reburning excess air coefficient of 1.1-1.2.
NOVELTY - A nickel (alloy) material cold-forging lubricant comprises 46-total-loss system base oil and a composite additive. The composite additive comprises 5-12 %mass oiliness agent, 5-8 %mass antiwear agent, 3-5 %mass extreme-pressure agent, 0.8-1.2 %mass antioxidant, 0.005-0.01 %mass defoamer, 3-5 %mass friction modifier, and 3-5 %mass reinforcing agent.    USE - Nickel (alloy) material cold-forging lubricant (claimed).    ADVANTAGE - The nickel (alloy) material cold-forging lubricant has excellent cooling property, and cleaning property. The lubricant does not adhere to the mold, increases oil-film strength, reduces friction coefficient, is nontoxic and non-pungent, and does not corrode metal or die.
NOVELTY - Preparation of biodiesel involves uniformly mixing 20-80 wt.% tung oil, 10-50 wt.% canola oil, 0-30 wt.% palm oil, alcohol and transesterification catalyst, obtaining mixture and sonicating the obtained mixture.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method provides biodiesel having high dynamic viscosity.
NOVELTY - Production of biological diesel involves mixing 1-5 %mass waste oil with 1-5 wt.% phosphorus acid, treating, pre-heating to 100-150 degrees C, dehydrating, degassing, distilling under reduced pressure at 180 degrees C, removing free acid by condensation, pre-esterifying waste oil, then adding excess of ethanol, mixing at 50-80 degrees C under pressure of 0.1-0.5 MPa, catalytically-reacting waste oil for 2-4 hours, allowing standing, extracting using extraction agent, separating aqueous layer and solid layer, distilling, removing extraction agent and obtaining pre-esterified waste oils.    USE - Production of biological diesel (claimed).    ADVANTAGE - The method efficiently and economically provides biological diesel, with high yield and purity.    DETAILED DESCRIPTION - Production of biological diesel involves mixing 1-5 %mass waste oil with 1-5 wt.% phosphorus acid, treating, pre-heating to 100-150 degrees C, dehydrating, degassing in a de-acidification column, distilling under reduced pressure at 180 degrees C under pressure of 0.05 MPa, removing free acid by condensation, pre-esterifying waste oil, then adding excess of ethanol, mixing at 50-80 degrees C under pressure of 0.1-0.5 MPa, catalytically-reacting waste oil for 2-4 hours, allowing standing, extracting using extraction agent, separating aqueous layer and solid layer, distilling at 100 degrees C under reduced pressure of 0.05 MPa, removing extraction agent and obtaining pre-esterification of waste oils, esterifying resultant waste oil in pre-mixer, adding ethanol, reacting at 80-100 degrees C for 2-3 hours under pressure of 0.5-1 MPa, distilling at 60 degrees C under pressure of 0.1 MPa, purifying crude biodiesel, separating, washing and drying.
NOVELTY - Production of biodiesel involves providing system comprising catalytic distillation column, which is plate column having floating valve trays or sieve trays and separation device, mixing poor-grade oil and acid catalyst, supplying mixture through the top of distillation column, supplying 1-6C fatty alcohol through bottom of tower, heating, vaporizing, collecting effluent to obtain an intermediate product, separating intermediate product in separation device, heating and pressurizing.    USE - Production of biodiesel (claimed).    ADVANTAGE - The biodiesel is produced at high conversion rate.
NOVELTY - Marsh gas tank comprises outer wall, inner wall, transverse H, bottom groove, top, a slag outlet, a scum outlet, a channel port, a feeding port and a gas outlet; where the marsh gas tank is mosquito-repellent incense type, and its inner and outer sides are round and square (including elliptical, trapezoidal) structure.    USE - Used as a marsh gas tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas tank.
NOVELTY - Method for preparing calcium ion slow release agent, involves mixing polyethylene alcohol (PVA) and water in a mass ratio of 1:7-10, stirring mixture at 100 degrees C, making polyvinyl alcohol to completely dissolve viscous solution, cooling the solution to room temperature, adding calcium hydroxide powder and polyethylene alcohol solution in a mass ratio of 1:6-12, uniformly mixing and freezing at -20 degrees C for 24 hours.    USE - The method is useful for preparing calcium ion slow release agent (claimed).    ADVANTAGE - The method reduces fat hydrolysis of long chain fatty acid content, and high long chain fatty acid concentration for inhibition of kitchen garbage anaerobic digestion, and is simple, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic digestion method of kitchen garbage, which involves crushing kitchen garbage, performing centrifugal treatment, adding 0.5-2% fermented raw material, adding 1000-3000 mg/kg calcium ion slow release agent, uniformly stirring mixture, adjusting pH of the mixture using alkali to 6.9-8, where the volume ratio of the fermentation raw material and water is 7-9:1, adding water, performing anaerobic digestion at 34-39 degrees C for 30-40 days.
NOVELTY - Method for producing acetic acid, involves performing fermentation of kitchen garbage, removing cellulose, filtering fermented liquid, adding limestone to generate calcium acetate, filtering the solution, and adding hydrochloric acid to obtain acetic acid.    USE - The method is useful for producing acetic acid (claimed).    ADVANTAGE - The method is simple, cost-effective and provides high extraction rate.
NOVELTY - Preparing protein from biologically treated surplus sludge, involves (a) adding 1-5 %mass bacterial liquid comprising mixture of Bacillus subtilis, B.amyloliquefaciens, B.licheniformis, and B.megaterium to the sludge, adding the obtained product to liquid sludge fermentation tank, reacting at 35-55 degrees C for 18-24 hours (aeration rate of 0.2-0.6 l/min), incubating the obtained product for 18-24 hours, pressing the obtained product in frame filter press, concentrating the filtrate and drying the concentrate.    USE - The method is useful for preparing protein from biologically treated surplus sludge which is useful as organic fertilizer and animal feed (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing protein from biologically treated surplus sludge, involves (a) adding 1-5 %mass bacterial liquid comprising mixture of Bacillus subtilis, B.amyloliquefaciens, B.licheniformis, and B.megaterium to the sludge, adding the obtained product to liquid sludge fermentation tank, reacting at 35-55 degrees C for 18-24 hours (aeration rate of 0.2-0.6 l/min), incubating the obtained product for 18-24 hours, pressing the obtained product in frame filter press, concentrating the filtrate and drying the concentrate, where mass ratio of Bacillus subtilis, B.amyloliquefaciens, B.licheniformis, and B.megaterium is 5-10:1-5:2-7:1-5.
NOVELTY - The generator has upper negative electrode plate whose electrolytic groove (1) is provided with a steam-water separator (2). The steam-water separator is connected with the electrolytic groove through pipeline. An output end of steam-water separator is connected with a purifier (3). An output end of anode plate is connected with a peristaltic pump (4) whose output end is connected to a liquid storage bottle (5). An output end of liquid storage bottle is connected to anode plate. A stainless steel anode plate and lower cathode plate are passed through a bolt hole through a bolt.    USE - Small scale hydrogen generator.    ADVANTAGE - The structure of the hydrogen generator is simple. The electrolytic efficiency is enhanced. The liquid bottle opening is equipped with steam-water separating film to prevent the water leakage. The sealing performance of the hydrogen generator is increased. The defect of electrolyte leakage can be suppressed. The production efficiency can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the small scale hydrogen generator.    Electrolytic groove (1)    Steam-water separator (2)    Purifier (3)    Peristaltic pump (4)    Liquid storage bottle (5)
NOVELTY - Preparing bortezomib injection freeze-dried formulation, involves (a) weighing bortezomib, adding weighed bortezomib to tert-butanol, and heating and dissolving added material at 25-60 degrees C, (b) adding water to dissolved solution at 25 degrees C, and stirring the solution until a homogenous solution is formed, (c) adding mannitol to water to obtain solution, adding 0.05 %g/g activated carbon to the solution, stirring the solution for 30 minutes, and filtering the solution, (d) mixing filtered solution and the homogenous solution uniformly, freeze-drying mixed solution.    USE - The method is useful for preparing bortezomib injection freeze-dried formulation (claimed).    ADVANTAGE - The method reduces drying time, causes no pollution, and improves product yield.    DETAILED DESCRIPTION - Method for preparing bortezomib injection freeze-dried formulation, involves (a) weighing bortezomib, adding weighed bortezomib to tert-butanol, and heating and dissolving added material at 25-60 degrees C, (b) adding water to dissolved solution at 25 degrees C, and stirring the solution until a homogenous solution is formed, (c) adding mannitol to water to obtain solution, adding 0.05 %g/g activated carbon to the solution, stirring the solution for 30 minutes, and filtering the solution, (d) mixing filtered solution and the homogenous solution uniformly, freeze-drying mixed solution, where total water content of the homogenous solution of step (b) is 0-30%, total water content of the solution of step (c) is 70-100%, weight ratio of bortezomib and mannitol is 1:(5-70), weight ratio of bortezomib and tert-butanol is 1:(30-100), and weight ratio of bortezomib and water is 1:(550-1300). The freeze-drying step is performed at -50 degrees C for 2 hours, -10 degrees C for 5 hours and 25 degrees C for 4 hours.
NOVELTY - A biomass cracking furnace comprises insulating shell (1), high temperature cracking room (2), fire grate (4), ash chamber (3), ash outlet, feeding port (6), air inlet room, air blower, and follow-up chamber.    USE - Biomass cracking furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass cracking furnace.    Insulating shell (1)    Cracking room (2)    Ash chamber (3)    Fire gate (4)    Feeding port (6)
NOVELTY - The furnace has an insulating shell (10) connected with a fan (6) and a burning room. A secondary air pipe (8) is connected with a cracking room (2) that is matched with an air inlet (9) of a combustion room (10). An upper part of a combustion room (12) is connected with a hot transfer room (17) that is connected with an oil tube (18). The hot transfer room is provided with a heating tube (13) that is connected with a thermoelectric couple unit (14). The thermoelectric couple unit is connected with a temperature controller (15) of the heating tube.    USE - Electric biomass furnace.    ADVANTAGE - The furnace is environment-friendly, and has wide range of applications, and ensures zero discharge effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an electric biomass furnace.    Cracking room (2)    Fan (6)    Secondary air pipe (8)    Air inlet (9)    Insulating shell (10)    Combustion room (12)    Heating tube (13)    Thermoelectric couple unit (14)    Temperature controller (15)    Hot transfer room (17)    Oil tube (18)
NOVELTY - This utility new type claims a improved enamel one anaerobic fermentation tank, comprise tank body, two vertical circulation pump, two of circulation water inlet tube, two of circulation, two of spraying pipes, said upper tank body is provided with a feeding tube, a discharging tube, a thermometer, a vertical ladder, a heating water return pipe, a heating water supply tube, a sampling tube and a manhole. This utility new type improved enamel anaerobic fermenting tank, a water circulation stirring device is set on the tank body, and two selected from a water circulation, the claim of stirring, of valve through a pipeline up selecting each opening or opened at the same time, the utility model is new type completely solves the sludge sedimentation and sintered plate in the fermentation tank and so on, and it can prevent the liquid surface crust valid, the long-term stable anaerobic fermentation tank, fermentation tank reduce the frequent maintenance cost, and it has popularization use of value.
NOVELTY - This utility new type provide a one biomass carbon based organic fertilizer of compression device, a compression device comprise mixing furnace and compressed cabinet, a mixing furnace and compressed cabinet through connecting pipeline, a mixing furnace is set in the mixing box, a mixing box lower part set with stirring system, stirring device of a stirring system is set at the bottom centre of the mixing box, an electric motor of said stirring system is set on the mixing box outer bottom part centre. This utility new type of device is not easy to damage, use life is long, the operation is simple, with low energy consumption, and the cost is greatly reduced, at the same time, produce compressed carbon product of high yield and good stability, can be applied to a multi-industrial production in manufacturing.
NOVELTY - This utility new type relates to a biomass de-dust one producing pneuma decoking device, producing pneuma include furnace, producing pneuma and connecting of furnace feeding port, through gas delivery tube and producing pneuma furnace connecting of purification system and purification system of connecting buffer tank, the condensed water through the artificial pneuma furnace connecting tube of water tank, connecting with the water tank of boiler, pneuma furnace is provided with a inner container and outer container, inner container and outer container are provided with an insulating layer, an inner container and outer container set with middle layer condensing, condensing the inner container middle layer set with adsorption, producing pneuma furnace upper part is raw material storage tank, lower part of cracking pneuma in chamber, cracking in the bottom set with pneuma quantitative oxygen supply system, lower quantitative oxygen supplying system set with carbon ash sedimentation tank, carbon ash sedimentation tank set with hydraulic seal system, the lower hydraulic seal system set with underground sealed ash, sealed cabin outer side set with an ash box body, a feeding set with feeding system, this utility new type energy-saving and environment-friendly, produce pure gas of it also can produce hot water, which avoids the pollution of for the environment.
NOVELTY - This utility new type provide a one environment-friendly methanol composite fuel of a device, comprise: methanol storage tank, an additive storage tank, electromagnetic flow valve, the additive homogenizer, liquid homogenizer, the finished product storage tank, a plurality of additive storage tank through a branch tube connecting to the main pipeline up, each upper branch tube set with electromagnetic flow valve, the main pipeline connecting with the additive homogenizer, additive homogenizer pipeline connecting the liquid through homogenizer, upper liquid homogenizer connecting with a methanol storage tank, a methanol storage tank and the liquid between the homogenizer set with electromagnetic flow valve. This utility new type has novel structure, reasonable design, it can according to different requirement, a precise control through electromagnetic flow valve, the preparation environment with controllability, article of manufacture is high mass time of the preparation environment-friendly methanol composite fuel, in addition, the product is firm and durable, long service life, not limited by the application place so as to reduce the production cost.
NOVELTY - An acyl coenzyme A synthetase comprising a defined sequence of 658 amino acids (SEQ ID NO. 1), given in the specification, is new.    USE - The acyl coenzyme A synthetase is useful for producing for biodiesel.    ADVANTAGE - The acyl coenzyme A synthetase has improved enzyme activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing acyl-coenzyme A synthetase.
NOVELTY - Stable amorphous form of linagliptin, is new.    USE - The stable amorphous form of linagliptin is useful for the treatment of type 2 diabetes mellitus (claimed). No biological data given.    ADVANTAGE - The stable amorphous form of linagliptin is stable towards conversion to crystalline linagliptin on heating to elevated temperature, and can be easily manufactured in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of a stable amorphous form of linagliptin.
NOVELTY - Blended fuel comprises: 5-90 vol.% of a petroleum fuel; and 95-10 vol.% of a low carbon fuel produced using a thermochemical or biochemical conversion process. The low carbon fuel has a well-to-wheels greenhouse gas content which is at least 50% lower than a wells-to-wheels greenhouse gas content of a petroleum fuel, and the low carbon fuel has at least two performance characteristic values measurable by ASTM tests which are 30% improved than corresponding performance characteristic values of the petroleum fuel.    USE - Blended fuel is useful in a vehicle.    ADVANTAGE - The blended fuel: has a well-to-wheels greenhouse gas content which is at least 5% lower than the well-to-wheels greenhouse gas content of the petroleum fuel; has at least two performance characteristic values measurable by ASTM tests which are at least 5% improved than corresponding performance characteristic values of the petroleum fuel (claimed); has lubricity value of less than 450 mu m by HFRR at 60 degrees C (scar) measured by ASTM 6079, thus improving various engine performance characteristics of the traditional fuel and exhibiting overall improved well-to-wheels greenhouse gas content, as well as improved performance characteristics of the fuels, compared to the petroleum derived fuels; and utilizes low carbon fuel which is produced from a renewable biomass feedstock.
NOVELTY - Purifying natural gas comprises: sending a natural gas feed stream to flow at supersonic velocity through a conduit of a supersonic inertia separator and for causing the fluid to cool to a temperature that is below a temperature/pressure at which the condensables will begin to condense and forming separate droplets and/or particles; separating the droplets and/or particles from the gas; and collecting the gas from which the condensables have been removed and then sending the gas through an adsorbent bed to further purify the gas.    USE - The method is useful for purifying natural gas (claimed) from a variety of sources including gas fields, oil fields, coal fields, fracking of shale fields, biomass, and landfill gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for purifying natural gas comprising a supersonic inertia separator and at least one adsorbent bed.
NOVELTY - The system has first and second pairs of separating stages (a1, a2, b1, b2) connected in series for transferring retentate from the first pair of stages to the second pair of stages. Compressors (c1, c2) load the former pair of stages with pressure. A first pair of spacers (Ra2, Rb2) discharges the retentate from one of the stages of the first pair and one of the stages of second pair. A second pair of spacers (Pa2, Pb2) recycles permeate of the stages of the pairs. A spacer (Pb1) draws the permeate from another stage of the second pair.    USE - Permeator system for separating gas mixtures containing methane and carbon dioxide by using membrane gas permeation during biomass fermentation in a biogas system.    ADVANTAGE - The utilization of the separating stages and the spacers reduces energy consumption of the system and increases separation efficiency of the system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for separating gas mixtures.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a permeator system with separating stages. '(Drawing includes non-English language text)'    Separating stages (a1, a2, b1, b2)    Compressors (c1, c2)    Spacers (Pa1, Pa2, Pb1, Pb2, Ra1, Ra2, Ra2, Rb2)
NOVELTY - Composition comprises an aqueous mineral slurry comprising a dust suppressing amount of a non-absorbent silicate mineral having interlocking chains of silicate tetrahedra.    USE - The composition is useful for reducing or eliminating dissemination of fugitive dust particles into the atmosphere from a dust producing substrate (claimed) such as a solid particulate fertilizer, during long term storage and/or handling/shipping conditions.    ADVANTAGE - The composition reduces or eliminates the dissemination of fugitive dust particles in a cost-effective and environmentally-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a dust producing substrate coated with a substantially continuous outer layer comprising the dust suppressing amount of a composition; and    (2) coating the dust producing substrate with a substantially continuous outer layer, comprising contacting the slurry coating composition with the dust producing substrate and drying the coated substrate for a sufficient time and/or at a sufficient temperature to remove substantially all of the moisture from the coated substrate, to coat the substrate with a substantially continuous outer layer.
NOVELTY - Producing methane from sludge comprises (a) diluting 10-40 g/l of residual sludge and then concentrating until moisture content is 96-98% to obtain pretreated sludge, (b) adding the pretreated sludge into a water phase and then mixing with alkali solution and hydrolyzing, and carrying out solid-liquid separation of the hydrolyzed mixture and then centrifuging, (c) transferring the supernatant to an anaerobic reactor and then inoculating with anaerobic granular sludge, controlling chemical oxygen demand content of the anaerobic granular sludge to 0.35-0.75 kg and then reacting.    USE - The method is useful for producing methane from sludge (claimed).    ADVANTAGE - The method is capable of economically producing methane from sludge in a rapid manner with good stability and high yield.    DETAILED DESCRIPTION - Producing methane from sludge comprises (a) diluting 10-40 g/l of residual sludge and then concentrating until moisture content is 96-98% to obtain pretreated sludge, (b) adding the pretreated sludge into a water phase and then mixing with alkali solution and hydrolyzing, and carrying out solid-liquid separation of the hydrolyzed mixture and then centrifuging to obtain supernatant, and (c) transferring the supernatant to an anaerobic reactor and then inoculating with 10-60 vol.% of anaerobic granular sludge, controlling chemical oxygen demand (COD) content of the anaerobic granular sludge to 0.35-0.75 kg and then reacting for 72 hours. The COD content of the methane is 200-400 ml.
NOVELTY - Method for processing biomass containing cellulose, involves heat-processing biomass in aqueous solution containing peroxide, drying heat-processed aqueous solution, stir-mixing the dried biomass in an ionic liquid, depositing cellulose from ionic liquid including biomass, and regenerating cellulose.    USE - The method is useful for processing biomass containing cellulose (claimed).    ADVANTAGE - The method is simple, energy-saving and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing monosaccharide, disaccharide, and/or oligosaccharide, which involves carrying out enzymatic decomposition of the regenerated cellulose by cellulase through the pre-processing method.
NOVELTY - A hydrogen production apparatus (1) comprises container main body (2) and water supply unit (3) which supplies water to bottom part in the container main body, hydrogen discharge unit (5), vertical partition plate (7) which is made from porous material and is provided in container main body, and hydrogen storage material which keeps product containing water from stopping mixing at the time of fluctuation.    USE - A hydrogen production apparatus (claimed).    ADVANTAGE - Hydrogen from hydrogen storage material is suitably obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a notional sectional view of the hydrogen production apparatus. (Drawing includes non-English language text).    Hydrogen production apparatus (1)    Container main body (2)    Water supply unit (3)    Hydrogen discharge unit (5)    Vertical partition plate (7)
NOVELTY - The gasifier has a particle storage unit (A) which sends out to combustible solid content (7) produced by a gasifier unit to the downstream. A sealing unit (10) blocks the movement of the gas between a gasifier and a combustion furnace (8). A particle splitter (24) transduces the gasifying gas (6) produced by the gasifier, and separates the unreacted particle (25) in gasifying gas. An output pipe (26) is connected to the particle storage portion of the sealing unit, for taking out the unreacted particles isolated with the particle splitter.    USE - Circulating fluidized bed gasifier for gasifying organic solid raw material such as coal and biomass for producing gasifying gas for use as fuel for hybrid power system, and for manufacture of hydrogen, synthetic fuel e.g. synthetic natural gas and synthetic petroleum, and chemical fertilizer e.g. urea.    ADVANTAGE - The temperature of output pipe can be kept highly and the problem which water condenses in output pipe is prevented, when taking out the unreacted particle from the particle splitter which isolates the unreacted particle of gasifying gas by output pipe. The unreacted particles are stably supplied to the combustion furnace with the hot flow medium and combustible solid content of the particle storage portion. The outstanding effect of utilizing some fuels for the heating can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the circulating fluidized bed gasifier. (Drawing includes non-English language text)    Gasifying gas (6)    Combustible solid content (7)    Combustion furnace (8)    Sealing unit (10)    Particle splitter (24)    Unreacted particle (25)    Output pipe (26)    Particle storage unit (A)
NOVELTY - A binder is mixed with biomass, and molded. The obtained molded material comprising biomass is baked to obtain solid fuel.    USE - Manufacture of solid fuel (claimed) used for manufacturing boiler fuel, and fuel for cement kilns.    ADVANTAGE - The method enables economical manufacture of solid fuel having favorable grindability, moldability, strength, preservability and handleability, by effectively utilizing the biomass resources.
NOVELTY - Composite pellet comprises a biogenic component and a fossil component.    USE - The composite pellet is useful as a climate neutral fuel for energy-intensive plants in industries such as chemical, paper, food, and textile.    ADVANTAGE - The stable composite pellet can be manufactured with less energy consumption in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing a composite pellet, comprising connecting the biogenic component to the fossil component.
NOVELTY - The apparatus (1) has DC power supply unit (14) that supplies DC voltage to pair of electrode plate. A gas supply device (10) dilutes the hydrogen gas emitted from electrode plate or vacuum pump. The portion of air layer is covered with hydrogen gas permeable film (8). The hydrogen gas concentration of position at time of electrolysis is maintained to specific value by ventilating cathode or cathode water surface in gas for dilution which is supplied using gas supply device. The mixed gas containing hydrogen gas and gas for dilution is supplied to biological portion.    USE - High concentration hydrogen gas supply apparatus for biological portion such as human/animal cell and organ.    ADVANTAGE - The hydrogen gas is safely used, such that health maintenance in medical field and home can be improved. The function improvement of biological portion and diagnosis of disease can be achieved reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen gas supply apparatus for biological portions.    Hydrogen gas supply apparatus (1)    Electrolysis chamber (3)    Hydrogen gas permeable film (8)    Gas supply device (10)    DC power supply unit (14)
NOVELTY - The device has a rack device whose front end is provided with a detachable cover. A frequency modulation motor is connected with rotary drum through speed-adjusting transmission portion. The rotary drum is connected with a water inlet tube. The top portion of rack device is equipped with a washing water tube comprising a mud conveying guide plate. A seal cover device is connected with mud hopper.    USE - Device for treating sludge.    ADVANTAGE - The sludge treatment cost is reduced, operation time is reduced, efficiency is improved, and the sludge treatment process can be carried out simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sludge treatment device. (Drawing includes non-English language text)
NOVELTY - The device has a water washing tower (5), a reflux groove (17), a condensing cooler (9), a tower re-boiler (11), a regenerator (14) and two heat exchangers (6,7). The water washing tower is connected with a bottom portion of the reflux groove through a pipeline. The condensing cooler is connected with a top portion of the reflux groove through a pipeline. A top portion of the condensing cooler is connected with a bottom portion of the tower re-boiler. The heat exchangers are connected with the tower re-boiler.    USE - Device for reducing loss of extracting agent of aromatic hydrocarbon extracting device.    ADVANTAGE - The loss of valid extracting agent can be reduced. The cost requirement can be reduced and efficiency and the economic benefit can be improved. The simple operation can be ensured without increasing extra water amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for reducing loss of extracting agent of aromatic hydrocarbon extracting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for reducing loss of extracting agent of aromatic hydrocarbon extracting device.    Water washing tower (5)    Heat exchangers (6,7)    Condensing cooler (9)    Tower re-boiler (11)    Regenerator (14)    Reflux groove (17)
NOVELTY - Refining 1-aminoanthraquinone comprises mixing distilled dichloroethane and nitroanthraquinone in an aqueous medium, adding a sulfonating agent at a pH of 8-9 at 95-100 degrees C to carry out sulfonation treatment, reducing the temperature to 80 degrees C, filtering, washing with water, drying, placing the dried product into a polar solvent, heating to 135-140 degrees C to dissolve, reducing the temperature to 50 degrees C, filtering, washing with the polar solvent and dissolving in a solvent to obtain mother liquor and lotion, reducing with sodium sulfide, filtering, washing and drying.    USE - The method is useful for refining 1-aminoanthraquinone (claimed).    ADVANTAGE - The method: utilizes sulfonation agent and polar solvent, which selectively removes organic impurities and other nitro products; provides high purity product (of more than 99.5%) with high yield (by more than 10%); is easy, simple, stable, and economical; and reduces the production of waste residue (waste residue of 5%).
NOVELTY - Separation of water from process liquids, comprises selectively separating water by bioprocess using membrane module.    USE - The process is useful for separation of water from process liquids for producing methane (claimed).    ADVANTAGE - The process: utilizes membrane module, which is temperature and/or chemical resistant (claimed); requires less amount of medium, thus reduces operating cost; utilizes smaller inlets and outlet equipments; and exhibit lower hydraulic volume exchange in the process, with less amount of medium, incurred loaded waste stream.
NOVELTY - Converting a sugar into the form of a compound containing at least one ionic binding site comprises enzymatically or non-enzymatically hydrolyzing a hemicellulose-containing material, preferably a biomass, subjecting the obtained hydrolyzate subjected to a reaction containing at least one enzymatic step, releasing sugars and converting released sugars into compounds that have at least one ionic binding site.    USE - The method is useful for converting a sugar into the form of a compound containing at least one ionic binding site and for the recovery of arabinose, xylose, especially arabinose, arabino- gamma -lactone, arabonic acid, 2-keto-3-deoxyarabonic acid, alpha -ketoglutaric acid semialdehyde and/or alpha -ketoglutaric acid from lignocellulose-containing material (claimed).    ADVANTAGE - The method allows a direct utilization of sugars resulting from the hydrolysis of lignocellulose-containing (or hemicellulose containing) material.
NOVELTY - Composition for decomposition of cellulose-containing biomass comprises polypeptide including (a) polypeptide comprising an amino acid sequence of SEQ ID NO: 1, and (b) polypeptide comprising an amino acid sequence of SEQ ID NO: 1 in which one or more amino acids are added, deleted, inserted or substituted, and has effect which stimulates decomposition of cellulose containing biomass using biomass degradation enzyme. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The composition is useful for decomposing cellulose-containing biomass, and preparing sugar liquid (all claimed).    DETAILED DESCRIPTION - Composition for decomposition of cellulose-containing biomass comprises polypeptide chosen from (a) polypeptide comprising an amino acid sequence of SEQ ID NO: 1, (b) polypeptide comprising an amino acid sequence of SEQ ID NO: 1 in which one or more amino acids are added, deleted, inserted or substituted, and has effect which stimulates decomposition of cellulose containing biomass using biomass degradation enzyme, (c) polypeptide comprising an amino acid sequence exhibiting at least 90% sequence identity to an amino acid sequence of SEQ ID NO: 1, and (d) has decomposition of cellulose containing biomass stimulation effect using biomass degradation enzyme. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication. An INDEPENDENT CLAIM is included for method for preparing sugar liquid which involves adding the composition to suspension of cellulose containing biomass, and hydrolyzing cellulose containing biomass.
NOVELTY - A biofuel composition comprises a mixture of 98-60 vol.% of petroleum diesel fuel and 2-40 vol.% of bio-additive 2 containing acetals and vegetable oils.    USE - As biofuel composition (claimed). Also useful as diesel fuel and motor fuel.    ADVANTAGE - The use of fuel composition leads to an increased efficiency of the combustion process, to an increased engine power and to reduce emissions from the engine. The composition provides a high-quality diesel fuel with low cost and high yield of the product.
NOVELTY - Processing empty fruit bunches (EFB) to fermentable sugars comprises providing EFB feedstock, pre-treating the feedstock using hydrothermal pre-treatment, subjecting the pretreated feedstock to partial enzymatic hydrolysis using a cellulase preparation, separating the liquid hydrolysate from the solid residual obtained from partial hydrolysis, and resuspending the solid residual from partial hydrolysis and continuing enzymatic hydrolysis in a subsequent hydrolysis stage.    USE - The method is useful for processing empty fruit bunches to fermentable sugars (claimed) using multiple-stage enzymatic hydrolysis, where the fermentable sugars are useful for producing fuel ethanol or other fuels such as butanol or lactic acid monomers in synthesis of bioplastics, or many other products.    ADVANTAGE - The improved method is capable of effectively processing empty fruit bunches in an economical and simple manner.
NOVELTY - Preparing methane, comprises (a) producing a reactant gas mixture comprising hydrogen, carbon monoxide and carbon dioxide, by thermal gasification of carbon-containing starting materials, and (b) reacting hydrogen present in the reactant gas mixture, with carbon dioxide in a fermenter in presence of hydrogenotrophic methanogens and a nutrient medium.    USE - The method is useful for preparing methane (claimed).    ADVANTAGE - The method is energy-efficient, environmentally friendly and economic.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method for preparing methane (Drawing includes non-English language text).
NOVELTY - Fertilizer granule coating, comprises: a base fertilizer granule; and a biodegradable dust control coating topically applied to the base fertilizer granule, comprising an oil component, and a polymer additive substantially dissolved within the oil component. The polymer additive is dissolvable within the oil component when the oil component is heated to a temperature above room temperature so that the oil component is flowable.    USE - The fertilizer granule coating is useful for controlling dust (claimed) generated in the production and transport of granulated fertilizer. No biological data given.    ADVANTAGE - The fertilizer granule coating: ensures adequate dust control, without significantly inhibiting release of the fertilizer's nutrients to the soil, once applied; and utilizes polymer additive which increases the viscosity of the oil-based coating, thus increasing the duration for which the coating is capable of controlling or inhibiting the formation of dust particulates from the fertilizer granules.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing (100) a fertilizer granule coating, comprising: formulating a base fertilizer slurry; granulating the base fertilizer slurry into a rolling bed of base fertilizer granules; heating an oil component; mixing a polymer additive into the heated oil component to formulate a dust control coating; and topically applying the dust control coating to the base fertilizer granules.    DESCRIPTION OF DRAWING(S) - The figure illustrates a flowchart of a method for producing a coated fertilizer granule.    Method for producing a coated fertilizer granule (100)    Fertilizer production stage (102)    Dust control coating preparation stage (104)    Coating application stage (106)
NOVELTY - Removing nutrients from wastewater by photobiotreatment with photosynthetic microorganisms comprises removing nutrients in a reactor in the dark; and growing biomass into photobioreactor under illumination.    USE - The method is useful for removing nutrients from wastewater by photobiotreatment with photosynthetic microorganisms (claimed).    ADVANTAGE - The photosynthetic organisms can assimilate nutrients in the dark at a higher rate at which they require to multiply (claimed). With the method, the treatment can be performed continuously both day and night.
NOVELTY - The gas sensor has a gas sensing element that contains metal oxide nanoparticles e.g. tungsten oxide nanoparticles, and thin-film heating element that contains polysilicon. The gas sensing element has a first electrode and a second electrode. The metal oxide nanoparticles are disposed between first and second electrodes. An insulation layer is provided between gas sensing element and thin-film heating element and contains silicon nitride.    USE - Gas sensor used in gas sensor system (claimed) for detecting whether analyte is present in gaseous sample. Uses include but are not limited to hydrogen sulfide, hydrogen, propane, nitrogen dioxide, ammonia, trimethylamine, 2-methylpyrazine, nitric oxide, methanethiol, ethanol, 1,1,1 ,2-tetrafluoroethane, ozone, carbon monoxide, dimethyl disulfide, acetone, hexanal, propene, sulfur dioxide, carbon dioxide, and the like.    ADVANTAGE - Increases specificity and sensitivity to particular gases of interest by printing more than one type of metal oxide nanoparticles onto each gas sensor. Ensures early detection and warning of user to the presence of potentially hazardous analyte of interest in the surrounding environment at a point in time before the level of analyte in surrounding environment is significant health risk to the user so that user has sufficient time to take appropriate course of action to mitigate the potentially hazardous situation. Allows sensor to be heated in short pulses that decreases the overall power consumption of the device since nanostructured nature of sensing element has added advantage of higher surface area and is thermally cycled using very little power and without suffering from fatigue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of detecting whether an analyte is present in a gaseous sample.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic profile and top views of a sensor.
NOVELTY - Operating a continuous catalyst regeneration (CCR) system for reforming, involves: introducing a coking additive into a hydrocarbon feedstock to increase coke production; continuously introducing the hydrocarbon feedstock and the coking additive into a CCR reforming unit (12); continuously introducing hydrogen into the CCR reforming unit; continuously operating the CCR reforming unit to produce coke and hydrocarbon rich, hydrocarbon stream; continuously operating the CCR reforming unit to burn off excessive coking additive; and continuously recovering the hydrocarbon rich, hydrocarbon stream.    USE - The method is useful for operating a CCR system for reforming coke to produce a hydrocarbon rich, hydrocarbon stream, 5C+ reformate (claimed), liquefied petroleum gas and hydrogen.    ADVANTAGE - The method ensures enhanced production of coke formation using sulfur and kerosene additives to economically produce hydrocarbon rich, hydrocarbon stream, even at very mild severity catalytic reforming operations.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a continuous catalyst regeneration system.    Continuous catalyst regeneration reforming unit (12)    Separator (14)    Stabilizer (17)    Line (20)    Gasoline pool. (21)
NOVELTY - The plant has pipes through which water is pumped and passed through digesters. The organic substances are loaded from the top by hoppers. The loading hoppers and pumps are allowed for mud extraction and located along the digestion line. The mud is pumped in the hopper. The tank is configured to distribute mud into draining bags, through heavy floats, so that the dehydration and the composting are occurred contemporarily. The vertical limestone photosynthetic greenhouse allows subtracting carbon dioxide from biogas produced and receives fresh biomass.    USE - Multifunctional plant for digestion, dehydration and composting.    ADVANTAGE - Since the potential of thermoelectric plants are immense compared to depuration global synergy plants for depuration, biomass production and thermoelectric cogeneration (GSPDPTC) replace simultaneously thermal and purifiers, the production of biogas of high quality from permitted in conjunction with the manufactured buildings synergistic vertical can be ensured, and important environmental and energy innovations can be realized, without energy recovery allowed by linear digester, dehydrator, composters in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional plant for digestion, dehydration and composting.
NOVELTY - The apparatus (100) has primary and secondary tanks (10) that are connected on both sides of a separator (23). Primary electrode (21) is arranged at primary tank. Secondary electrode (22) is arranged at secondary tank. A suction element is arranged for inhaling the produced gas and is connected to a connection element (54a).    USE - Apparatus for producing gas such as hydrogen gas and oxygen gas used in chemical experiment.    ADVANTAGE - The hydrogen gas and/or oxygen gas can be obtained easily. The size reduction of the gas production apparatus can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gas production apparatus.    Tank (10)    Electrodes (21,22)    Separator (23)    Connection element (54a)    Gas production apparatus (100)
NOVELTY - The electrolytic cell comprises chambers (4, 5) through which the separation of oxygen and hydrogen is carried out by removal of gases across electrodes including an anode (2) and a cathode (3). The recirculation of oxygen/ozone mixture to the anode is carried out by an ozone generator. The electrodes are made of open-pored metal foam. The pore size of the open-pored metal foam is 10 mu m to 1 mm. The electrodes are rotatable. The anode is illuminated with an UV light.    USE - The electrolytic cell is useful for the separation of gases such as oxygen and hydrogen (claimed).    ADVANTAGE - The electrolytic cell separates the gas with high yield, and prevents a backward reaction of gases to water and/or inhibits undesired chemical reactions thus improving efficiency of electrolysis.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an electrolytic cell for gas separation.    Terminal (1)    Anode (2)    Cathode (3)    Chambers. (4, 5)
NOVELTY - The system (10) has a reaction unit (11) that electrolyzes decomposition water in oxygen and hydrogen using an electric power obtained by a power station. A storage system (13) connects a hydrogen storage unit (12) and reaction unit to store and send hydrogen. A first heat exchange unit (14) heats up the decomposition water sent to the reaction unit by exchanging heat with a heat source. A restoration system (16) connects to a discharge system (15) to discharge oxygen to an exterior of the reaction unit, and returns the remaining heat of the oxygen to first heat exchange unit.    USE - Hydrogen electric power storage system for electrolyzing decomposition water in oxygen and hydrogen using electric power obtained by power station.    ADVANTAGE - The energy efficiency of the system can be improved by returning the remaining heat which produced in the reaction unit by the restoration system to the first heat exchange unit. The purity of the hydrogen stored in the hydrogen storage unit can be raised by non-decompose water vapor being isolated in the isolation par.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen electric power storage method for electrolyzing decomposition water in oxygen and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram showing the state during the electrolysis of hydrogen electric power storage system and electric power generation state of the hydrogen electric power storage system. (Drawing includes non-English language text)    Hydrogen electric power storage system (10)    Reaction unit (11)    Hydrogen storage unit (12)    Storage system (13)    First heat exchange unit (14)    Discharge system (15)    Restoration system (16)
NOVELTY - Saccharification performance is evaluated by pretreatment process performed by contacting cellulose biomass and alkaline solution, saccharification process performed by saccharifying cellulose biomass using hydrolase, measuring the thermal decomposition temperature of cellulose biomass after and during the pretreatment process and evaluating the saccharification performance of the saccharification process based on the measured thermal decomposition temperature.    USE - Evaluation method of saccharification performance of a saccharification process for manufacturing biofuel and bio-butanol.    ADVANTAGE - The process is rapid and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the relationship between the thermal decomposition temperature of biomass after preprocessing and the saccharification rate of hexose in the cellulose biomass. (Drawing includes non-English language text).
NOVELTY - A microbial fuel cell (1) has tank (A) comprising microorganisms decomposing organic substance and generating an electron and a proton, an oxygen supplier supplying oxygen to a tank (B) adjacent to the tank (A) through proton permeable film (A1), electrode (E1) arranged positioned in tank (A) and electrode (E2) arranged in the tank (B), tank (C) adjoining the tank (A) through a proton permeable film (A2), and comprising water decomposed by light-receiving for generating electron and proton, and a photocatalyst electrode (10) arranged in the tank (C) and electrically connected.    USE - Microbial fuel cell is used for producing electric power.    ADVANTAGE - The microbial fuel cell has excellent output efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the microbial fuel cell. (Drawing includes non-English language text)    Microbial fuel cell (1)    Microorganisms tank (2)    Water tank (4)    Attached water tank (9)    Photocatalyst electrode (10)
NOVELTY - The control device has microcontroller that outputs operation command. The electrolysis of the water in electrolytic cell is performed to decompose the hydrogen and oxygen. The electrolytic liquid level, temperature, pressure and gas leakage signals corresponding to operation command are received. The ignition flame temperature adjustment control is performed based on received signals and the position of the working conditions and failure of machine is displayed by display circuit.    USE - Control device for water fuel machine used for cooking and shower heating applications.    ADVANTAGE - The environment-friendly and less pollution emission of water fuel machine are realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the control device for water fuel machine.    Water storage tank (2)    Ignition regulating liquid tank (3)    Liquid pump (5)    Electromagnetic valve (6)    Pressure transducer (7)
NOVELTY - The production device has hydrogen and oxygen depolymerizing kettles (2,4) that are connected with the hydrogen collector (3) and oxygen collector (5). A hot bridge (6) is located between the depolymerization kettles. A power supply (1) is connected with depolymerizing kettles through connecting electrode. A heat collector (7) is located between hot bridge and electrolytic bridge (9) and is connected with heating furnace (8). The pipeline of the hot bridge is equipped with upper valve (13).    USE - High-temperature steam electrolysis hydrogen production device.    ADVANTAGE - The low cost and high efficiency of high-temperature steam electrolysis hydrogen production device are ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a high-temperature steam electrolysis hydrogen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high-temperature steam electrolysis hydrogen production device.    Power supply (1)    Hydrogen depolymerizing kettle (2)    Hydrogen collector (3)    Oxygen depolymerizing kettle (4)    Oxygen collector (5)    Hot bridge (6)    Heat collector (7)    Heating furnace (8)    Upper valve (13)
NOVELTY - The coal mine wind-lack extraction device has absorbing cover (2) which is covered on air shaft diffusion tower (1). A steel frame in provided with molecular sieve desorbing device (3). A hollow tube is arranged on outer surface of absorbing cover. The opening end of hollow tube is connected to methane conveying passage (4). The air outlet is connected to methane device through methane conveying passage. The water-ring vacuum pump (5) is arranged between methane conveying passage and conveying device (6).    USE - Coal mine wind-lack extraction device.    ADVANTAGE - The methane in mine ventilation air can be extracted effectively for providing air source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the coal mine wind-lack extraction device.    Air shaft diffusion tower (1)    Absorbing cover (2)    Molecular sieve desorbing device (3)    Methane conveying passage (4)    Water-ring vacuum pump (5)    Conveying device (6)
NOVELTY - Manufacture of D,L-2-hydroxy-4-methionine-trace element chelate involves preparing hydrogen cyanide gas mixture in hydrogen cyanide synthesis unit using raw material comprising methane, ammonia and oxygen, performing delamination process, adding to reactor, reacting in presence of methylthiopropanal, obtaining 2-hydroxy-4-methylthiobutanenitrile, adding alkali, performing hydrolysis reaction, obtaining intermediate product, adding aqueous ammonia and aqueous solution of soluble salt of trace metals, performing chelation reaction, cooling, crystallizing and recycling mother liquor.    USE - Manufacture of D,L-2-hydroxy-4-methionine-trace element chelate (claimed).    ADVANTAGE - The method efficiently enables manufacture of D,L-2-hydroxy-4-methionine-trace element chelate with high yield by economical process.    DETAILED DESCRIPTION - Manufacture of D,L-2-hydroxy-4-methionine-trace element chelate involves using system containing hydrogen cyanide synthesis production unit, acid tower, tandem tank reactor, reactor, trace element chelate synthesis reactor and cooling crystallization reactor, preparing hydrogen cyanide gas mixture in hydrogen cyanide synthesis unit using raw material comprising methane, ammonia and oxygen, performing delamination process, adding obtained product to reactor, reacting in presence of methylthiopropanal as base catalyst, obtaining 2-hydroxy-4-methylthiobutanenitrile, adding alkali, performing hydrolysis reaction, obtaining intermediate product, adding aqueous ammonia solution, reacting, adding aqueous solution of soluble salt of trace metals, performing chelation reaction, cooling, crystallizing and recycling mother liquor.
NOVELTY - Pre-processing corn straw comprises taking crop straw and then crushing into a crushing machinery to obtain first product and then adding into 20-30% of acetic acid solution, boiling and cooling for 15-35 minutes to obtain second product and then heating to adjust a pH value to neutral using alkali solution.    USE - The method is useful for pre-processing corn straw (claimed).    ADVANTAGE - The method is capable of pre-processing corn straw in an economical manner with high yield improved conversion rate.
NOVELTY - Central modular pumping and crushing unit (24) of a biogas system (10) comprises a number of fluid- and/or substrate lines, intercommunicating reaction- and/or storage container (14) and conveying devices or pump (52). The central unit combines at least two pumps, a crushing unit, valves and/or slide valve via a separable connecting interfaces or flanged connections (44) which are connected to the other components of the biogas plant.    USE - Used as a central modular pumping and crushing unit of a biogas system.    ADVANTAGE - The central modular pumping and crushing unit has simple structural design; and allows faster and easier installation during setting up of the biogas plant and its components.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a biogas plant.    Biogas system (10)    Storage container (14)    Crushing unit (24)    Flanged connections (44)    Pump (52)
NOVELTY - The gasifier has conjoined and vertically positioned tubes including a proximal end defining an inlet (11) and a distal end defining an outlet. Contiguous reaction zones include a pyrolysis zone (20) angled toward central convergence followed by an oxidation zone (30) dilated in middle followed by a reduction zone (40). Separate rings of pressurized plano air inlets (31, 32) deliver adjustable volume and pressure of oxidant stream defined around perimeter of the oxidation zone. A grate is positioned below to the reduction zone without touching the reduction zone.    USE - Gasifier i.e. partially opened core downdraft gasifier, for gasifying feedstock (all claimed) e.g. carbon-containing feedstock such as solid biomass, household and industrial waste, and fossil fuel. Can also be used as a counter-current fixed bed updraft gasifier and a fluidized bed gasifier for gasifying a coal.    ADVANTAGE - The gasifier allows flow rate of the carbon-containing feedstock to be controlled when the feedstock passes through the dilated oxidation zone with minimal restriction in a cost-effective manner and to easily improve overall volume and flow of the feedstock passing through the gasifier, where the conjoined and vertically positioned tubes of the gasifier can eliminate a need for restriction i.e. hearth, that limits maximum achievable throughput of the gasifier.    DETAILED DESCRIPTION - The grate is a variably rotating and vertically adjustable grate (50).    DESCRIPTION OF DRAWING(S) - The drawing shows a cut-away front view of a gasifier.    Drying zone (10)    Inlet (11)    Pyrolysis zone (20)    Oxidation zone (30)    Pressurized plano air inlets (31, 32)    Reduction zone (40)    Variably rotating and vertically adjustable grate (50)
NOVELTY - The diffused layer production method involves producing a paste which includes carbon. The paste with carbon undergoes a curing process for 60 days. A diffused layer is formed the cured paste with carbon.    USE - Diffused layer production method for fuel cells.    ADVANTAGE - Improves the drain property of a diffused layer at low cost, by employing a curing process for the paste with carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a relationship between bottom portion of solid content and magnitude of crack within curing period. (Drawing includes non-English language text).
NOVELTY - The electrode has metal (hydr)oxide clusters deposited on a surface of an electrode metal, where the electrode exhibits bifunctionality with respect to hydrogen evolution reaction. The electrode metal comprises low coordination areas placed on the surface of the electrode metal, where the metal hydroxide clusters are placed on surface defects of the low coordination areas, 35% of the electrode is covered with deposited metal hydroxide clusters and the metal hydroxide clusters have height of about 0.7 nanometer and width of about 8 nanometer to about 10 nanometer.    USE - Rotating ring disk electrode e.g. Nickel hydroxide modified electrode and platinum and lithium ion electrode, for use in a hydrogen evolution reaction (HER) application in alkaline environments.    ADVANTAGE - The electrode improves surface reactivity of the HER by introducing solvated lithium ions into a compact portion of a double layer in factor of total increase in activity and by tailoring active sites for more efficient dissociative adsorption of water molecules. The electrode improves water dissociation process to improve alkaline HER activities. The electrode chooses lower potential limits so as to avoid significant bubble formation and minimize extended dissolution of a counter electrode.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an electrolytic cell    (2) a method for generating hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view representing water dissociation, formation of intermediates and recombination of atoms to form desorption from Nickel hydroxide domains followed by adsorption of another water molecule on a site.
NOVELTY - Preparation of dimethyl ether from straw briquette-charcoal biomass involves adding straw briquette to pyrolysis furnace, heating, pyrolyzing, obtaining biochar solid product and mixture of gas and coarse dust, separating crude gas, adding solid product to catalytic furnace, heating, performing cracking reaction, generating hydrogen, carbon monoxide and carbon dioxide, adding pyrolysis gas to gas purification equipment, performing alkaline solution desulfurization, washing, removing tar and carbon dioxide, adding to distillation column and distilling.    USE - Preparation of dimethyl ether from straw briquette-charcoal biomass (claimed).    ADVANTAGE - The method efficiently enables preparation of dimethyl ether from straw briquette-charcoal biomass by environmentally-friendly process with reduced consumption of energy.    DETAILED DESCRIPTION - Preparation of dimethyl ether from straw briquette-charcoal biomass involves adding straw briquette to pyrolysis furnace, heating to 400-650 degrees C, pyrolyzing for 10-60 minutes, obtaining biochar solid product and mixture of gas and coarse dust, separating crude gas in cyclone separator, obtaining pure biomass pyrolysis and ash by product, adding solid product to catalytic furnace, transferring nitrogen vent during pyrolysis process to catalytic furnace containing nickel-magnesium-cerium-tungsten oxide-containing compounds as catalyst, heating to 900-1200 degrees C, performing cracking reaction, generating hydrogen, carbon monoxide and carbon dioxide, adding pyrolysis gas to gas purification equipment, performing alkaline solution desulfurization, washing with water, removing tar and carbon dioxide, adjusting content of hydrogen and carbon monoxide, adding to distillation column, distilling, removing impurities and dehydrating water content to 1.1% or less.
NOVELTY - Apparatus for producing biomass energy using organic wastes in excrements and food wastes of passenger boat, comprises a collection unit (10) attached to the passenger boat for collecting organic wastes; a fermentation unit (20) for fermenting organic wastes collected in the collection unit; a storage unit (30) for storing biogas produced in the fermentation unit; and a combustion unit for combusting the biogas stored in the storage unit.    USE - Used as apparatus for producing biomass energy using organic wastes in excrements and food wastes of passenger boat.    ADVANTAGE - The apparatus minimizes the pollutant emissions by recycling organic wastes produced by passenger boats.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biomass energy, comprising (a) collecting organic wastes in the collection unit attached to the passenger boat, (b) fermenting the organic wastes collected in the collection unit in fermentation unit to produce biogas, (c) storing the biogas in the storage unit, and (d) combusting the biogas in the combustion unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of apparatus for producing biomass energy (Drawing includes non-English language text).    Collection unit (10)    Fermentation unit (20)    Storage unit (30)    Boiler (40)    Generator (50)
NOVELTY - The system has waste sludge fryer (30) provided with oil of high temperature to heat waste sludge segregated by segregation unit (20) and stored in waste sludge reservoir (10). The cooling devices (22,24) are provided to cool segregated waste sludge. A waste oil heater (60) is connected to oil recovery tank (44). The recovered oil is provided to crusher (70) for crushing waste sludge dried in dryer (80) to provide pellet-shaped particle. The waste oil ejected from waste oil storage tub (50) is conveyed to one side of refrigerator (82) for processing with condensed water.    USE - Continuous regenerative system of waste sludge such as waste food, sewage sludge, wastewater sludge and waste wood for producing bio coal.    ADVANTAGE - The production process time of the bio coal can be shortened. The productivity of the bio coal can be increased. The waste oil can be smoothly reused for the production of the bio coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous waste sludge regenerative system. (Drawing includes non-English language text)    Waste sludge reservoir (10)    Segregation unit (20)    Cooling devices (22,24)    Waste sludge fryer (30)    Oil recovery tank (44)    Waste oil storage tub (50)    Waste oil heater (60)    Crusher (70)    Dryer (80)    Refrigerator (82)
NOVELTY - Manufacture of synthetic zeolite catalyst involves using sodium catalyst, ion exchanging, developing using saline solution tetrachloropalladate, double calcining, and reducing.    USE - Manufacture of synthetic zeolite catalyst e.g. Pd-ZS2661 used for vegetable oil cracking product for producing gasoline product (all claimed) and palm oil cracking reaction.    ADVANTAGE - The method enables manufacture of synthetic zeolite catalyst having surface area of 118 m2/g.
NOVELTY - A mushroom cultivating material comprises 8-12 wt.% walnut branch powder, 17-23 wt.% shell powder, 35-45 wt.% husk chips, 15 wt.% fungi residue, 12 wt.% bran, 2 wt.% calcium superphosphate and 1 wt.% gypsum powder.    USE - Mushroom cultivating material.    ADVANTAGE - The cultivating material has rational proportion, and good ventilation property and water-retaining property. It has mushroom yield and biological efficiency of 130.3-142.6%. The method degrades toxic bacteria and decomposes lignin and cellulose macromolecular material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivating material comprising drying materials 1-2 days before using, killing bacteria by UV light, mixing walnut branch powder and shell powder, dry stirring, pre-wetting, piling to height of 1.0-1.2 m and width of 2-3 m, naturally fermenting, maintaining for 24 hours when material temperature reaches 60 degrees C, turning once a day, culturing, adding remaining raw materials, fermenting for 6-7 days, packing, sterilizing and cooling.
NOVELTY - Processing solid waste comprises fermenting wheat straw, pig manure and chicken manure and then culturing to obtain biogas to culture solution and then placing in a incubator, taking activated sludge as composite flora cultivated strains and then diluting with water to adjust a pH value to 7-8 and domesticating to composite flora, diluting the biogas slurry with water to adjust a pH value to 7-8, and adding the slurry to adjust a pH value to 7-8 and then mixing with composite bacteria at 25-30 degrees C and then culturing and screening.    USE - The method is useful for processing solid waste to produce biogas (claimed).    DETAILED DESCRIPTION - Processing solid waste comprises (S1) fermenting wheat straw, pig manure and chicken manure and then culturing to obtain biogas to culture solution and then placing in a temperature-controlled incubator, taking activated sludge as composite flora cultivated strains and then diluting with water to adjust a pH value to 7-8 and domesticating to composite flora at a temperature of 25-30 degrees C to obtain biogas slurry with chemical oxygen demand (COD) concentration of 1500-2000 mg/l, total nitrogen (TN) concentration of 120-170mg / L and total phosphorus (TP) is a 60-100mg / L, (S2) diluting the biogas slurry with water to adjust a pH value to 7-8 and domesticating composite flora to obtain slurry, and (S3) adding the slurry to adjust a pH value to 7-8 and then mixing with composite bacteria at 25-30 degrees C and then culturing and screening. The activated sludge has: COD concentration of 300-900 mg/l; TN of 30-45 mg/l; and TP of 15-30 mg/l.
NOVELTY - The method comprises preparing microorganisms by adding porous zeolite particles to slow oxygen releasing material, Bacillus subtilis, polyphosphate, nitrifying bacteria and denitrifying bacteria in ratio of (3-3.5):(1-1.5):(2-3):(1-1.5). The porous zeolite has a size of 40-250 meshes.    USE - The method is useful for dredging microorganisms (claimed).    ADVANTAGE - The method has good biological effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for dredging microorganisms.
NOVELTY - Biosolid nitrogenous fertilizer of formula H2NCONH2-N2?? (I) is new.    USE - Biosolid nitrogenous fertilizer (I).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biosolid nitrogenous fertilizer (I).
NOVELTY - Organic fertilizer comprises wheat bran, corn straw, manure, rice hull ash, grape vine powder, and fermenting agent. The fermenting agent is Bacillus subtilis, silicate bacteria, Trichoderma, Lactococcus lactis, ray fungi, Azotobacter chroococcum, Bacillus, B. megatherium, Escherichia coli, active material, cellulase, protease, and phosphorylase. The active material comprises bagasse, corn straw, bean powder, yeast, orange water, and Aspergillus niger.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has greatly improved viable cell content, greatly reduced fermentation time and temperature, and improved absorption efficiency.    DETAILED DESCRIPTION - Organic fertilizer comprises 8-12 pts. wt. wheat bran, 7-12 pts. wt. corn straw, 15-17 pts. wt. manure, 5-8 pts. wt. rice hull ash, 6-10 pts. wt. grape vine powder, and 2-4 pts. wt. fermenting agent. The fermenting agent is 1-2 pts. wt. B. subtilis, 3-4 pts. wt. silicate bacteria, 2-4 pts. wt. Trichoderma, 8-12 pts. wt. L. lactis, 2-5 pts. wt. ray fungi, 2-4 pts. wt. Azotobacter chroococcum, 1-2 pts. wt. B. megatherium, 1-2 pts. wt. Bacillus, 3-6 pts. wt. E. coli, 10-13 pts. wt. active material, 8-12 pts. wt. cellulase, 5-6 pts. wt. protease, and 8-12 pts. wt. phosphorylase. The active material comprises 13-15 pts. wt. bagasse, 7-8 pts. wt. corn straw, 7-8 pts. wt. bean powder, 15-17 pts. wt. yeast, 0.1-0.3 pt. wt. orange water, and 0.1-0.2 pt. wt. A. niger. An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing each component, adding wheat bran, corn straw, manure, rice hull ash, and grape vine powder into 0.15-0.2 MPa high pressure cooker, processing for 15-20 minutes, dividing the fermenting agent into 5 equal parts, uniformly mixing and stirring, fermenting for 10-12 days, uniformly mixing and stirring, and crushing to grain diameter of 0.1-0.7 cm.
NOVELTY - Organic selenium humic acid fertilizer (I), which is prepared by fermentation using fermentation bacteria, is new.    USE - Organic selenium humic acid fertilizer (I).    ADVANTAGE - The organic selenium humic acid fertilizer (I) has improved fertilizer efficiency, realizes soil heavy metal degradation of more than 40%, and is suitable for large-scale application.    DETAILED DESCRIPTION - Organic selenium humic acid fertilizer of formula FA-CH3-Se-CH3-CH3COO-Na (I), which is prepared by fermentation using fermentation bacteria, is new. An INDEPENDENT CLAIM is included for preparation of organic selenium humic acid fertilizer (I).
NOVELTY - A composite biofertilizer comprises 10-15 pts. wt. inorganic nitrogen fertilizer, 10-15 pts. wt. inorganic phosphate fertilizer, 8-11 pts. wt. inorganic potassium fertilizer, 2-5 pts. wt. copper trace element, 1-3 pts. wt. manganese trace element, 5-10 pts. wt. Bacillus natto preparation, 4-8 pts. wt. humic acid, 0.5-2 pts. wt. citric acid, and 0.2-0.5 pts. wt. procaterol hydrochloride.    USE - Composite biofertilizer used for breeding filter-feeding fish (claimed) e.g. chub and bighead carp.    ADVANTAGE - The composite biofertilizer can meet the growth requirement for filter-feeding fish. It is good for normal growth of algae, does not consume water-dissolved oxygen, and can turn the water color into green. It can effectively balance the water environment condition, prevent water quality deterioration, create good fish ecological condition, reduce the occurrence of fish diseases, and greatly improve fish production yield. It can enable a weight gain of 1 kg for chub and bighead carp when it is utilized based on an application dosage of 1.8 kg fertilizer (with 40 % ammonium bicarbonate and calcium-magnesium-phosphate content, and 20 % potassium chloride content) for each 667 m2 fish pond area.
NOVELTY - A biological fertilizer additive comprises 10-15 pts. wt. fresh corn cob extraction liquid, 12-14 pts. wt. seaweed extraction liquid, 5-8 pts. wt. fumaric acid, 2-5 pts. wt. EDTA, 5-10 pts. wt. cellulase-producing Cellulomonas, 2-5 pts. wt. white ant Clostridium, and 0.2-1 pts. wt. urea. The fresh corn cob extraction liquid is prepared by crushing mature corn cob, and then pressing to obtain fresh corn cob extraction liquid. The seaweed extraction liquid is prepared by cleaning seaweed, crushing, and then squeezing to obtain seaweed extraction liquid.    USE - Biological fertilizer additive used for freshwater cultivation (claimed) of e.g. fish.    ADVANTAGE - The biological fertilizer additive utilizes pure plant extraction liquid as raw material source, and includes beneficial bacteria which can activate and effectively improve the disease resistance of fish in freshwater, thus providing fish with good meat quality and more healthy protein.
NOVELTY - A green soil-improving fertilizer comprises 40-50 pts. wt. bean powder, 22-25 pts. wt. corn straw powder, 20-25 pts. wt. oxalic acid, 5-10 pts. wt. pole, 2-5 pts. wt. acetic acid, 0.5-2 pts. wt. cytokinin cells, 0.2-0.5 pts. wt. wolf associated unit cell bacteria, 0.05-0.2 pts. wt. ferment phage fiber bacteria and 0.05-0.2 pts. wt. slow release agent.    USE - Green soil-improving fertilizer.    ADVANTAGE - The fertilizer avoids environmental pollution, maintains fertility loose softness of soil, and has good cultivation effect of fruit tree.
NOVELTY - A mountain tea slow controlled-release fertilizer comprises urea, ammonium dihydrogen phosphate, potassium dihydrogen phosphate, kaolin, bauxite, potassium tripolyphosphate, sodium metaphosphate, disodium hydrogen phosphate, Bacillus thuringiensis powder, soybean straw powder, sweet potato straw powder, silicate bacteria powder, Bacillus cereus powder, calcium superphosphate, potassium sulfate, calcium nitrate, diatomite, and peat soil.    USE - Mountain tea slow controlled-release fertilizer.    ADVANTAGE - The environment-friendly fertilizer has organic and inorganic nutrients and trace elements content which can improve soil nutrient and quality of tea, and reduced costs.    DETAILED DESCRIPTION - A mountain tea slow controlled-release fertilizer comprises 35-45 pts. wt. urea, 15-20 pts. wt. ammonium dihydrogen phosphate, 16-26 pts. wt. potassium dihydrogen phosphate, 9-14 pts. wt. kaolin, 8-15 pts. wt. bauxite, 3-6 pts. wt. potassium tripolyphosphate, 2-6 pts. wt. sodium metaphosphate, 7-14 pts. wt. disodium hydrogen phosphate, 0.001-0.002 pts. wt. Bacillus thuringiensis powder, 25-30 pts. wt. soybean straw powder, 25-30 pts. wt. sweet potato straw powder, 0.001-0.002 pts. wt. silicate bacteria powder, 0.002 pts. wt. Bacillus cereus powder, 3-6 pts. wt. calcium superphosphate, 1-5 pts. wt. potassium sulfate, 3-6 pts. wt. calcium nitrate, 10-12 pts. wt. diatomite, and 16-20 pts. wt. peat soil.
NOVELTY - Tea tree plantation biofertilizer comprises chicken manure, potassium chloride, ammonium nitrate, diammonium phosphate, calcium biphosphate, calcium nitrate, potassium mineral powder, limestone powder, peat, conch shell powder, white clam shell powder, clam shell powder, turnip powder, mustard straw pole powder, flax straw powder, plant activating enzymes, Trichoderma, Bacillus subtilis, and potassium sulfate.    USE - Tea tree plantation biofertilizer used for reducing disease and insect pests.    ADVANTAGE - The fertilizer improves quality and yield of tea, solves slow growth of tea tree, is convenient to use and environment-friendly, and has low cost.    DETAILED DESCRIPTION - Tea tree plantation biofertilizer comprises 25-30 pts. wt. chicken manure, 15-20 pts. wt. potassium chloride, 15-20 pts. wt. ammonium nitrate, 9-11 pts. wt. diammonium phosphate, 8-14 pts. wt. calcium biphosphate, 3-5 pts. wt. calcium nitrate, 2-8 pts. wt. potassium mineral powder, 1-4 pts. wt. limestone powder, 3-6 pts. wt. peat, 2-8 pts. wt. conch shell powder, 3-5 pts. wt. white clam shell powder, 11-20 pts. wt. clam shell powder, 15-20 pts. wt. turnip powder, 25-30 pts. wt. mustard straw pole powder, 25-30 pts. wt. flax straw powder, 0.0001 pts. wt. plant activating enzymes, 0.001-0.002 pts. wt. Trichoderma, 0.003 pts. wt. Bacillus subtilis, and 11-16 pts. wt. potassium sulfate.
NOVELTY - Tea tree biofertilizer comprises ammonium nitrate, potassium sulfate, lactic acid bacteria powder, highland barley straw powder, broad bean straw powder, wheat straw powder, hairy clam shell powder, clam shell powder, Ginkgo wooden meal, oak wooden meal, potassium polymetaphosphate, potassium pyrophosphate, sodium aluminum phosphate, nitrifying bacteria powder, Rhizobium powder, zinc sulfate, and manganous sulfate.    USE - Tea tree biofertilizer.    ADVANTAGE - The fertilizer is environment-friendly, and improves soil, yield and quality of tea.    DETAILED DESCRIPTION - Tea tree biofertilizer comprises 15-20 pts. wt. ammonium nitrate, 9-12 pts. wt. potassium sulfate, 0.1-0.2 pts. wt. lactic acid bacteria powder, 10-15 pts. wt. highland barley straw powder, 30-45 pts. wt. broad bean straw powder, 60-80 pts. wt. wheat straw powder, 8-12 pts. wt. hairy clam shell powder, 3-9 pts. wt. clam shell powder, 3-5 pts. wt. Ginkgo wooden meal, 3-6 pts. wt. oak wooden meal, 2-4 pts. wt. potassium polymetaphosphate, 3-8 pts. wt. potassium pyrophosphate, 4-8 pts. wt. sodium aluminum phosphate, 0.1-0.2 pts. wt. nitrifying bacteria powder, 0.1-0.2 pts. wt. Rhizobium powder, 3-6 pts. wt. zinc sulfate, and 2-5 pts. wt. manganous sulfate.
NOVELTY - A compound fertilizer comprises 30-40 wt.% nitrogen-phosphorus-potassium complex (NPK) fertilizer, 22-30 wt.% imidacloprid, 0.1-1 wt.% difenoconazole oxazole, 0.1-0.5 wt.% Bacillus thuringiensis, 5-8 wt.% coating agent and 24-36 wt.% ascharite slag.    USE - Compound fertilizer.    ADVANTAGE - The fertilizer is nutrient-rich. The safe and environment-friendly method does not need high-temperature drying and is suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of compound fertilizer comprising crushing ascharite into 80-100 mesh powder, mixing Bacillus thuringiensis, ascharite slag powder, and NPK fertilizer to obtain mixed powder, mixing imidacloprid and difenoconazole oxazole, adding water, stirring, spray-coating onto mixed powder, adding coating agent, screening, and obtaining compound fertilizer granules.
NOVELTY - A biodiesel from food waste is produced by performing hydrothermal treatment, separating food grease from food waste, feeding food grease in single-stage or multi-stage reactor containing inflow immobilized lipase enzyme, adding short chain alcohol, and performing biodiesel transesterification. Lipase enzyme contains Aspergillus niger, Candida rugosa and Klebsiella lipase mixture at mass ratio A. niger:C. rugosa:Klebsiella of (0.8-5):(0.8-6):(0.5- 4).    USE - Production of biodiesel from food waste (claimed).    ADVANTAGE - The method produces high quality biodiesel, includes catalytic transesterification reaction which is highly efficient, and has excellent yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of the production of biodiesel from food waste. (Drawing includes non-English language text).
NOVELTY - This utility new type claims a integrated one baffled autotrophic biological nitrogen removal reactor, include reactor main body, wherein said reactor main body is provided with a first baffle plate, the first baffle plate of the said of said reactor main body is divided into unit short-range nitrification and anaerobic ammonia oxidation unit, upper end of first baffle plate of the reactor main body of said top connecting the lower end with the reactor main body of the bottom of the gap, the anaerobic ammonia oxidization unit from left to right is divided into bio-membrane zone, bio-membrane zone, a sludge zone, the second zone and the second area of said bio-membrane of the second area and a sludge zone is set between the second baffle plate, the a sludge zone and the second zone is provided with a third baffle plate. This utility new type realizes the short-range nitrification and anaerobic ammonia oxidation process in a single reactor process of coupling set of multi-level baffling plate prolongs the waste water flows through the path, and improves the valid reaction time, strengthening the left holding ability.
NOVELTY - Paecilomyces varioti F1-23 strain (I) having preservation number of CCTCC No. M2013471, is new.    USE - (I) is useful for processing formaldehyde containing industrial waste water (claimed).    ADVANTAGE - (I) is capable of processing the formaldehyde containing industrial waste water with high degradation ability and hereditary.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of (I) for processing formaldehyde containing industrial waste water, where the application method comprises placing Paecilomyces varioti in a carrier, mixing and oscillating treatment or fully contact degrading formaldehyde in industrial waste water with content of lower than 6 g/l.
NOVELTY - This utility new type claims a one anaerobic ammonia oxidation and biological filler device, wherein, set with porous filling material ball in the stuffing balls fill with an annular porous suspended filler, multi-porous filling material ball by a connecting rod in series together to form the filling material ball string, set with multi-filling ball string, the multi-filling ball string side by side lengthways, composed of multi-row multi-column up in the horizontal direction, and filling material ball filling material ball pitch control is polypropylene material at 5 cm degrees centigrade, each filling ball string of upper lower two end transverse fixed fixing pole, the fixing pole fixed on outer frame of upper, a porous filling material ball, the diameter is 10cm-15cm, the spherical porous, the pore size is less than inner fill of annular suspension filler. In this utility new type sewage treatment pool for anaerobic ammonia oxidizing bacteria of a steam-cured, with simple and practical structure, use effect is good, convenient to assemble and disassemble and change.
NOVELTY - Agrobacterium LAD9 strain has a preservation number is CGMCC NO.2962, and is new.    USE - Agrobacterium LAD9 strain used for treating waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating waste water, which involves:    (A) utilizing bacterial strain LAD9; and    (B) inoculating the bacterial strain in waste water to remove organic nitrogen.
NOVELTY - Alpha-amylase gene (I) having nucleotide sequence of SEQ ID NO: 2 (a 1542 base pair sequence fully defined in the specification), is new.    USE - (I) is useful for degrading starch including rice starch, wheat starch and crude green bean starch (all claimed).    ADVANTAGE - (I) has high purity of more than 85% and renaturation rate of more than 50%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) amylase encoding gene having an amino acid sequence of SEQ ID NO: 1 (a 513 amino acid sequence fully defined in the specification); (2) recombinant expression plasmid comprising (I); (3) recombinant bacteria comprising (I); (4) renaturation of (I) comprising washing alpha -amylase inclusion liquid for 1-2 times with deionized water, adding washing liquid including 50 mM of tris(hydroxymethyl)aminomethane-hydrochloric acid (Tris-HCl) buffer to pH value of 8, 5 mM of EDTA and 1 vol.% of TritonX-100 (RTM: Tert-octylphenoxypolyethoxyethanol), dissolving in the alpha -amylase solution, adding 280-320 mu g/ml of dissolved liquid into 6 M of Tris-HCl buffer to pH value of 6, sodium chloride solution, and EDTA, then placing at 4 degrees C for 24 hours, oscillating for 3 hours, centrifuging the solution at 12000 revolutions per minute (rpm) for 20 minutes, removing the supernatant, placing supernatant into a dialysis bag for renaturation for 12 hours, carrying out dialysis process at 4 degrees C, adding dialysis liquid including 50 mM of Tris-HCl buffer to pH value of 8, 10 vol.% of glycerol, 50 mM of sodium chloride and 0.5 mM of EDTA.
NOVELTY - Sludge quick stabilization machine, which is suitable for 10 ton following sludge quick stabilizing treatment of sludge microorganism aerobic fermentation. By spray tower, maintenance ladder, a fixed guardrail, throwing door, the hydraulic door opening mechanism, the movable guardrail, decorative plate, a discharging door, a stirring shaft driving, control cabinet, a machine liner, a double-shaft stirring system and protecting pole and the base to form the sludge quick stabilization machine is an integral welding structure. The processor suitable for configuration of microorganism flora, the sewage treatment plant can produce of sludge within 7-9 days, aerobic ferment, the process is easy to be degraded in sludge of organic matter degradation rate of more than 95%, water content is less than 45%, carbon nitrogen ratio is about 26, the stabilizing of; rear sludge, can automatically control the fermentation process, it does not need the look after; can use local processing sludge, reduce the transportation by using existing factory, saves the investment cost.
NOVELTY - Methane conversion accelerator comprises 144-300 g of phosphate comprising disodium hydrogen phosphate, sodium dihydrogen phosphate, dipotassium hydrogen phosphate, or potassium dihydrogen phosphate, 300-850 g of urea, 0.5-1 g of cobalt chloride, and 1-5 g of iron salt comprising ferrous chloride or ferrous sulfate.    USE - The methane conversion accelerator is useful for anaerobic fermentation of industrial wastewater i.e. xylose wastewater, and methane biogas (all claimed).    ADVANTAGE - The methane conversion accelerator is convenient to use, and can be prepared in simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the methane conversion accelerator comprising weighing the above components, and then uniformly mixing.
NOVELTY - This new type utility claims a industrial organic fertilizer production line, one filling production line comprise (1), culture room (4), a separating system (6) and organic fertilizer production system (13), filling production line (1) through transferring trolley (3) is connected with the culture room (4) connect, culture room (4) through transferring trolley (3) and the separating system (6) connecting and separating system (6) and the organic fertilizer production system (13) connect. This utility new type can be organic waste process for preprocessing, using full-automatic device the musca domestica for a biological conversion of organic waste production, and finally obtain organic fertilizer, it has high degree of mechanization, high efficiency of production. Greatly reduces the production period, reduces the labour intensity.
NOVELTY - This utility new type claims a manure turning one target, include roller, orderly fixing multiple turning rake teeth up on the roller, a roller two ends is provided with a left and right side plate, a left side plate of right head through two of fixing plate is welded on the transverse pole and the cross pole II is up to the fixed rectangle frame, each set with two limit wheels and two end of retaining ring, a cross rod I of two steel wire rope and the bolt pole II and the long head upper cross bar m and cross pole II, said upper rolling shaft orderly fixed several turning rake teeth using phi 3-phi 4 mm of elastic steel wire of the transverse rod II position fixed inner radius rolling turning rake teeth of 5-15 mm, the turning time on the rake teeth rod II and the butt scraper produce , the effect of the poultry excrement of upper turning rake teeth, use time through two head of upper cage traction device of steel wire rope bolt up the retaining ring, traction time rolling turning rake teeth stirring with cushion and the turning target of poultry excrement, traction device and time for cleaning the fermentation tank is used for traction excrement shovel, and it can save investment and maintenance cost.
NOVELTY - Arrangement structure of one fermentation tank, a biogas pneuma comprise anti-backflow device, double storage pneuma, bolt cover plate, a discharge port, a return port, a feeding port, a constant pressure control cabinet, a thermometer, a knife gate valve, a negative pressure protecting, viewing mirror, a manhole cover plate, a biogas pneuma backflow-proof device is set on the one of the upper corner of the whole structure, a double-membrane pneuma storage cabinet is arranged at the middle of the whole structure, a discharge hole is set in the whole structure of the lower end, a thermometer, a knife gate valve is set on the side surface of the whole structure. This utility new type has unique design, reasonable arrangement and low cost, high feasibility, suitable for popularization and use and small floor area.
NOVELTY - This utility new type claims a online marsh gas fermenting process one data collect and treat system, comprising a gas measuring and transmitting device, signal transmission and receiving device, data processing device, and the display device is composed of a through mounting gas measuring and transmitting device of the marsh gas fermentation tank upper, time in a fermentation tank fermentation status, signal transmission and receiving device, the information send to data processing device a processing operation, and finally displayed on the display device is set up. This utility new type through the filtering collecting device upper CH4 transmitter, CO2 transmitter or the like of a gas component change condition in marsh gas fermenting process, through a PLC programmable controller and a processing, real-time on-line displaying and recording the fermentation process parameter to realize the whole marsh gas fermenting process in gas component change of visualization is of improved fermentation process and fermenting device provide thoery. Besides, this utility new type has simple structure, a high precision, good portability.
NOVELTY - Fuel cell reactor comprises two wall cloisters provided with hollow partition wall, where hollow partition wall comprises carbon felt (6). Carbon felt is provided with corrosion resistant material (7) and is connected with an external circuit. Water inlet (1) is connected to inner wall of the fuel cell reactor, whereas water outlet (2) is connected with power generating system.    USE - Fuel cell reactor for activated sludge treatment (claimed).    ADVANTAGE - The fuel cell reactor is convenient in operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell reactor.    Water inlet (1)    Water outlet (2)    Carbon felt (6)    Corrosion resistant material (7)
NOVELTY - Producing nicotinic foliar fertilizer using fresh tobacco waste, comprises e.g. adding crushed waste fresh tobacco leaves in probiotic liquid, carrying out stack-fermentation treatment, adding waste crushed fresh tobacco leaves in fermentation liquid, using 100 meshes filter screen to filter large granule impurity, concentrating filtrate, adding aluminum sulfate and polyacrylamide, stirring, decoloring the concentrated liquid and allowing to stand, using filter screen to filter, adding 5% probiotic in decolored filter liquid, stirring and allowing it to stand, and removing pungent smell.    USE - The method is useful for producing nicotinic foliar fertilizer using fresh tobacco waste (claimed).    ADVANTAGE - The method uses biochemical treatment to improve the fertilizing efficiency of fertilizer with insecticidal activity.    DETAILED DESCRIPTION - Producing nicotinic foliar fertilizer using fresh tobacco waste, comprises (i) adding crushed waste fresh tobacco leaves in 1% probiotic liquid, carrying out stack-fermentation treatment, where the fermentation time is 10-15 days, (ii) adding the waste crushed fresh tobacco leaves in fermentation liquid, using 100 meshes filter screen to filter large granule impurity, and then taking the filtrate and heating, concentrating to one-half of the original volume, (iii) adding aluminum sulfate and polyacrylamide to the concentrate, stirring uniformly, decoloring the concentrated liquid and allowing to stand for 2 days, then using 200 meshes filter screen to filter and repeating one time, (iv) adding 5% probiotic in decolored filter liquid, fully stirring and allowing it to stand for 2 days, and removing pungent smell.
NOVELTY - Method for preparing microorganism fertilizer or pesticide, involves (a) uniformly mixing carbon residue mud, yeast and Actinomycete, adding fructus cannabis, tobacco residue and bean residues, immobilizing mixture at 15-55 degrees C, fermenting mixture for 25-60 hours to obtain medicinal fertilizer, processing mixture, packaging fertilizer, and fermenting mixture to obtain product of microorganism fertilizer.    USE - The method is useful for preparing microorganism fertilizer or pesticide (claimed).    ADVANTAGE - The fertilizer is convenient in package and transport.    DETAILED DESCRIPTION - Method for preparing microorganism fertilizer or pesticide, involves (a) uniformly mixing carbon residue mud, yeast and Actinomycete, adding fructus cannabis, tobacco residue and bean residues, immobilizing mixture at 15-55 degrees C, fermenting mixture for 25-60 hours to obtain medicinal fertilizer, where the mass ratio of mud carbon residue, fructus cannabis tobacco residue and bean residue is (100-500):(5-25):(10-50):(2-10), where the carbon residue is fulvic acid and brown humic acid, and the total humic acid of mud carbon residue is 5-35%, processing mixture, packaging fertilizer, and fermenting mixture to obtain product of microorganism fertilizer, or (b) continuously fermenting fertilizer middle product, filling to obtain product of microorganism liquid pesticide, adding chelated microelement in microorganism liquid farm chemical to obtain trace of liquid pesticide, where the microelement comprises boron, molybdenum, selenium, zinc and iron, and adding amount of microorganism liquid is 15-25 g/l.
NOVELTY - Preparing crop and fruit tree fertilizer comprises grinding raw material into paste or powder using a grinder or a mill, soaking in clean water for 24 hours, removing water, adding 1-1 vol.% Bacillus subtilis, controlling temperature at 28-37 degrees C, stirring to uniformity, composting and fermenting continuously for 3-7 days.    USE - The method is useful for preparing crop and fruit tree fertilizer (claimed).    ADVANTAGE - The fertilizer can be directly applied on crop and fruit tree (claimed), quickly recovers soil fertility and persists for long time, and improves air permeability and water permeability of soil. The method solves secondary comprehensive utilization of waste, protects living environment, realizes recycling and avoids use of large amount of chemical fertilizer.
NOVELTY - Organic fertilizer comprises 20-30 pts. wt. plant ash, 55-65 pts. wt. waste edible mushroom cultivation material, 10-15 pts. wt. soybean meal and 5-15 pts. wt. livestock manure. The plant ash is residue of rice pile or burnt trees.    USE - The organic fertilizer is useful for improving soil quality; loosening soil; and preventing, and treating plant diseases and insect pests.    ADVANTAGE - The organic fertilizer effectively facilitates in-vitro cultivation of plants, and thus it improves the quality of vegetables; can re-use the waste material; converts waste into useful materials; and has low cost raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer, comprising either (i) performing mixed fermentation by spraying calcium oxide into a fermentation tank at thickness of 1-1.5 cm, (ii) adding the above mentioned raw materials, and spraying a layer of calcium oxide at thickness of 1-1.5 cm, and (iii) fermenting for 60-90 days by covering a film on the fermentation tank, drying the fermented organic fertilizer until the water content is 50-55%, granulating, and packaging; or (a) performing mixed fermentation by spraying calcium oxide into a fermentation tank at thickness of 1-1.5 cm, (b) adding the above mentioned raw materials, and spraying a layer of calcium oxide at thickness of 1-1.5 cm, and (c) uniformly mixing, adding 1-3 wt.% corrosion accelerating agent, fermenting for 15-20 days by covering a film on the fermentation tank, drying the fermented organic fertilizer until the water content is 50-55%, granulating, and packaging.
NOVELTY - Producing natural organic fertilizer using tobacco solid waste comprises collecting and sorting tobacco solid waste; drying naturally the tobacco waste, and pulverizing; carrying out high-temperature steam sterilization of pulverized tobacco waste; mixing 60-80 wt.% sterilized tobacco waste, 10-30 wt.% maize straw and 10 wt.% animal manure, and stirring well; adding biological agent into the mixture, stirring evenly and composting fermenting; and composting naturally for 10-15 days, cooling the compost to ambient temperature, drying, and crushing into organic fertilizer.    USE - The method is useful for producing natural organic fertilizer using tobacco solid waste (claimed).    ADVANTAGE - The method uses tobacco waste, and thus solves long-term problem of tobacco cigarette factory, and brings economic benefit and social benefit.    DETAILED DESCRIPTION - Producing natural organic fertilizer using tobacco solid waste comprises (i) collecting and sorting tobacco solid waste, where the waste can be classified into tobacco stems, tobacco powder, broken tobacco pieces and ash stick, which are discarded after burning; (ii) drying naturally the tobacco waste, and pulverizing into a diameter of 0.1-1 cm; (iii) carrying out high-temperature steam sterilization of pulverized tobacco waste, where the sterilization pressure is 102.9 kPa, sterilization temperature is 121-126 degrees C, and the sterilization time is 20-30 minutes; (iv) mixing 60-80 wt.% sterilized tobacco waste, 10-30 wt.% maize straw and 10 wt.% animal manure, and stirring well; (v) adding 0.5-1 wt.% biological agent into the mixture, stirring evenly and composting fermenting, where the biological agent is commercially available compost fermentative bacteria; and (vi) composting naturally for 10-15 days, cooling the compost to ambient temperature, drying, and crushing into organic fertilizer.
NOVELTY - This new type utility claims belongs to the environment protection technical field of a one double-circulation efficient anaerobic reactor. The reactor comprise a tank body, a tank body from the bottom up in turn is provided to the first-stage reaction sludge bed, first-stage three-phase separator, second level sludge bed reaction, second level three phase separator, first-stage sludge reaction and second level sludge bed reaction bed set with gas collecting tube, the gas-liquid separator is connected with the gas-liquid separator through the central pipeline is connected with the water collecting, water collector through circulation outlet is connected with the bottom of the tank body of the water distribution system is connected, a gas-liquid separator top part with the marsh gas compressor. This utility new type is gas-liquid separator and marsh gas compressor can be valid of removing gas generated by fermentation, and can rationally use resource, two level three phase separator structure increases the removal efficiency, a water distribution system using multi-point inlet, a through tube is cleaned, the water circulation system, high efficiency.
NOVELTY - This utility new type relates to a one based on anaerobic filter tank reactor of solar heating, solar power generation through an anaerobic reactor needed of provide power and heating device is set to provide suitable reaction temperature reactor and an outer reactor wall using vacuum glass, it can prevent heat loss to achieve heat preservation. This utility new type has simple structure, energy saving, convenient operation, the residual sludge amount, is suitable for wide range of. The process module has strong popularization, system operation stable, treatment effect is obvious, it can used for processing organic waste water of different concentration.
NOVELTY - A Bacillus mucilaginosus strain deposited as CGMCC N0.7549, is new.    USE - The B.mucilaginosus strain is useful for preparing seaweed bio-fertilizer for promoting growth of foliage (claimed) and improving crop quality.    ADVANTAGE - The prepared bio-fertilizer is convenient and has greater than or equal to 2x 109 colony forming units (CFU)/ml viable B.mucilaginosus cells and hence promote high yield of quality food.
NOVELTY - Preparation of soil remediation active organic fertilizer comprises adding water and proteolytic plant enzyme into meal, hydrolyzing, obtaining hydrolyzate containing active free amino acid, concentrating, drying to obtain meal with 12-15% water content, mixing Hydrilla soil, yellow bran, shellfish powder, bone meal, and shrimp and crab shell powder, inoculating bacteria enzymes in organic materials, fermenting, cooling, air drying, obtaining fermented organic material, blending meal and fermented organic material, adding soil enzymes, mixing and granulating.    USE - Method for preparing soil remediation active organic fertilizer used for promoting crop growth, improving crop yield and soil structure (all claimed) and increasing storage capacity of soil.    ADVANTAGE - The fertilizer has high crop nutrient conversion rate and 1.5-1.8 times increased efficiency.    DETAILED DESCRIPTION - Preparation of soil remediation active organic fertilizer comprises adding water and proteolytic plant enzyme into meal, hydrolyzing, obtaining hydrolyzate containing active free amino acid, concentrating, drying to obtain meal with 12-15% water content, mixing Hydrilla soil, yellow bran, shellfish powder, bone meal, and shrimp and crab shell powder at mass ratio of 0.5-1.5:2-4:1-3:0.5-1.5:0.5-1.5, inoculating bacteria enzymes in organic materials with 40-60% moisture content and 60-40% solids content, fermenting at 40-70 degrees C for 7-15 days, cooling to less than 40 degrees C, air drying at room temperature to reach 20-25% moisture content, obtaining fermented organic material, blending meal containing active free amino acid and fermented organic material at mass ratio of 1-3:7-9, adding 0.5-1 wt.% soil enzymes, mixing and granulating. The soil enzyme comprises urease, phytase, acidic proteolytic enzyme and chitinase at mass ratio of 1-3:3-5:2-4:05-1.5, preferably 2:4:3:1.
NOVELTY - The decomposition method involves performing electrolysis on the electrolytes of water, exceeding the value of the electrode voltage not above a maximally possible value of a potential barrier between the electrodes, which is achieved via constant alternating of electrolysis and non-electrolysis operations. During the generation of hydrogen and oxygen via the electrodes, the counter electromagnetic force and the potential barrier values are reduced as a result of the reduction in power consumption during electrolysis.    USE - Decomposition method of water to hydrogen and oxygen.
NOVELTY - This utility new type relates to a high one fat and oil food processing waste water treatment device set with coarse screen, fine grid, a water collection pool, accident ABR reactor, UBF reaction tank, floatation water inlet multi-section point A/O reaction tank, a secondary sedimentation tank, a coagulation reaction tank, a filter cloth filter pool, contact pool, a sludge concentrating tank, a sludge dewatering machine, a marsh gas desulphurization and burning system, the tail gas deodorizing system. This utility new type for water quality feature and high of concentration in food processing waste water, firstly ABR reactor through multi-grid construction in the form of animal and plant floating oil removing, through adding lime and PAC of the coagulation tank in combination flotation tank, the waste animal and plant oil and so on in forming floc, organic pollutant in waste water of phosphate and calcium ion and aluminium ion reaction to generate phosphate precipitate, then produce micro-bubble of a through floatation, residual oil of impurity flocculation grain is adhered to upper, upper forming flocculating body of water is less than the floating water surface, so as to remove most of animal fats and vegetable oils such as organic pollutant, so oil index reaches the standard, and it reduces subsequent A/O biochemical treatment of load.
NOVELTY - One a walking type full-automatic turner is installed on the fermentation groove rail upper compound fertilizer, mainly include, a truss, a truss upper of turning device is installed on the bottom of the truss walking device installed on the upper truss and the connecting device of the driving device installed on the truss up device connect with the walking of the walking driving device, upper cover plate on the truss end of automatic control box, the shift mechanism of fermentation groove, a driving device, a walking driving device of driving a using mode of the driving motor, a walking driving motor driving chain transmission driving of driving mode, an automatic control box and a turning driving motor, a walking driving motor, control box connecting shift driving motor, a shift driving motor through transmission shaft of chain wheel, chain and machine frame connecting. This utility new type material piling fermenting high, turning yield is large, the material turned completely, the fermentation process the multi-water, stable operation device, the failure rate is very low, in the process, it can control the multi-turning flow line, high utilization rate.
NOVELTY - This utility new type provide the one a biogas reactor bottom structure, include down according to set order of base layer, heat-insulating layer, the fill layer and surface layer, a fill layer fill with hot filling material, a fill layer is embedded with a heating tube. In the utility model, the new type heating tube embedded in the fill layer, no reaction medium directly contacts with the heating medium, the heating tube so as to avoid scaling or winding outer wall hanging condition of all kinds of impurities and prolongs the maintenance period and reduce the maintenance cost.
NOVELTY - The method comprises: denitrification and desulfurization of microorganism sludge using an anaerobic reactor; domestication of the sludge under autotrophic and heterotrophic conditions till the nitrate removal efficiency reaches to 85%; completing domestication process; adjusting the molar ratio of nitrogen and sulfur to be 0.9-2.2:1; controlling the temperature of the reactor to be 25-35 degrees C and pH to be 7-8; and maintaining hydraulic retention time for 6-12 hours until complete removal of carbon, nitrogen and sulfur in the wastewater.    USE - The method is useful for removing sulfur, carbon and nitrogen in wastewater (claimed).    ADVANTAGE - The method is capable of removing sulfur, carbon and nitrogen in wastewater in an economical and environmental-friendly manner.    DETAILED DESCRIPTION - The method comprises: denitrification and desulfurization of microorganism sludge using an anaerobic reactor; domestication of the sludge under autotrophic and heterotrophic conditions till the nitrate removal efficiency reaches to 85%; completing domestication process; adjusting the molar ratio of nitrogen and sulfur to be 0.9-2.2:1; controlling the temperature of the reactor to be 25-35 degrees C and pH to be 7-8; and maintaining hydraulic retention time for 6-12 hours until complete removal of carbon, nitrogen and sulfur in the wastewater.
NOVELTY - Treating livestock biological sewage comprises: washing livestock contaminations of livestock house in a marsh gas tank; separating biogas slurry and biogas from the marsh gas tank by a dry-wet separation process; diluting the separated biogas slurry; adding the diluted biogas slurry into Chlorella cultivation tank; centrifuging the added slurry to obtain a solution; concentrating the obtained to make a chlorella liquid and clean water separately; and returning the clean water to livestock house and again recycling the diluting step.    USE - The method is useful for treating livestock biological sewage, where separated biogas sludge is used as fertilizers, and as a bio-feed for animals (all claimed).    ADVANTAGE - The method is capable of environmental friendly, economically and efficiently treating livestock biological sewage with improved utilization rate of biogas slurry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for livestock biological sewage treatment system comprising marsh gas tank, livestock, manure separator, diluting tank, liquid pump, a small ball algae cultivation tank, algae liquid separating machine, clear water tank connected to the livestock house through a water pump and centrifugal water separator for returning clean water to the livestock house after washing the livestock.
NOVELTY - Recycling domestic waste material comprises adding domestic waste and/or waste stacking cultivation in a fermentation tank and then fermenting, adding effective microorganisms (EM) fermenting solution into the fermentation raw material to ferment, culturing rear waste as culture maggot and fermented raw material into a culture medium, adding the culture base material into maggot fly eggs or fly bait into the culture medium to culture, and collecting culture of adult fly maggot and then adding into EM fermentation liquid and then culturing and fermenting in earthworm culture medium.    USE - The method is useful for recycling domestic waste material, which is useful as organic fertilizer for planting grain and crops (claimed).    ADVANTAGE - The method is capable of simply and economical recycling domestic waste material.    DETAILED DESCRIPTION - Recycling domestic waste and waste material comprises adding domestic waste and/or waste stacking cultivation in a fermentation tank and then fermenting, adding effective microorganisms (EM) fermenting solution into the fermentation raw material to ferment, culturing rear waste as culture maggot and fermented raw material into a culture medium, adding the culture base material into maggot fly eggs or fly bait into the culture medium to culture for 2-5 days to obtain adult fly maggot, collecting culture of adult fly maggot and then adding into EM fermentation liquid and then culturing and fermenting in earthworm culture medium, adding earthworm to culture for 2-4 months to obtain adult earthworms, and collecting the culture of earthworm and then drying until water content is less than 5%, crushing and sieving.
NOVELTY - A one kitchen garbage automatic sorting of device, include a large object sorting machine, set with multi-set large object sorting machine main body upper part are the same to the multi-angle disk group to rotate, one end of multi-angle disk group of connecting spiral conveying machine, and the other end multi-disk set of angle is large object discharge, the feeding port-collecting conveying device and the crushing machine of the multi-angle regulation disk of lower part set with material conveying device is connected, the feeding outlet and the fine light sorting machine of crushing of humidifying machine is connected with the fine light sorting machine of discharging port through the feeding pipeline of the fine sand type sorting machine is connected with the coarse material sorting machine the discomfort fermentation of big material roll, is suitable for fermentation of the material entering into the crushing air humidifier and sorting heavy material sinks to the bottom discharging slurry through tank side pipeline of humidifying machine input in the crushing machine to fine light separating filter, removing the rear light, is suitable for fermentation of slurry entering into storing groove has simple structure, high degree of automation and high sorting speed is fast, clean of.
NOVELTY - Recycling and regenerating waste gas by metal-organic chemical vapor deposition (MOCVD) comprises (a) introducing exhaust gas generated by MOCVD into water; (b) cooling water containing exhaust gas of MOCVD, storing ammonia in water, and removing impurities; and (c) raising the temperature of the ammonia-containing water to escape ammonia. The MOCVD process comprises removing nitrogen, hydrogen, methane and impurities of waste gas to produce recycling ammonia gas and achieves the purpose of recycling of waste gas.    USE - The method is useful for recycling and regenerating waste gas by metal-organic chemical vapor deposition (claimed).
NOVELTY - Carbon molecular sieve preparation involves crushing raw materials to obtain particles of 1-2mm, where carbon content of agricultural waste is more than 80%. Agricultural waste and adhesive are mixed and extruded in mass ratio of 1-2:1 to obtain mixture. The obtained mixture is mixed with crushed material, phenolic resin, coal tar, asphalt, humic acid, molasses or their mixture. The obtained mixture is heated at 300-500 degrees C in a tubular furnace under inert atmosphere for 30 minutes to 1 hour, and then heated at 5-10 degrees C/minute to obtain mixture.    USE - Method for preparing carbon molecular sieve used for separating carbon dioxide and methane (claimed).    ADVANTAGE - The method enables to prepare carbon molecular sieve that has high absorption selectivity (65-73%) and adsorption capacity.    DETAILED DESCRIPTION - Carbon molecular sieve preparation involves crushing raw materials to obtain particles of 1-2mm, where carbon content of agricultural waste is more than 80%. Agricultural waste and adhesive are mixed and extruded in mass ratio of 1-2:1 to obtain mixture. The obtained mixture is mixed with crushed material, phenolic resin, coal tar, asphalt, humic acid, molasses or their mixture. The obtained mixture is heated at 300-500 degrees C in a tubular furnace under inert atmosphere for 30 minutes to 1 hour, and then heated at 5-10 degrees C/minute to obtain mixture. The obtained mixture is cooled at room temperature, and then washed with water. The obtained product is immersed in solution containing organic amine for 2-4 hours, and then dried in a vacuum oven at 80-100 degrees C. The sample is placed in a microwave oven for 0.5-1 hour under nitrogen atmosphere at 400-500 Volt, and then sample is placed at 800-1000 degrees C for 0.5-1 hour. The obtained sample is heated at 5-10 degrees C/minute, and then cooled at room temperature to obtain desired product.
NOVELTY - This utility new type claims a with one device of hydraulic marsh gas tank, marsh gas tank is easy to solve the problem that structure of shell and acidification and include the tank body, a tank body set with feeding channel, discharging channel and a biogas outlet, a tank body upper part is gas storage room, the lower part is a fermentation room, a discharge hole channel and one water pressure chamber connected in the tank body set with a device, a device one end a water pressure chamber is set on the upper part, and the other end through a water pressure chamber, a discharge channel and a fermentation room extends to the said gas storage room, the said band pulling device of slag overturning device for hydraulic biogas pool equipment is simple, the cost is low, does not need many or very complex of device, operation is simple, it does not need open marsh gas tank seal cover, it only needs to toggle one end device is set on the water pressure chamber of the cracking, it can improve the utilization rate of the raw material in the marsh gas tank and reduces the disease pool incrustation caused by the problem of waste tank, the marsh gas utilization rate, reduces the pollution and improves the ecological effect.
NOVELTY - This utility new type claims a new-type straw rotten one generating device, said device include the fermentation cylinder body, the generating core, monitoring system and storage device. Said fermentation tank body with heat preservation layer and seal layer. Said fermentation tank comprises a tank body heat preservation layer, a material inlet, a outlet and discharging device, a power generating core include semiconductor generating sheet array, cooling circuit, said monitoring system include gas sensor, temperature detector, an alarm and controller. Crop straw and kitchen garbage of this utility new type can be used for compost, silage, marsh gas and self-heating edible fungus culture medium production process, and matched, it can fully take use of corn, wheat, rice, sweet potato, soybean, cotton seed skin and so on organic matter decomposed in the process of high temperature produce a power generation, improves the energy utilization rate.
NOVELTY - An Agaricus blazei culture material comprises 20-30 pts. wt. sugar cane bagasse, 30-40 pts. wt. crop straw, 15-20 pts. wt. livestock and poultry manure, 5-10 pts. wt. bran or wheat bran, 3-5 pts. wt. cake fertilizer, 3-5 pts. wt. corn flour, 1 pt. wt. gypsum powder, 1 pt. wt. lime powder, and 60 pts. wt. water.    USE - Agaricus blazei culture material.    ADVANTAGE - The method achieves comprehensive utilization of agricultural waste which effectively reduces environmental pollution with good economic and ecological benefits and has good application prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of material by chopping crop straw into 15-20 mm long, pre-wetting with water, mixing with sugar cane bagasse, livestock and poultry manure, bran or wheat bran, cake fertilizer, corn flour, gypsum powder, and lime powder, performing compost fermentation, and heating with steam at 50-55 degrees C to carry out secondary fermentation for 3-5 days.
NOVELTY - A seed cultivation matrix comprises fermented agricultural waste, garden soil and perlite at 2:0.8-1.2:0.8-1.2 volume ratio.    USE - Seed cultivation matrix used for Camellia rosthorniana (claimed).    ADVANTAGE - The method promotes strong plant growth vigor, fast seedling speed and prolonged florescence. It is low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of seed cultivation comprising preparing seedling basin, placing seed cultivating matrix, adding seedlings, layering with cultivating matrix, compacting, irrigating, adding 3-5 g slow-release fertilizer from April to May, and adding 25 g cake fertilizer from October to November.
NOVELTY - Preparation of liquefied plant growth regulator comprises collecting litter of leaves, oven drying at 41-57 degrees C, crushing to 200-450 mesh, standing for 35-56 minutes, placing phenol in water bath, heating at 50-80 degrees C for 10-21 minutes, pouring liquid phenol into reaction vessel, adding litter powder, reacting at 85-110 degrees C, stirring, adding concentrated nitric acid and hydrogen peroxide, stirring for 50-75 minutes until color changes dark red, adding sodium dodecylbenzenesulfonate, stirring, cooling and sealing.    USE - Method for preparing liquefied plant growth regulator (claimed) used for promoting growth of plants and protecting against diseases.    ADVANTAGE - The method is safe, simple, energy-saving, cost-saving and environment-friendly.    DETAILED DESCRIPTION - Preparation of liquefied plant growth regulator comprises collecting litter of leaves, oven drying at 41-57 degrees C, crushing to 200-450 mesh, standing for 35-56 minutes, placing phenol in water bath, heating at 50-80 degrees C for 10-21 minutes, pouring liquid phenol into reaction vessel, adding litter powder, reacting at 85-110 degrees C, stirring, adding concentrated nitric acid and hydrogen peroxide, stirring for 50-75 minutes until color changes dark red, adding sodium dodecylbenzenesulfonate, stirring where weight ratio of litter powder, phenol, concentrated nitric acid, hydrogen peroxide and sodium dodecylbenzenesulfonate is 3-5:8-12:0.1-0.3:0.1-0.3:0.3-0.5, cooling and sealing. Liquefied plant growth regulator comprises 19-40 wt.% forest litter and 60-81 wt.% solvent where solvent is methanol or ethanol.
NOVELTY - An insecticidal bioorganic fertilizer used for strengthening disease resistance, comprises 13-23.5 pts. wt. eucalyptus leaves, 20-25 pts. wt. tobacco stem, 20-25 pts. wt. marigold stem, 15-18 pts. wt. radix sophorae flavescentis, 17-22.5 pts. wt. wool soil amendment, 1-2 pts. wt. mixed bacterial culture and 1.5-2.5 pts. wt. potassium carbonate.    USE - Insecticidal bioorganic fertilizer used for strengthening disease resistance (claimed) and promoting plant growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of insecticidal bioorganic fertilizer comprising (A) taking eucalyptus leaf, tobacco stem, marigold stem, radix sophorae flavescentis and wool soil amendment, mixing, and crushing; (B) preparing Actinomyces slant culture medium, preparing Actinomyces liquid culture medium, inoculating slant with Actinomyces, activating, and culturing; (C) preparing photosynthetic bacteria slant culture medium, preparing photosynthetic bacteria liquid culture medium, inoculating photosynthetic bacteria, activating, and culturing; (D) preparing yeast slant culture medium, preparing yeast liquid culture medium, inoculating yeast, activating, and culturing; (E) harvesting cultures, mixing, spraying on crushed raw materials, stirring, fermenting aerobically for 8-15 days, adding potassium carbonate, and regulating pH; and (F) drying, crushing to 40-100 mesh, sieving, and packaging.
NOVELTY - High and low pressure twin tower demethanizer and deethanizer rectifying process comprises feeding l-3C hydrocarbon comprising methane, ethylene, propylene, hydrogen and carbon monoxide in middle part of demethanizer, controlling demethanizer pressure, tower top temperature, and tower bottom temperature, heating through reboiler, removing all methane; pumping 2-3C hydrocarbon from demethanizer tower bottom to deethanizer tower, controlling operation pressure, tower top temperature, and tower bottom temperature.    USE - Method for high and low pressure twin tower demethanizer and deethanizer rectifying process (claimed).    ADVANTAGE - The method does not need refrigerant and refrigeration device for separation process of methane and ethylene, thus reducing operating cost and investment.    DETAILED DESCRIPTION - High and low pressure twin tower demethanizer and deethanizer rectifying process comprises feeding l-3C hydrocarbon comprising 5-15% methane, 22-42% ethylene, 40-60% propylene, hydrogen and carbon monoxide in middle part of demethanizer at - 8-- 30 degrees C, controlling demethanizer pressure to 1.7-2.4 MPaG, tower top temperature to - 32-- 41 degrees C, and tower bottom temperature to 10-22 degrees C, where tower theoretical plate number is greater than or equal to 35, heating through reboiler provided on demethanizer, removing all methane; pumping 2-3C hydrocarbon from demethanizer tower bottom to deethanizer tower, controlling operation pressure to 2.5-2.8 MPaG, tower top temperature to - 10-- 18 degrees C, tower bottom temperature to 58-70 degrees C, where tower theoretical plate number is greater than or equal to 35, heating through reboiler to obtain less than 0.2% 3C content of ethylene and ethane and less than 0.4% 2C content of propylene and propane.
NOVELTY - Preparing 4-N-di-tert-butyl dicarbonate(boc)-amino-cyclohexanone comprises adding 4-amino cyclohexanol hydrochloride, polyguanidine and boc anhydride into a reaction kettle, reacting the mixture at room temperature for 12-24 hours, washing the mixture by water, drying the mixture to remove solvent to obtain white solid 4-N-boc-amino cyclohexanol, adding obtained 4-N-boc-amino cyclohexanol and acid to sodium hypochlorite or sodium chlorite solution, stirring reaction mixture, separating the organic layer, washing the mixture by water, and drying to remove dichloromethane.    USE - The method is useful for preparing 4-N-boc-amino-cyclohexanone, 3-N-boc-amino-cyclohexanone and 3-N-boc-cyclopentanone (claimed).    ADVANTAGE - The method is capable of simply economically preparing the 4-N-boc-amino-cyclohexanone in an eco-friendly manner with high yield and stability.    DETAILED DESCRIPTION - Preparing 4-N-di-tert-butyl dicarbonate(boc)-amino-cyclohexanone comprises adding 4-amino cyclohexanol hydrochloride, polyguanidine and boc anhydride according to mass ratio of 1:2:1.5 into a reaction kettle, reacting the mixture at room temperature for 12-24 hours, washing the mixture by water, drying the mixture to remove solvent to obtain white solid 4-N-boc-amino cyclohexanol, adding obtained 4-N-boc-amino cyclohexanol and acid to sodium hypochlorite or sodium chlorite solution, stirring reaction mixture for 1-2 hours, separating the organic layer, washing the mixture by water, and drying to remove dichloromethane.
NOVELTY - 2,4-dibasic thiophene derivative (I) is new.    USE - 2,4-Dibasic thiophene derivative used for preparing antibacterial agent (claimed).    ADVANTAGE - The simple and eco-friendly preparation ensures high yield.    DETAILED DESCRIPTION - 2,4-dibasic thiophene derivative of formula (I) is new.    R3=optionally substituted phenyl or naphthyl;    R1=1-20C alkyl, benzyl or R3; and    R2=methyl or ethyl.
NOVELTY - Preparation of 7-amino-3-chloro-cephalosporin ring-4- carboxylic acid (I) comprises reacting 7-amino-3-chloro-3-cephem-4-carboxylic acid diphenylmethyl ester (II), dehydrated dimethyl formamide, thionyl chloride, and dimethyl sulfone, cooling, filtering, washing with water, and vacuum drying; reacting with p-cresol, extracting, concentrating, crystallizing, crystal for filtering, drying; and reacting with immobilized penicillin G acylase IPA-750, crystallizing, filtering, and vacuum drying.    USE - Method for the preparation of 7-amino-3-chloro-cephalosporin ring-4- carboxylic acid (I) (claimed).    ADVANTAGE - The method has mild reaction condition, uses inexpensive raw materials, is energy-saving, has high product yield, and is inexpensive.    DETAILED DESCRIPTION - Preparation of 7-amino-3-chloro-cephalosporin ring-4- carboxylic acid (I) comprises reacting 7-amino-3-chloro-3-cephem-4-carboxylic acid diphenylmethyl ester (II), dehydrated dimethyl formamide, thionyl chloride, and dimethyl sulfone to obtain 7-phenylacetylamino-3-chloro-cephalosporin-4-carboxylic diphenylmethyl ester (III), cooling, filtering, washing with water, and vacuum drying; removing benzophenone by reacting (III) and p-cresol to obtain 7-phenylacetamido-3-chloro-3-cephalosporin -4-carboxylic acid (IV), extracting, concentrating, crystallizing, crystal for filtering, drying; and removing acid group by reacting (IV) with immobilized penicillin G acylase IPA-750, crystallizing, filtering, and vacuum drying.
NOVELTY - Anaerobic fermentation of kitchen waste, involves: mixing kitchen waste in water, carbon source and nitrogen source to obtain mixed solution, where the solution of carbon and nitrogen are in a mass ratio of (30-40):1; and preparing from the mixed solution a marsh gas.    USE - For anaerobic fermentation of kitchen waste (claimed) including rice flour and food residual, vegetable, animal and vegetable oil.    ADVANTAGE - The waste water in kitchen waste contains high content of soluble carbohydrate, protein and fat; is good for process of anaerobic fermentation process and improves the yield, but also improve the obtained methane in methane content of greater than or equal to 85%. The method has gas production amount of 383 mL/g. The process maintain good contact of material and microorganism fungus, avoids the anaerobic fermentation system is temperature uniformity, and would not damage normal propagation of bacteria and improve biogas yield.
NOVELTY - A biogas fermentation material comprises: 60-150 pts. wt. livestock excrement, 5-20 pts. wt. effective microorganisms, and 1-10 pts. wt. biogas residue, where the livestock manure includes 20-60 pts. wt. dry chicken manure, 20-60 pts. wt. pig manure and 20-60 pts. wt. dry dairy manure.    USE - As a biogas fermentation material (claimed) for producing methane, hydrogen and carbon dioxide gas.    ADVANTAGE - The biogas fermentation raw material provides faster rate of gas generation; and contains number of beneficial bacteria which converts organic matter into marsh gas in a tank immediately after the start of decomposition and accelerate the hydrolysis process, which is good for forming gas at high speed.
NOVELTY - A biogas fermentation feedstock comprises 60-150 parts livestock manure, 5-20 parts effective micro-organisms (EM) bacteria, 1-10 parts slag, and 10-25 marsh gas waste liquid, where the livestock manure comprises 20-60 parts dry chicken manure, 20-60 parts pig manure, and 20-60 parts dry dairy manure.    USE - As biogas fermentation feedstock for marsh gas tank (claimed).    ADVANTAGE - The biogas fermentation feedstock provides fast gas generating speed and high utilization rate.
NOVELTY - A methanol fuel composite additive comprises 15-40 wt.% 2-ethylhexanol, 10-25 wt.% ethylene glycol monobutyl ether, 0.5-10 wt.% lanolin fatty acid isopropyl ester, 1.5-12 wt.% lanolin fatty acid methyl ester, 10-40 wt.% polyisobutylene, 5-15 wt.% antioxidant and 8-20 wt.% xylene.    USE - Methanol fuel composite additive used for vehicle.    ADVANTAGE - The composite additive is corrosion retardant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol fuel composite additive comprising mixing all raw materials, standing, and filtering.
NOVELTY - Alcohol-based gasoline additive comprises 1-3 pts. wt. dimethyl adipate, 0.2-1.5 pts. wt. amyl cyclohexylphenol, 0.5-2 pts. wt. oleic acid, 0.005-0.1 pt. wt. perfluorooctanoic acid, 0.02-0.15 pt. wt. polyisobutylene succinimide.    USE - Alcohol-based gasoline additive used for preventing rubber swelling, corrosion and oxidation in alcohol-based gasoline.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based gasoline additive comprising mixing dimethyl adipate, amyl cyclohexylphenol and oleic acid in reaction kettle, carrying out polymerization reaction at 70-80 degrees C for 1-2 hours, adding perfluorooctanoic acid and polyisobutylene succinimide and incubating at 50-60 degrees C for 0.5-1 hour.
NOVELTY - Waste oil biodiesel technology comprises heating recovered waste oil at 60-80 degrees C, settling, removing impurities, mixing 80-90 pts. wt. methanol and 20-30 pts. wt. waste oil at 40-50 degrees C for 1-2 hours, adding 1-5 wt.% enzyme, reacting at 30-40 degrees C for 18-24 hours, standing for 2-3 hours, separating layers and recovering methanol.    USE - Waste oil biodiesel technology.    ADVANTAGE - The method is simple, easy and has high conversion rate.
NOVELTY - A solar biogas digester comprises main body (1) in which inside of main body has fermentation room (6) with hollow structure, top of main has body has movable cover (2) with same size and shape as main body, movable cover is provided with air tube (3), upper part of main body has turning cover, upper half of main body and inner surface of turning cover has solar panel (8), lower half of main body has stored battery provided with battery box (9), battery box is connected to solar panel through wire, and bottom of fermentation room has heating rod (7).    USE - A solar biogas digester (claimed).    ADVANTAGE - Solar biogas digester greatly improves energy rate and automatically removes residue to avoid further cleaning.    DETAILED DESCRIPTION - A solar biogas digester comprises main body (1) in which inside of main body has fermentation room (6) with hollow structure, top of main has body has movable cover (2) with same size and shape as main body, movable cover is provided with air tube (3), upper part of main body has turning cover, upper half of main body and inner surface of turning cover has solar panel (8), lower half of main body has stored battery provided with battery box (9), battery box is connected to solar panel through wire, bottom of fermentation room has heating rod (7), and heating rod is connected to stored battery through wire.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a solar biogas digester.    Main body (1)    Movable cover (2)    Air tube (3)    Feed inlet (4)    Feed tube (5)    Fermentation room (6)    Heating rod (7)    Solar panel (8)    Battery box (9)
NOVELTY - A Rhizopus stolonifer strain PF102 with preservation number CGMCC NO.8435 is new.    USE - A Rhizopus stolonifer strain PF102 with preservation number CGMCC NO.8435 for preparing biological fertilizer (claimed).    ADVANTAGE - The biological fertilizer improves crop yield, prevents pathogenic bacteria, enhances crop root number, soil bulk density, soil porosity, characteristics and growing conditions of plants.
NOVELTY - Candida tropicalis (Saccharomyces cerevisiae) DLPU-1L-, with a preservation number of CGMCCN0.7784, is new.    USE - The Candida tropicalis is useful for preparing high purity L-valine (claimed).    ADVANTAGE - The method: is simple; has mild conditions and non-polluting production process; and produces the product with high product purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of Candida tropicalis for preparing high-purity L-valine, comprising adding Candida tropicalis DLPU-1L- to L-valine containing fermentation liquor for culture fermentation, after consumption of L-valine, L-leucine, L-alanine and L-isoleucine, removing cells of fermentation clear liquid, adding activated carbon to decolor, then filtering to remove activated carbon, concentrating, crystallizing, using ethanol for crystallizing and rinsing, centrifuging to obtain high purity L-valine wet crystal, and drying obtain high purity L-valine product.
NOVELTY - Preparing yeast particles comprises: inoculating yeast into a carrier material after sterilization; fermenting the yeast with starch; performing filtration under pressure; and drying and compressing.    USE - The method is useful for preparing yeast particles, which is useful for processing organic waste water (claimed).    ADVANTAGE - The method is capable of effectively, economically preparing yeast particles in a simple and manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of yeast particles for processing organic waste water, where the application method comprises distributing organic waste water into a reactor, dissolving and dispersing yeast in waste water, aerating for 4 hours, standing and depositing for 0.5 hours, then discharging to obtain supernatant, and repeating distribution of organic waste water.
NOVELTY - An Acinetobacter is Acinetobacter baumannii strain DD1 (CCTCC M2013560).    USE - Acinetobacter for degradation of dioxane, phenol, toluene, n-butanol, n-hexane, ethanol, benzene, tetrahydrofuran, or o-xylene (all claimed).    ADVANTAGE - Acinetobacter is aerobic and energy efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) application of Acinetobacter used for degradation of dioxane, phenol, toluene, n-butanol, n-hexane, ethanol, benzene, tetrahydrofuran, or o-xylene; and (2) dioxane degradation which involves inoculating Acinetobacter in dioxane-containing wastewater, introducing into inorganic salt medium containing dioxane or exhaust gas in inorganic culture salt medium, and degrading.
NOVELTY - Synthesizing bio-diesel using lipase-catalyzed method, involves adding oleic acid and methanol in a molar ratio of 1:0.8-1.4, and 5 wt.% immobilized lipase into a petroleum ether system, where the temperature is 28-44 degrees C and the reaction time is 24 hours.    USE - For synthesizing bio-diesel (claimed).    ADVANTAGE - The method has industrial conversion rate of 92%.
NOVELTY - A kitchen wastewater is produced by sorting kitchen garbage, subjecting collected garbage to hydrothermal treatment, separating solid kitchen waste, and preparing ethanol. Preparation of ethanol involves adding complex enzyme to solid kitchen waste and fermenting by mixed flora in which complex enzyme is amylase, cellulase, lipase, protease, glucoamylase, or xylanase, mixed flora is Kluyveromyces yeast, Saccharomyces cerevisiae, Pseudomonas, Bacillus subtilis, Aspergillus niger, Rhizopus oryzae, Trichoderma reesei, and Mucor.    USE - Production of kitchen wastewater (claimed).    ADVANTAGE - Hydrolysis is complete, fermentation has high efficiency and good effect, and production process is simple and low-cost, utilizes raw material, and has easy strain.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of production of kitchen wastewater. (Drawing includes non-English language text).
NOVELTY - The device has a compressor refrigeration system provided with a mixed coolant compressor and an interstage cooler. The compressor comprises two compression sections. A pre-cooling system includes a pre-cooling heat exchanger and a refrigerant gas-liquid separator. The compressor is formed with a cooling heat exchanger cold fluid section. A liquid nitrogen outlet of a tower top gas-liquid separator is matched with a reflux liquid inlet of a coolant compressor stage rectifying tower. Nitrogen tower bottom reboiler of the tower is fixed with a hot fluid section of a liquefying heat exchanger.    USE - Coke oven coal liquefied natural gas and hydrogen-rich product manufacturing device.    ADVANTAGE - The device realizes single-tower rectifying process by utilizing single mixed refrigerant and the coolant compressor stage rectifying tower and utilizes the coolant compressor and the rectifying tower so as to reduce product manufacturing cost and energy consumption. The device is convenient to realize parking operation, and has better comprehensive economic benefits, and increases coke oven coal rear pressure purification rate to about greater than 2.3MPa and coke oven coal processing rate of a liquefying device to about less than or equal to 100 per day purifying coke oven coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a coke oven coal liquefied natural gas and hydrogen-rich product manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a coke oven coal liquefied natural gas and hydrogen-rich product manufacturing device.'(Drawing includes non-English language text)'
NOVELTY - Producing biogas and/or methane, comprises (a) providing a slurry comprising one or more solid spent product(s) and a liquid which possesses a high bicarbonate alkalinity, (b) subjecting the slurry to an anaerobic digestion comprising methanogenesis at a pH of 6.6-7.6 to obtain a biogas and liquid digestate, and (c) optionally further processing the biogas to obtain methane.    USE - The process is useful for producing biogas and/or methane (claimed).    ADVANTAGE - The process simply prepares biogas and/or methane using pot ale or other concentrated syrup, which saves costs and physical sizes of the digesters, and wide range of different starting substrate materials such as waste products from a malt/grain distilling, by efficiently controlling the anaerobic processes to provide a specific set of conditions for each particular substrate being digested.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system, preferably an anaerobic digestion system, for digestion of a substantially aqueous solution, or aqueous and oil two phase system and digestion of one or more solid spent product(s), comprising a first anaerobic reactor for anaerobically treating the substantially aqueous solution or aqueous and oil two phase system, to produce biogas and a liquid digestate with a high level of bicarbonate alkalinity and a second anaerobic digester for anaerobically digesting one of more solid spent product(s) which are provided to the digester in the form of a slurry comprising the solid spent product(s) and the liquid digestate from the first anaerobic reactor.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of a solid digestion process for producing biogas and/or methane.    Slurry vessel (28)    Digester (44)    Internal deformable gas hood (46)    Whole digestate (56)    Fiber/liquor separation phase. (58)
NOVELTY - Process for producing health beneficial probiotic composition from lactic acid bacteria and bifidus bacteria, involves (a) selecting the lactic acid and bididus bacterial strains, (b) fermenting and recovering biomass of the lactic acid and bifidus bacteria, (c) collecting biomass and creating drying material, and (d) producing the composition.    USE - The process is useful for production of health beneficial probiotic composition from lactic acid and bifidus bacteria.    ADVANTAGE - The production process is based on non-heated and low-temperature vacuum-drying method, and hence obtained probiotic composition has viable microbial cells proportion up to 30-60%, and low production cost.
NOVELTY - Method for saccharifying enzyme using lignocellulosic raw material, involves adding lignocellulosic raw material to aqueous solution containing saccharogenic amylase, where the process in carried out in culture tank, and concentration of solid material contained in raw material discharged from discharge port of culture tank is 12 %mass or less.    USE - The method is useful for saccharifying enzyme, which is useful for preparing saccharides and ethanol (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enzyme saccharification fermentation method of lignocellulosic raw material, which involves performing fermentation and enzyme saccharification in parallel using fermenting microorganism to ferment substrate sugars.
NOVELTY - Microspheroidal Fischer-Tropsch iron catalyst comprising silicon to aluminum of oxide as carrier and surface activity component, where the catalyst is present in an amount of 30-70 wt.%, is new.    USE - The microspheroidal Fischer-Tropsch iron catalyst is useful for synthesizing heavy hydrocarbon (claimed).    ADVANTAGE - The microspheroidal Fischer-Tropsch iron catalyst has high selectivity.    DETAILED DESCRIPTION - Microspheroidal Fischer-Tropsch iron catalyst comprises silicon to aluminum of oxide as carrier and surface activity component of formula ((Fe100AaB1bZncOx)), is new. The catalyst is present in an amount of 30-70 wt.%.    A = alkali metal;    B1 = Cu or Mn;    a = 0.1-10;    b = 5-60;    c = 0.1-15; and    x = oxygen atom.    INDEPENDENT CLAIMS are included for:    (1) preparing microspheroidal Fischer-Tropsch iron catalyst; and    (2) use of microspheroidal Fischer-Tropsch iron catalyst for synthesizing heavy hydrocarbon.
NOVELTY - Producing methane by transforming carbon dioxide in activation reservoir using methanogenic bacteria, comprises (i) analyzing target reservoir fluid with presence of bacteria of Syntrophomonadaceae or Thermotogaceae, at least one of the bacteria is Methanobacterium, Methanothermobacter, Methanolinea, Methanospirillum, Methanoculleus, (ii) injecting acetic acid or acetate in the reservoir, making acetic acid or acetate concentration in the reservoir to be 5-10 mM, and (iii) producing methane.    USE - The method is useful for producing methane by transforming carbon dioxide in activation reservoir using methanogenic bacteria (claimed).    ADVANTAGE - The method can greatly improve carbon dioxide reduced methane production rate, is economical, and has simple processing technique.
NOVELTY - This utility new type relates to in purified gas of device, especially a natural gas acid gas of one device. Wherein the series include first absorption tower (1), a second absorption tower (2), the third absorbing tower (3), absorption tower (4), fourth fifth absorption tower (5) and the sixth absorption tower (6), wherein the first absorption tower (1) is set with gas inlet and the sixth upper tower (6) is set with upper natural gas outlet are set with lean amine liquid inlet on the tower top six, further include in series first regeneration tower (7), regeneration tower (8), the third second regeneration tower (9) and fourth regeneration tower (10), the first regeneration tower (7) is set with acid outlet, set with reboiler beside the fourth regeneration tower (10) bottom (14). Through probation proves that, this utility new type of device capable of solving the problem that the traditional amine method of removing acid gas device in the lifting, installation and transportation is not convenient is not safety of.
NOVELTY - Desulfurization and denitrification method involves (a) preparing ammonium hydroxide and sulfur dioxide, reacting ammonium hydroxide with sulfur dioxide to form ammonium sulfite, and oxidizing ammonium sulfite to obtain ammonium sulfate, (b) preparing nitrogen oxide, and oxidizing nitrogen oxide to form nitrogen dioxide, and (c) preparing ammonia water, and reacting ammonia water with nitrogen dioxide to form ammonium nitrate.    USE - The desulfurization and denitrification method is useful for preparing fertilizer composition, preferably nitrogen fertilizer (all claimed).    ADVANTAGE - The method is simple, saves 5-10 times of cost compared to existing method, and environmentally-friendly, and produces high yield.
NOVELTY - Treatment of printing and dyeing sewage using mixed fungi comprises inoculating Gloeophyllum trabeum and Phanerochaete chrysosporium fungi in seed medium for 6 days, fermenting in fermenting medium at concentration of 10% for 4 days, inoculating in printing and dyeing sewage at concentration of 10-30%, diluting 10 times and standing for 3 days.    USE - Method for treating printing and dyeing sewage using mixed fungi used for reducing chemical oxygen demand and removing color.    ADVANTAGE - The method has high chemical oxygen demand removal.
NOVELTY - The solar garbage fermentation device has fermentation system which is provided to accommodate the processing waste in fermentation chamber (1). The upper portion of fermentation chamber is arranged with throwing door (11). The liquid from fermentation chamber is entered into through hole of liquid storage tank. The outlet of exhaust tube is connected to inlet of fan (5). The outlet of fan is connected to outside of waste gas treatment system. The fermenting chamber is arranged with regular spray for spraying of microorganism with spray device.    USE - Solar garbage fermentation device.    ADVANTAGE - The energy consumption of the solar garbage fermentation device can be reduced. The uniform distribution and high efficiency of microorganism can be ensured. The rotten degree of garbage fermentation compost can be controlled efficiently. The high efficiency of the degradable garbage is achieved, so that the garbage decrement can be processed to 70-80%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solar garbage fermentation device.    Fermentation chamber (1)    Fan (5)    Throwing door (11)    Spraying tube (42)    Human body infrared sensing switch (51)
NOVELTY - Method for preparing organic fertilizer using biogas slurry curing process involves crushing crop straw, and adding biogas slurry, adding the mixture into stirring tank, performing mixed aerobic fermentation process, and complex fermentation process in fermentation tank, granulating the fermented mixture, and packing the obtained product according to existing conventional method.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare product which is environmentally-friendly, and rich in nitrogen, phosphorus and potassium nutrient elements.
NOVELTY - Method for processing agricultural waste using phthalate, involves pulverizing plant residues comprising phthalate esters (PAEs), mixing pulverized plant residues with livestock manure in a ratio of 1:(1-10), adding water to mixture to adjust water content of the mixture to 55-65%, forming a uniform mixture of the pile, placing the pile in a sealed container or enclosed composting sites, and composting the pile for 10-50 days to obtain clinker.    USE - The method is useful for processing agricultural waste using phthalate (claimed).    ADVANTAGE - The method is simple and cost-effective, and has excellent economic value.
NOVELTY - The method involves cooling and crystallizing ammonium sulfate slurry (1). The enough liquid level and buffer volume of slurry storage on ammonium sulfate slurry buffer tank is maintained. The secondary ammonia is added to maintain granulating material of neutralization degree. The granulating material is covered after performing sieving and cooling process of granulating material. The water in the granulating material is reduced to 2.5%, so as to reduce extraction particle size of product and store to warehouse.    USE - Nutrient regulating method of diammonium phosphate product used in phosphogypsum residue field.    ADVANTAGE - The valid diammonium phosphate product phosphorus extraction reducing nitrogen can be promoted, and also the stable product mass can be maintained. The treatment cost and environment protection pressure can be reduced and thus the phosphogypsum residue field use life can be prolonged. The product total nitrogen amount can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for passing ammonium sulfate slurry to the tubular reactor preparing groove (3) or washing liquid collecting groove (5) through gas feeding pump (4), when diammonium phosphate product nutrient is offset high time. The ammonia scrubber cleaning solution density containing washing liquid is maintained for ammonia washer with neutralizing degree. The granulator ammonia is granulated in tubular reactor mixing head which distribute tube in residence time of slurry. The granulated particle is formed in the granulator through coating and bonding. The content of nitrogen, phosphorus, potassium is distributed.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram illustrating the nutrient regulating method of diammonium phosphate product. (Drawing includes non-English language text)    Ammonium sulfate slurry (1)    Gear pump (2)    Tubular reactor preparing groove (3)    Gas feeding pump (4)    Washing liquid collecting groove (5)
NOVELTY - Bio-organic fertilizer comprises raw materials comprising 100-150 pts. wt. natural laterite, 100-180 pts. wt. rice straw, 10-20 pts. wt. plant ash, 10-15 pts. wt. animal excrement and 0.1-0.2 pts. wt. organic matter decomposing inoculant.    USE - As bio-organic fertilizer.    ADVANTAGE - The fertilizer is prepared using rice straw as main raw material that has wide source of availability, and is easy to obtain, and hence production cost of the fertilizer is low, and air pollution caused by combustion of rice straw is controlled.
NOVELTY - Organic fertilizer comprises straw, coal, weathered coal, peat, powdered rock phosphate, potassium mineral powder, powder, soybean Phellodendron, rice hull, rice, fungus powder, urea and polyacrylamide.    USE - As organic fertilizer.    ADVANTAGE - The fertilizer has long-acting effect and no residue, improved quality, prevents soil borne disease, and is cost-effective, simple and environmentally-friendly.
NOVELTY - Bio-organic fertilizer comprises raw materials containing 35-40 pts. wt. urea, 10-12 pts. wt. calcined lime, 20-25 pts. wt. ammonium dihydrogen phosphate, 9-11 pts. wt. potassium dihydrogen phosphate, 25-30 pts. wt. goose dung, 25-30 pts. wt. pig manure, 15-20 pts. wt. dairy manure, 10-25 pts. wt. rice straw powder, 0.1-0.3 pts. wt. Rhodococcus powder, 3-9 pts. wt. potassium sulfate, 15-20 pts. wt. straw powder, 0.1-0.3 pts. wt. Aeromonas powder, 10-15 pts. wt. clamshell powder, and 15-20 pts. wt. clam shell powder.    USE - The bio-organic fertilizer is useful for tea leaves (claimed).    ADVANTAGE - The bio-organic fertilizer contains nitrogen, phosphorus, potassium, and trace elements, and provides balanced nutrients.    DETAILED DESCRIPTION - Bio-organic fertilizer comprises raw materials comprising 35-40 pts. wt. urea, 10-12 pts. wt. calcined lime, 20-25 pts. wt. ammonium dihydrogen phosphate, 9-11 pts. wt. potassium dihydrogen phosphate, 25-30 pts. wt. goose dung, 25-30 pts. wt. pig manure, 15-20 pts. wt. dairy manure, 10-25 pts. wt. rice straw powder, 0.1-0.3 pts. wt. Rhodococcus powder, 3-9 pts. wt. potassium sulfate, 15-20 pts. wt. straw powder, 0.1-0.3 pts. wt. Aeromonas powder, 10-15 pts. wt. clamshell powder, 15-20 pts. wt. clamshell powder, 5-9 pts. wt. sawdust powder, 5-9 pts. wt. cypress powder, 0.001-0.002 pts. wt. yeast powder, and 0.001-0.002 pts. wt. actinomycetes powder.
NOVELTY - Preparation of bio-diesel gemini ionic liquid catalyst involves adding acid-functionalized ionic liquid as catalyst, catalyzing mixture of short-chain fatty acids with alcohols at 40-80 degrees C for 3-6 hours, obtaining reaction mixture, cooling obtained reaction mixture to room temperature through gravity settling, layering reaction solution, obtaining lower acid functionalized ionic liquid, and decompressing obtained liquid to remove short chain alcohol under reduced pressure.    USE - Preparation of bio-diesel gemini ionic liquid catalyst (claimed).    ADVANTAGE - The bio-diesel gemini ionic liquid catalyst is efficiently prepared without polluting the environment.
NOVELTY - Preparation of 4-(carbamoyl(5,5,8,8-tetramethyl-6,7-dihydro-2))benzoate involves condensing 5,5,8,8-tetramethyl-5,6,7,8-tetrahydro-2-yl-amine and monomethyl terephthalate and obtaining 4-((4,5,6,7-tetrahydro-5,5,8,8-tetramethyl-2-naphthyl)carbamoyl)benzoate, reacting obtained product with potassium carbonate aqueous solution, heating to reflux, and then acid-precipitating.    USE - Preparation of 4-(carbamoyl(5,5,8,8-tetramethyl-6,7-dihydro-2))benzoate (claimed).    ADVANTAGE - The method efficiently and economically provides 4-(carbamoyl(5,5,8,8-tetramethyl-6,7-dihydro-2))benzoate, without causing pollution to environment.
NOVELTY - Synthesis of pefloxacin mesylate using solid formaldehyde involves taking solid formaldehyde, 85% formic acid and norfloxacin, refluxing, performing methylation reaction under proper temperature, carrying out decompression distillation of unreacted formic acid, directly subjecting intermediate product to salt-forming reaction with methanesulfonic acid, crystallizing, and then re-crystallizing using 83% ethanol solution.    USE - Synthesis of pefloxacin mesylate (claimed).    ADVANTAGE - The pefloxacin mesylate is economically synthesized by environmentally-friendly method with reduced intermediate product loss and formaldehyde dosage amount, and improved yield.
NOVELTY - Operating and diluting evenly mixed straw marsh gas material in specific distribution manner involves: pre-processing a preprocessing straw, crushing into tobacco-like shape, then feeding straw:inoculum:water at a vol. ratio of 1:2:2-4, adding feed liquid and mixing uniformly.    USE - For operating and diluting evenly mixed straw marsh gas material in specific distribution manner (claimed).    ADVANTAGE - The method present method is simple, convenient and fast, thus also saves energy.
NOVELTY - A pit (1) for compositing material comprises upper sealing layer (3) and lower sealing layer (2) that seal composting materials (6) within the pit. The pit is also provided with a U-shaped gas tube (4) for methane, and installed upwards on four edges of the pit walls, forming a U-shaped natural groove (5).    USE - - As a pit for compositing material such as straw, leaves and weeds, to produce methane (claimed).    ADVANTAGE - The pit enables low cost production of biogas, which everyone can easily operate, and use. It represents the most simple, convenient, lowest cost and most safe method for production of biogas. It is suitable for methane production from straw, leaves, weeds, such as full charging fermentation process, and has a simple design.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of membrane stack.    Pit (1)    Lower sealing layer (2)    Upper sealing layer (3)    Gas tube (4)    U-shaped groove (5)    Compositing material (6)
NOVELTY - A method of production of ethanol using high temperature synchronously saccharifying and fermenting (HT-SSF) technique, involves: fermenting Saccharomyces cerevisiae (TIB-S.C Y01) cultures in strain culture medium using lignocellulose raw material as substrate in high temperature synchronously saccharifying and fermenting (HT-SSF) technique, adding substrate within 48 hours, and maintaining the fragrance temperature of 38 degrees C.    USE - For the production of ethanol (claimed) as vehicle fuel.    ADVANTAGE - The process improves yield of ethanol, and is economical.
NOVELTY - Preparing plant fuel involves: (1) drying and crushing water hyacinth, to obtain dry powder; (2) mixing the dry powder with sodium hydroxide solution, to obtain wet powder; (3) mixing the wet powder and water, regulating pH, and then adding liquid cellulase and xylanase, mixing and fermenting to obtain fermentation liquid; (4) filtering the fermentation liquid, distilling the filtrate and recovering the alcohol residue; (5) mixing the residue with residual liquid, to obtain mixture; and (6) drying the mixture and mixing with triglyceride and wax and then granulating.    USE - For the preparation of plant fuel (claimed) e.g. ethanol.    DETAILED DESCRIPTION - A method of preparation of plant fuel using water hyacinth as raw material, involves: (1) collecting and drying the water hyacinth, and then crushing through 40 meshes sieve, to obtain the dry powder; (2) mixing the dry powder with sodium hydroxide solution according to the weight ratio of 1:10, putting in the reaction kettle, heating to 60-80 degrees C, maintaining the temperature for 2-3 hours, cooling, and filtering to remove the alkaline water, to obtain wet powder; (3) mixing the wet powder and water according to the weight ratio of 1:8, regulating pH value to 3-4 using acid, and then adding liquid cellulase and xylanase, mixing uniformly, and fermenting in a fermentation tank at 40-45 degrees C for 20-30 hours, and cooling to obtain fermentation liquid; (4) filtering the fermentation liquid to obtain residue and filtrate, distilling the filtrate and recovering the alcohol residue and residual liquid; (5) mixing the alcohol residue with residual liquid, to obtain mixture; (6) drying the mixture till the water content of 15-20 wt.%, and mixing with triglyceride and wax, and then pelletizing, extruding and granulating.
NOVELTY - Hydrogen peroxide solution and ammonia combined preprocessing of cellulosic biomass raw material comprises mixing biomass having a diameter of 10-100 meshes with 30% hydrogen peroxide aqueous solution (0.2-2 times of biomass), adding the obtained mixture into a pressure reaction container, injecting liquid ammonia (0.2-5 times) at room temperature, heating to 70-190 degrees C, maintaining for 2-30 minutes to release ammonia gas and cooling.    USE - The preprocessed cellulosic biomass raw is useful in producing ethanol or as a feed additive.    ADVANTAGE - The method improves the enzymolysis efficiency and improves monosaccharide and ethanol yield after biomass treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for.
NOVELTY - Producing fuel by ethanol fermentation of cellulose substance raw material comprises saccharifying at cellulose at optimum temperature of 50-60 degrees C, fermenting with yeast at 20-40 degrees C, and picking heat-resistant yeast; breeding the heat-resistant yeast; and mixing the heat-resistant yeast with ordinary yeast, and fermenting.    USE - The method is useful for producing fuel by ethanol fermentation of cellulose substance raw material.    ADVANTAGE - The method adopts direct use of mixed bacterial fermentation, and thus solves the problem of low alcohol yield and production of organic acid byproducts.
NOVELTY - Manufacture of esomeprazole magnesium trihydrate involves adding inorganic alkali and solvent to esomeprazole sodium complex, stirring, separating, acidifying alkaline aqueous layer using solvent, drying, evaporating, forming esomeprazole crude product, dissolving esomeprazole crude product in sodium hydroxide in alcohol solution, adding inorganic magnesium salt aqueous solution, stirring, crystallizing, filtering, 30-40 degrees C and drying for 48 hours.    USE - Manufacture of esomeprazole magnesium trihydrate used for pharmaceutical.    ADVANTAGE - The environmentally-friendly esomeprazole magnesium trihydrate is manufactured efficiently and economically in high yield and purity, and excellent productivity, by simple method.    DETAILED DESCRIPTION - Manufacture of esomeprazole magnesium trihydrate involves adding omeprazole to mixed solution of absolute ethyl alcohol and sodium hydroxide, stirring for 2-3 hours, adding disodium hydrogen phosphate, stirring for 1.5 hours, crystallizing using acetone, stirring, adding titanate and D-diethyl tartrate, reacting for 1-2 hours, evaporating, forming omeprazole sodium complex, adding triethylamine and S-mandelic acid in solvent, stirring for 8-10 hours, filtering, esomeprazole sodium complex, adding inorganic alkali and solvent to esomeprazole sodium complex, stirring for 2 hours, separating, acidifying alkaline aqueous layer using solvent, drying, evaporating, forming esomeprazole crude product, dissolving esomeprazole crude product in sodium hydroxide in alcohol solution, adding inorganic magnesium salt aqueous solution, stirring, crystallizing, filtering, 30-40 degrees C and drying for 48 hours. The inorganic alkali is chosen from sodium hydroxide, potassium hydroxide, sodium bicarbonate and potassium bicarbonate. The solvent (a) is chosen from ethanol, acetone and isopropyl alcohol. The solvent (b) is chosen from ethyl acetate and methylene dichloride.
NOVELTY - The device comprises a fermentation room for stacking to ferment a solid waste material, a hot air pipe provided with a heat source, which is connected to the fermentation room, and a leachate treatment system connected to the fermentation room through a leachate collecting pipes. A biological bacteria spray device including a clean water spray device and biological bacteria spray device are connected to the fermentation room through a spraying pipeline.    USE - The device is useful for fermenting the rubbish (claimed).    ADVANTAGE - The device is capable of fermenting the rubbish using anaerobic fermentation process to reduce damage to the environment.    DETAILED DESCRIPTION - The device comprises a fermentation room for stacking to ferment a solid waste material, a hot air pipe provided with a heat source, which is connected to the fermentation room, and a leachate treatment system connected to the fermentation room through a leachate collecting pipes. A biological bacteria spray device including a clean water spray device and biological bacteria spray device are connected to the fermentation room through a spraying pipeline. A marsh gas collection device including a marsh gas power generating system is connected to the fermentation room and the leachate treatment system through a pipeline. The fermentation room is provided with 28-30 rooms. The heat source is solar air heating device. The fermentation room is provided with a sensor for detecting temperature, humidity and biogas. The fermentation room has a length of 20 m, width of 10 m and height of 6 m, is made of concrete, and has a sealed door.
NOVELTY - Preparing biodiesel comprises adding 4 g of Chinese tallow oil, methanol and molecular sieves with tert-butyl alcohol into a 50 ml conical flask with a stopper, reacting the mixture using enzyme containing Novozym 435 (RTM: Immobilized Candida antarctica lipase B) and Lipozyme (RTM: Lipase from Thermomyces lanuginosus), controlling the reaction temperature, centrifugating the obtained reacted sample, and calculating the conversion rate.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method produces the biodiesel in an eco-friendly manner.
NOVELTY - Method for producing olive cake silage, involves (a) pouring watery oily olive cake extracted from 2-phase olive oil production untouched by human hands in leak-proof hygiene tank, (b) separating olive cakes and cores by passing the cake to core separation unit from the leak-proof pool (tank), (c) homogenizing the separated olive cake and cores in malaxator, (d) separating olive cake paste in 3-phase decanter as raw olive oil, ecological olive cake water and ecological olive cake, and (e) packaging ecological olive cake extracted from decanter as silage.    USE - The method is useful for producing olive cake silage which is useful as fuel, and liquid fertilizer (all claimed).    ADVANTAGE - The method produces olive cake silage having excellent smell, taste, life, flavor and feeding value, and calorific value and which is easily digested, is simple, hygienic, cost-effective and environmentally-friendly, ensures moisture of the oilcake hence prevents deterioration of the oilcake, and consumes minimal energy.    DETAILED DESCRIPTION - Method for producing olive cake silage, involves (a) pouring watery oily olive cake extracted from 2-phase olive oil production untouched by human hands in leak-proof hygiene tank, (b) separating olive cakes and cores by passing the cake to core separation unit from the leak-proof pool (tank), (c) homogenizing the separated olive cake and cores in malaxator by impasting, heating and maturing the mixture, (d) separating olive cake paste in 3-phase decanter as raw olive oil, ecological olive cake water and ecological olive cake, and (e) packaging ecological olive cake extracted from decanter as silage by passing with 55-65% dampness to packaging unit or packing it as silage by drying the extracted ecological olive cake in drying unit.
NOVELTY - Providing a fuel for an engine involves: mixing an alcohol or formic acid with water to produce a wet alcohol; adding in the wet alcohol to form a liquid fuel, a fuel constituent which is soluble in the wet alcohol; and converting, in a container having an interior formed of an armored material, the liquid fuel into a gaseous fuel substance using at least one of heat energy or electrical energy to pressurize the liquid fuel, the gaseous fuel substance exhibiting a higher pressure and lower density than that of the liquid fuel.    USE - For providing a fuel for an engine (claimed).    ADVANTAGE - The fuel conversion unit applies heat and/or electrical energy to pressurize the liquid fuel by thermal expansion and/or conversion to less dense phases to form the gaseous fuel. The formic acid is included in liquid fuel solutions to provide for denaturing of stored fuel or as an odorant and/or to serve with an electronic or optical detector as a more easily detected agent for early detection of incipient fuel leaks.
NOVELTY - Producing 2-5C hydrocarbons from methane, comprises (i) reacting methane with oxygen in the presence of a catalyst 1 in a product gas mixture comprising ethane, ethylene, carbon monoxide and carbon dioxide, and (ii) contacting the product mixture with hydrogen in the presence of a catalyst 2 without prior separation, and hydrogenating carbon monoxide and carbon dioxide to 2-5C hydrocarbons.    USE - The method is useful for producing 2-5C hydrocarbons from methane.    ADVANTAGE - The method: produces increased yield of 2-5C hydrocarbons; and completely eliminates the by-product carbon dioxide.
NOVELTY - Synthesizing silver nanoparticles (SNPs) in the form of silver nanoparticle dispersed nanogel using Fusarium oxysporum by optimizing cultural and physical parameters such as different media, temperature, pH, light intensity, salt concentration, volume of filtrate, and biomass quantity for the synthesis of SNPs, is claimed.    USE - The method is useful for synthesizing SNPs to treating wound healing (claimed) and burn, and treating secondary fungal infection. Test details are described but no results given.    ADVANTAGE - The method effectively synthesizes SNPs in a low-cost and eco-friendly manner, and can be optimized under physico-cultural conditions so as to obtain desired shape, size and mono-dispersed SNPs. The SNPs have antimicrobial activity, multidrug resistant and secondary fungal infections resistant.
NOVELTY - The shed has a sealed food sink area provided with two fences that are divided into an eating area and a host area. The sealed food sink area is arranged with a feeding rack. A destination area is arranged with a side wall that is arranged with a door. The side wall is arranged with a fan that is arranged with a ventilation window. The ventilation window is arranged with the door that is connected to a cow house. A sink region of a ground part is arranged with a fermentation bed.    USE - Ecological milk cow shed.    ADVANTAGE - The shed is compact in structure, environment friendly and convenient to feed, and has small footprint food area. The shed ensures better cow growth.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an ecological milk cow shed.
NOVELTY - An open biogas digester and low pressure transmission system has biogas digester (1) with opening which is sealed with flexible thin film cover (12) to control air passage through air pipe (3), feeding port (11) at both sides of digester opening, discharging port (2), gas pipeline (5) which is equipped with air pump (9), gas pipe terminal and bypass pipe which is connected to pressure control device (4) comprising tank body containing water and is provided with exhaust port opening at upper part, and overflow outlet opening at lower part.    USE - An open biogas digester and low pressure transmission system (claimed).    ADVANTAGE - The system has simple and reliable structure, reduces leakage generated by gas pressure and biogas digesters, and is easy to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the open biogas digester and low pressure transmission system.    Biogas digester (1)    Discharging port (2)    Air pipe (3)    Pressure control device (4)    Gas pipe terminal (5)    Air pump (9)    Feeding port (11)    Film cover (12)
NOVELTY - A corn straw fermentation microbial inoculum contains Phanerochaete chrysosporium fungus, Trichoderma koningii, Bacillus subtilis, Bacillus licheniformis, and Candida tropicalis.    USE - Corn straw fermentation microbial inoculum (claimed).    ADVANTAGE - The corn straw fermentation microbial inoculum is environment-friendly, easy to use, decomposes straw rapidly, improves usage of corn straw, increases corn straw material protein content and nutritional value, and has structural stability, high activity, and high bacteria count.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of corn straw fermentation microbial inoculum which involves inoculating P. chrysosporium fungus, T. koningii, B. subtilis, B. licheniformis, and C. tropicalis in corresponding activated culture medium to obtain generated strains, separately inoculating strains in nutrient broth agar culture medium to obtain 5 bacterial liquid, and mixing bacterial liquids; and (2) fermentation of corn straw which involves mixing corn straw powder with organic nitrogen, composite trace elements, soybean meal, and rapeseed to obtain fermentation substrate with 65-75% water content, mixing 0.15 L activating aqueous solution containing 0.85% sodium chloride (NaCl) and 1% glucose per 100 kg of fermentation substrate, spreading fermentation substrate to thickness of 30-40 cm, scattering corn straw fermentation microbial inoculum, layering with fermentation substrate and corn straw fermentation microbial inoculum alternately until corn straw fermentation microbial inoculum is 10-15% with respect to fermentation substrate, covering with plastic film, fermenting at 28-35 degrees C for 7-10 days in which substrate easily breaks with light rubbing when fermentation ended.
NOVELTY - Synthesizing aromatic nitro compounds comprises dissolving 1:1-5 molar ratio of an aromatic hydrocarbon compound and ceric ammonium nitrate in acetonitrile, mixing, stirring at 60-100 degrees C for 12-72 hours, cooling to room temperature, extracting, drying, and distilling the solvent through a column to give the aromatic nitro compound.    USE - The method is useful for synthesizing aromatic nitro compounds including acetanilide, haloacetanilide, 1-4C-alkyl, 1-3C-alkoxy substituted acetanilide, 1-3C-alkoxy-substituted acetophenone, 2,4-dinitro aryl hydrocarbon compound and 2,6-dinitro aryl hydrocarbon compound (all claimed).    ADVANTAGE - The method easily prepares aromatic nitro compounds using cheap raw materials in an environmentally friendly manner.
NOVELTY - Manufacture of fatty-acid alkyl ester involves reacting fats and oils (1), and lower alcohol (2) reacting in presence of catalyst (3), separating unreacted lower alcohol from reaction liquid (5), reducing moisture content contained in unreacted lower alcohol to 0.05 weight% or less by adsorption treatment, recycling unreacted lower alcohol from raw material, revitalizing the adsorption agent used for adsorption treatment by heat processing and recycling.    USE - Manufacture of fatty-acid alkyl ester e.g. polyunsaturated fatty-acid alkyl ester used for oil e.g. fish oil, marine animal oil and microorganism oil (claimed), pharmaceuticals, biodiesel fuel and health food.    ADVANTAGE - The method efficiently and economically provides fatty-acid alkyl ester, without causing pollution to environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heat-treatment equipment of zeolite.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining the manufacture of fatty-acid alkyl ester.    Fats and oils (1)    Alcohol (2)    Catalyst (3)    Reaction liquid (5)    Glycerol (6)
NOVELTY - Method of preparing poultry droppings coming from poultry farms and poultry production units for subsequent anaerobic fermentation with the production of biogas and organic fertiliser provides for preparation of poultry droppings or dropping mixture to the maximum humidity of 91%, the ratio of carbon:nitrogen:phosphorus 25:1:1, pH 7\|;8.5, the optimum temperature not exceeding 64?oC, depending on the size of the sludge digester, the size of droppings or dropping mixture, comparable to the size of bacteria, adding the activated sludge of anaerobic origin to neutralise the effect of products of sanitisation and vaccination, using the two-stage fermentation.    USE - Agriculture.    ADVANTAGE - Invention enables to bring the substrate to optimum humidity, to create a certain ratio of nitrogen and carbon.
NOVELTY - A benzene compound substituted with specific functional group is reacted with acetamide in presence of metal catalyst, and resulted product is reacted with an aqueous solution in presence of metal catalyst and base, to obtain acetaminophen.    USE - Preparation of acetaminophen (claimed).    ADVANTAGE - The method economically, efficiently and environmentally-friendly enables preparation of acetaminophen with high yield without using strong base and eliminating separation of position isomers.
NOVELTY - Manufacturing saccharified liquid from cellulosic biomass, comprises (a) dissolving lignin by immersing cellulosic biomass in alkali solution, (b) separating cellulosic biomass from alkali solution, (c) feeding separated cellulosic biomass into pre-treating reactor, pre-treating by injecting steam into reactor using steam generator, (d) recovering steam and hexose containing cellulosic biomass, (e) performing enzymatic degradation of pre-treated cellulosic biomass to obtain hexose containing saccharified liquid, and (f) extracting the useful by-product in effluent of step (d).    USE - The method is useful for manufacturing saccharified liquid from cellulosic biomass.    ADVANTAGE - The method removes lignin prior to enzymolysis to improve saccharification efficiency and maximize hexose recovery; and recovers high pressure-steam and prevents energy loss and loss of solids, there by reducing wastewater effluent treatment cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for manufacturing saccharified liquid from cellulosic biomass (Drawing includes non-English language text).    Cellulosic biomass immersion step (S100)    Step of separating cellulosic biomass from alkali solution (S200)    Pre-treatment step (S300)    Step of recovering steam and hexose containing cellulosic biomass (S400)    Enzymatic degradation step (S500)
NOVELTY - The hydrogen generation device has cylindrical cavitator (3) which is filled with water and provided with cathode (1) and anode (2) that are made from stainless steel and have coaxial cylindrical form connected by tube to cavitator circulation water pump (4) connected to cathode and anode pulsed energy source, voltage modulator (5), and hydrogen and oxygen tanks (6,7). The hydrogen and oxygen tanks are connected to pump and cavitators upper part.    USE - Hydrogen generation device using cavitation electrolysis.    ADVANTAGE - Ensures that efficiency of hydrogen generation can be improved by energy effective combination of cavitation and electrolysis, while reducing the hydrogen production costs due to cheap materials.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the hydrogen generation device by cavitation electrolysis.    Cathode (1)    Anode (2)    Cylindrical cavitator (3)    Water pump (4)    Modulator (5)    Hydrogen and oxygen tanks (6,7)
NOVELTY - A waste-treatment apparatus has storage unit for storing organic waste, drying unit for drying organic waste, incinerating unit for incinerating the dried organic waste, decomposition unit for decomposing organic materials contained in organic waste using microorganisms, gas storage unit for storing blast furnace gas produced from decomposition unit, and fuel cell unit for producing electricity by supplying heat generated from drying unit.    USE - Apparatus is used for treating waste.
NOVELTY - Separating ethane or ethylene, comprises (a) forming clathrate of ethylene-hydroquinone by contacting hydroquinone with mixed gas containing ethane and ethylene, and (b) dissociating ethylene from clathrate.    USE - The method is useful for separating ethane or ethylene from mixed gas (claimed).    ADVANTAGE - The method separates ethane or ethylene effectively in single process.
NOVELTY - An earthworm feed contains biodegradable garbage, microbial degradation bacteria, herbal dregs, chicken manure, and sludge.    USE - An earthworm feed (claimed).    ADVANTAGE - Feed is nutritious and promotes growth for earthworms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of earthworm feed which involves mixing raw material, adding water which is 4-6 times the mass of raw materials, decocting for 2-4 hours, and filtering to obtain slag.
NOVELTY - Extraction of enzyme comprises selecting traditional Chinese medicine plant, microprocessing, and ultramicro crushing; selecting enzyme usually cellulose and latex enzyme; adding albumin, dissolve enzyme, and cooling at room temperature; adjusting pH value to 8-8.5; and hydrolyzing at not greater than 60 degrees C.    USE - Method for extracting enzyme (claimed).    ADVANTAGE - The method is short, simple, and environment-friendly.
NOVELTY - Invention relates to agriculture. The method of producing organomineral fertiliser from sewage sludge by composting, wherein sewage sludge is mixed with sawdust (wood processing wastes) in ratio of 1:0.12 by weight or 1:0.61 by volume, or with shredded straw in ratio of 1:0.11 by weight or 1:1.82 by volume, and potassium sulphate is then added to said mixture in amount of 0.2-0.3% by weight of the substrate, followed by composting in piles.    USE - Chemistry.    ADVANTAGE - Invention simplifies and reduces the cost of producing organomineral fertiliser and increases fertilising value of the end product.2 cl, 2 ex
NOVELTY - The method involves performing chicken manure pre-treating and fermenting process. Chicken manure is transfer to a lengthways receiving conveyer belt. Chicken manure stirring process is performed. Carrier strain is added into the stirred chicken manure. Fermenting process of belt displacement fermentation tank is performed. A granulating machine is pressed during chicken manure drying, grading and sieving processes. A lengthways receiving belt is connected with a greenhouse. A bottom part of a chicken coop is fixed with the receiving belt. A belt terminal is provided with a dung scraper.    USE - Environment-friendly large-scale disposable massage comb integrated chicken manure treating method.    ADVANTAGE - The method enables preventing a chicken house from being damaged, reducing disposable chicken manure treating difficulties and effectively realizing environment-friendly large-scale disposable massage comb integrated chicken manure treating process with wide range of applications and better social and economic benefits.
NOVELTY - A Bacillus amyloliquefaciens strain Y10 (CGMCC 8362), is new.    USE - The B.amyloliquefaciens strain Y10 (CGMCC 8362) is useful for synthesizing protease, amylase, and lipase, and degrading organic matter, protein, starch, fat, kitchen garbage, biomass, and organic waste (all claimed).    ADVANTAGE - The B.amyloliquefaciens strain Y10 improves biogas yield of kitchen garbage to 15-40%.
NOVELTY - This utility new type relates to a one for processing of excrement biological fermentation tank is built up one of rear biological fermentation tank, pig or cow wall outside of the normal of each pig or cow rear wall is provided with a waste outlet, the leading lower edge of the excrement fermentation tank up along the horizontal, in the fermentation tank with biological padding, the fermentation tank outer side wall bottom side part is equipped with liquid guide tube. The biological cushion material is composed of wooden meal, rice hull, straw, rice bran and microbial fermentation microbial inoculum, the discharged excrement fermentation tank of pig or cattle, through biological padding so as to fast ferment decomposing to realize harmless. A of the common pig or cow in parallel rows with pig or cattle of scale, the fermenting groove connecting to one strip, is convenient for mechanical maintenance and cleaning ferment pad material. Using the biological fermentation tank processing pig or cattle excrement investment and construction cost and waste maintenance operation cost, the pig or cattle of 100 % field, which fulfills agricultural of combined cycle, and has very high economic value.
NOVELTY - A mung bean bread comprises 400-420 pts. wt. wheat flour, 120-130 pts. wt. oat flour, 10-12 pts. wt. yeast powder, 80-100 pts. wt. mung bean, 40-50 pts. wt. black rice, 40-50 pts. wt. white turnip, 60-70 pts. wt. guava, 50-60 pts. wt. banana, 8-9 pts. wt. liquorice, 6-7 pts. wt. wheatgrass, 5-6 pts. wt. radix bupleuri, 5-6 pts. wt. bark of tree peony root, 5-6 pts. wt. balloon flower, 6-7 pts. wt. radix isatidis, pawpaw, peach seed, 4-5 pts. wt. milk, 120-130 pts. wt. coffee bean, 30-40 pts. wt. wine, 40-50 pts. wt. salt, white granulated sugar, and remainder of water.    USE - Mung bean bread.    ADVANTAGE - The mung bean bread is prepared in a simple and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing mung bean bread, which involves mixing raw materials, heating and decocting, performing water extraction on resultant product for 5-10 times, spray drying resultant product to obtain Chinese medicine, stirring, forming dough, fermenting for 6-8 hours, and baking resultant product to obtain finished product.
NOVELTY - Method of preparation compost from sewage sludge comprises mixing of fresh sewage sludge with the retention period of less than 3 years with the organic component, which is used as sawdust of any tree species, with the addition of bioactivator and subsequent aerobic composting of the resulting mixture, and prior to mixing the components the layering of sawdust with humidity of 30-40% and sewage sludge, which humidity is 79-81% is carried out, in a ratio of 3:1, at that the dust is subjected to bioactivation by spraying with the working solution of preparation EM-1 "Baikal" at a consumption rate of 5 liters per 1 t at its concentration in the working fluid of 0.0001%, in addition, the aerobic composting of the resulting mixture is carried out in storage pits, at that when the temperature of the composted mixture reaches 50-60 degrees C the mixture is incubated for 20 days, after which the break-in of the storage pit is repeatedly carried out for 2 months with the intervals of 15-20 days, followed by aging of compost for 14-15 days.    USE - Agriculture.    ADVANTAGE - Invention enables to provide the low-cost environmentally friendly organic fertiliser, to resolve the problem of disposal of sewage sludge.4 cl, 3 tbl, 2 ex
NOVELTY - The electrolyzer assembly has unit cell which is provided with a membrane electrode assembly comprising a proton exchange membrane interposed between an anode and a cathode. A cathode flow field plate is arranged adjacent to the cathode. An anode flow field plate (100A) is arranged adjacent to the anode. The anode flow field plate is provided with an anode channel (110A) formed for directing water in contact with anode. A cross-sectional area of the anode channel is varied along a portion of length.    USE - Electrolyzer assembly for generating hydrogen and oxygen from water.    ADVANTAGE - The channel width is decreased in the direction of reactant flow along portion of the length of the channel according to natural exponential function, so that the performance and/or efficiency of operation of the electrolyzer assembly can be improved. The localized reactant and/or product flow velocity during electrolyzer operation can be enhanced. The pressure drop along the channel can be reduced. The parasitic loads can be reduced and the overall system efficiency can be improved. The variation in channel width can be designed to adjust or control the localized residency time of the gaseous products in the channels, so that diffusivity of reactants for localized homogeneous concentration can be increased. The efficient removal of products from the cell can be realized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the unitized regenerative fuel cell assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the electrolyzer anode flow field plate.    Anode flow field plate (100A)    Anode channel (110A)    Inlet (116A)    Water supply manifold opening (120A)    Discharge manifold opening (130A)
NOVELTY - The composter has a cylindrical shaped body, and an inner casing, where a rotation axis of the cylindrical shaped body passes through a composter ventilation tube on which a vane turner is mounted.    USE - Thermally insulated rotary self-shoveling composter.
NOVELTY - Tobacco waste production process involves collecting tobacco waste, separating at high temperature high pressure, and fermenting and performing fumigation for disinfection to obtained decomposed material. The decomposed material, perlite and vermiculite are mixed in mass ratio of 60-70:10-30:10-30 to obtain a substrate, which is applied to grow seedling. Fermentation process is performed by mixing tobacco waste, nutrient source material and auxiliary material in mass ratio of 70-75:10-20:10-20, where water content and additives are adjusted to 50-60% and 0.5-1% respectively.    USE - Tobacco waste production process used for seedling substrate (claimed).    ADVANTAGE - The tobacco waste production process provides good seedling rich in nutrient source in an economic and cost-effective manner.    DETAILED DESCRIPTION - Tobacco waste production process involves collecting tobacco waste, separating at high temperature high pressure, and fermenting and performing fumigation for disinfection to obtained decomposed material. The decomposed material, perlite and vermiculite are mixed in mass ratio of 60-70:10-30:10-30 to obtain a substrate, which is applied to grow seedling. Fermentation process is performed by mixing tobacco waste, nutrient source material and auxiliary material in mass ratio of 70-75:10-20:10-20, where water content and additives are adjusted to 50-60% and 0.5-1% respectively. The mixture is fermented in fermenting tank with stirring 2 times at 45-55 degrees C for 5-10 days, and then the material is dried and packaged to obtain finished product.
NOVELTY - An anti-fouling composition comprises 55-80 wt.% copper flake or cuprous oxide, 10-30 wt.% a film-forming resin selected from high molecular weight water resistant acrylic resin and a vinyl resin, 1-7 wt.%, preferably 2-5 wt.%, especially 3 wt.% rosin, and 0.5-5 wt.% fumed silica and/or fluorinated resin.    USE - As anti-fouling composition useful for application to a marine propeller; and applying antifouling coat to a metallic marine structure such as a marine propeller (claimed).    ADVANTAGE - The composition provides protection against fouling for boat propellers.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a composition for application to a surface comprising the anti fouling composition and a solvent selected from methylethylketone, xylol and/or toluol in a weight ratio of solvent to antifouling composition of 1:1 to 2:1;    (2) a composition for application to a marine propeller comprising the anti fouling composition and a mixture of tert butyl acetate and acetone in a weight ratio of 3:1;    (3) a container fitted with a spray valve and actuator containing a propellant and a composition comprising 55-80 wt.% copper flake or cuprous oxide, 10-30 wt.% acrylic resin, and 0.5-5% fumed silica and/or fluorinated resin; and    (4) a method of applying an antifouling coat to a metallic marine structure, such as a marine propeller involving: roughening the surface to a profile of 50-75 microns; applying a dielectric primer; and then applying the copper flake or cuprous oxide-containing composition.
NOVELTY - Method for preparing water purifying agent, involves mixing hydrogen phosphate, ammonium chloride, sodium bicarbonate, sodium sulfide, ammonium sulfate and glucose to obtain medium, inoculating nitrogen-fixing bacteria, yeast, lactic acid bacteria, nitrate bacteria, phosphorus solubilizing bacteria, photosynthetic bacteria, Actinobacteria and fungi into the medium, culturing to obtain red brown symbiotic microorganisms, removing impurity from sewage discharge of pig farm excrement, adding the microorganisms into the obtained sewage, and fermenting to obtain the agent.    USE - The method is useful for preparing water purifying agent (claimed).    ADVANTAGE - The agent has 4x 105 effective microorganisms/ml, improves water quality, maintains good ecological water environment, causes no secondary pollution, and is prepared simply and cost-effectively.    DETAILED DESCRIPTION - Method for preparing water purifying agent, involves mixing 0.3 g hydrogen phosphate, 0.6 g ammonium chloride, 5 g sodium bicarbonate, 3 g sodium sulfide, 0.3 g ammonium sulfate and 3 g glucose, mixing uniformly at 200-300 degrees C and sterilizing at high temperature for 20-25 minutes to obtain culture medium, inoculating nitrogen-fixing bacteria, yeast, lactic acid bacteria, nitrate bacteria, phosphorus solubilizing bacteria, photosynthetic bacteria, Actinobacteria and fungi in a weight ratio of 1:1:1:1:1:1:1:1 into the above-obtained medium, under anaerobic illumination and room temperature, culturing for 8 hours and 12 days respectively to obtain red brown symbiotic microorganisms, removing impurity from sewage discharge of pig farm excrement using solid-liquid separation machine to obtain removing impurities of sewage, adding the obtained microorganisms into the obtained sewage, and fermenting at normal temperature for 6-7 days under anaerobic condition until the sewage turns golden yellow to obtain the agent.
NOVELTY - A helicid ester derivative is new.    USE - Helicid ester derivative for medicine.    ADVANTAGE - The synthesis of helicid ester derivative is simple, mild, easy to control, environment-friendly, uses highly selective biological enzyme, does not require protection and deprotection, and has easy to separate products.    DETAILED DESCRIPTION - A helicid ester derivative is new.    R=optionally branched alkanoyl, 9-11C (un)saturated alkoxy, or trans or cis aromatic acyl.    An INDEPENDENT CLAIM is also included for the preparation of compound (I).
NOVELTY - A bifunctional chimera comprising a beta -1,4-endoglucanase (Endo5A) having SEQ ID No. 1 at one end and beta -1,4-glucosidase (Gluc1C) having SEQ ID No. 4 at another end, is new.    USE - The bifunctional chimera is useful for hydrolyzing cellulosic biomass (claimed) and for producing ethanol.    ADVANTAGE - The bifunctional chimera is used for low cost and effective cellulosic biomass hydrolysis and ethanol production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a beta -1,4-glucosidase (Gluc1C) from Paenibacillus MTCC S639 comprising SEQ ID No. 4 comprising a GH superfamily-1 domain, where the enzyme comprises a defined sequence of 448 amino acids (SEQ ID No. 23), given in the specification; (2) a process for preparing bifunctional chimera above; and (3) a method of hydrolyzing cellulosic biomass by contacting the bifunctional chimeras above with pretreated cellulosic biomass; and incubating the mixture for 4-24 hours at 40 degrees C.
NOVELTY - Fertilization of tomato comprises planting tomato, applying fertilizer after 10-15 days, and continuously administering for 5-10 times at interval of 7-10 days/time.    USE - Method for fertilization of tomato (claimed).    ADVANTAGE - The method can make tomato reach its maturity for 7-15 days and improves production yield to 20-25%.    DETAILED DESCRIPTION - Fertilization of tomato comprises planting tomato, applying fertilizer after 10-15 days, and continuously administering for 5-10 times at interval of 7-10 days/time. The fertilizer is prepared by:    (A) mixing 40-60 pts. wt. phosphorus, 30-40 pts. wt. peanut cake, and 120-150 pts. wt. water, fermenting for 1-5 months, filtering, and collecting filtrate to obtain fermented manure; and adding 1-1.5 pts. wt. obtained manure with 0.8-1.5 pts. wt. of honey, 0.4-0.6 pts. wt. high potassium foliage fertilizer, and 280-320 pts. wt. water, and mixing to obtain foliar fertilizer; or    (B) mixing 40-60 pts. wt. phosphorus, 30-40 pts. wt. peanut cake, and 120-150 pts. wt. water, fermenting for 1-5 months, filtering, and collecting filtrate to obtain fermented manure; and adding 1 pt. wt. manure with 4-6 pts. wt. water or with 8-15 pts. wt. homogeneous slurry, and mixing to obtain fertilizer.
NOVELTY - The pulverizing device comprises a body (11) and a fixture (12) that is fixed in both upper portions of the body. A motor (13) is provided, which is fixed in the either side of the fixture. A rotary shaft (14) is connected to the motor. A backward direction spiral valve (15) is fixed in one side of the rotary shaft. An inner container (20) is fixed on the upper portion to the fixture. An inlet port (21) is formed on a top surface of the inner container. A vent is formed in the inner container. A power transmission device (40) is formed in an outer periphery of the outer container.    USE - Pulverizing device for livestock industry waste.    ADVANTAGE - The pulverizing device comprises a body and a fixture that is fixed in both upper portions of the body, and thus enables facilitating the fermentation of the domestic animals body, and facilitating the mixing and crushing the excrements. The combustion cost is reduced. The pulverization of the dead domestic animals is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a pulverizing device.    Body (11)    Fixture (12)    Motor (13)    Rotary shaft (14)    Backward direction spiral valve (15)    Inner container (20)    Inlet port (21)    Power transmission device (40)
NOVELTY - An organic fertilizer is prepared by mixing 1.00-5.00% urea, 0.70-3.20% calcium superphosphate, 0.15-1.25% potassium chloride and diammonium phosphate to obtain additive, adding selenium-enriched vermicompost, stirring, adding 1-12% water to obtain pH of 6.5-8.5, granulating to 0.20-0.45 mm, drying, cooling, screening, coating, inspecting, packing and storing.    USE - Method for preparing organic fertilizer used for preventing and controlling vegetable soil-borne disease (claimed).    ADVANTAGE - The environment-friendly and economical method returns production process investment. The fertilizer having high selenium content improves product yield and crop quality.
NOVELTY - Preparing dimethyl carbonate by using immobilized lipase as catalyst involves orderly adding reactants methanol and ethylene carbonate or propylene carbonate and methanol; adding immobilized lipase as catalyst in the reactant in reaction device; and carrying out transesterification reaction at 25-75 degrees C for 160 hours at a pressure of 0.1 Mpa, to obtain the dimethyl carbonate.    USE - For preparing dimethyl carbonate (claimed), used in food production, biotechnology, and biomedicine.    ADVANTAGE - The method has high conversion rate, high selectivity and high universality; has simple technique, and mild reaction condition; has reduced cost; and is environment-friendly.    DETAILED DESCRIPTION - Preparing dimethyl carbonate by using immobilized lipase as catalyst involves orderly adding reactants methanol and ethylene carbonate or propylene carbonate and methanol; adding immobilized lipase as catalyst in the reactant in reaction device; and carrying out transesterification reaction at 25-75 degrees C for 160 hours at a pressure of 0.1 Mpa, to obtain the dimethyl carbonate. The immobilized lipase is prepared by adding 400 g substrate, 25 l de-ionized water in container to form substrate solution (A); heating to boiling matrix solution, continuously stirring, boiling for 50 minutes after substrate basically dissolved, cooling to room temperature after stirring for 60 minutes to substantially colorless, to obtain transparent substrate solution (B); adding 100 g lipase and 300 l deionized water mixture into the substrate solution (A) to obtain mixed solution, stirring the mixed solution for 120 minutes, introducing the mixed solution into culture dish containing poly(tetrafluoroethylene), freezing and drying in vacuum for 24 hours to obtain the immobilized lipase.
NOVELTY - Digester (7) comprises a heater (3) with a flow regulating valve (2). A water storage tank (1) is connected to a flow regulating valve (4) and a waste water recycling device (5) is connected to the outlet flow through the heater. The obtained gas is divided into 2 paths and one flows through a compressor into a drying apparatus for residwential use and the other passes through the drying apparatus, carbon dioxide removal unit and compressor into the plant with a gas tank.    USE - Used for producing biogas.    ADVANTAGE - The biogas can save energy and reduce emission effect. The production efficiency of the boiler can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the digester.    Water storage tank (1)    Flow regulating valves (2,4)    Heater (3)    Waste water recycling device (5)    Heater inlet (6)
NOVELTY - The effective unit has a reactor to generate hydrogen-oxygen by using pure water supplied from a water reservoir, and to guide generated hydrogen-oxygen into an auto engine through a plastic hose. The water reservoir is connected with a top portion of reactor through plastic hose for automatically supplying water to reactor. An electrical circuit is connected with reactor through a relay, a breaker and a switch.    USE - Auto engine effective unit used in engine of vessel and aircraft. Can also be used in engine of car.    ADVANTAGE - The gas and diesel of 27% can be saved. The pollution of harmful carbon monoxide can be reduced from the exhaust of 80%. The dynamic power of the engine can be increased about 10% to 15% while increasing accelerate ability.
NOVELTY - A special microbial fertilizer comprises 35-45 wt.% sludge, 15-20 wt.% cattle manure, 10-15 wt.% chicken manure, 15-25 wt.% edible fungi cultivation waste, 8-12 wt.% arbuscular mycorrhizal fungi, 10-15 wt.% salt marsh fungi, and 0.05-0.15 wt.% wood vinegar.    USE - Special microbial fertilizer used for improving coastal saline soil (claimed).    ADVANTAGE - The fertilizer promotes aggregate formation, reduces soil pH and salinity, improves soil fertility, and promotes crop absorption of nitrogen, phosphorus, potassium and other trace elements and essential elements to promote crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by uniformly mixing sludge, cattle manure, chicken manure, edible fungi cultivation waste and wood vinegar; sealing the mixture in plastic film and fermenting for 10-12 days, while turning once on the third, sixth and ninth days; drying and crushing fermented material; preparing salt marsh fungi and arbuscular mycorrhizal fungi; and mixing with crushed fermented material and drying at 50-60 degrees C.
NOVELTY - This utility model claims a kind of dumper solves the problem that the existing turning and stacking depth limited, turning effect is bad, comprising a machine frame, the machine frame is provided with a plurality of connected on the machine frame by the wheel rotating shaft, turning device, wherein the turning main shaft, turning shaft through the hanging shaft is connected with the machine frame, a driving device, comprising a motor and a speed reducer connected with the motor, a lifting device, a machine frame placed on the upper part, a lifting device is connected with the hanging shaft, turning the main shaft is provided with a turning main shaft chain wheel, a wheel on the rotating shaft is provided with a wheel chain wheel, a speed reducer is provided with a speed reducer chain wheel, the chain is provided with a chain through a speed reducer chain wheel, turning main shaft chain wheel and a wheel chain wheel to realize the turning wheel rotating main shaft and a shaft is matched with the chain. This utility model claims a dumper capable of realizing turning requirement of different depth, turning effect is good, it is suitable for commercial popularization.
NOVELTY - This utility model claims a shell with a compost bin, a discharging component comprises a shell body surrounded by the first inner cavity of the shell body, and connected with the inner cavity of the feeding port, a discharging port, an air inlet, an air outlet, wherein, the first inner cavity of the shell is provided with an inner part, discharging of the discharging element comprises a housing and a plurality of holes are formed in the second shell body and the gas discharge in the second shell of the exhaust pipe. This utility model of the discharging structure is simple, the production is very convenient to install and use, can effectively discharging nature of compost in a compost process, it does not need the additional fan and so on, and is energy-saving and environment-friendly, reduces the resource waste.
NOVELTY - Preparation of pepper seedling culturing substrate comprises piling chicken manure into 3-5 m long, 1-1.2 m high and 1.5-2 m wide, and adding water after 3 months to obtain humus mixture; piling sheep manure, adding 100 g/m3 actinomycetes and fermentation bacteria mixture, uniformly turning, covering with plastic sheet, and composting for 5-7 days to obtain vermiculite; and mixing with humus mixture, straw, 100-150 g/m3 actinomycetes, 200-250 g/m3 ammonium nitrate, 100-150 g/m3 saponin, 80-150 g/m3 rhubarb powder, and 100-200 g/m3 phosphate rock, and stirring.    USE - Method for preparation of pepper seedling culturing substrate (claimed).    ADVANTAGE - The method is simple, can effectively shortens planting time to harvest for 10-13 days.
NOVELTY - A seed potatoes soil matrix comprises 8-10 pts. wt. high, medium or low-grade peat; 3-5 pts. wt. loosening agent comprising perlite, vermiculite or rice hulls; 2-4 pts. wt. inorganic ash comprising plant ash or coal ash; and 0.5-1.5 pts. wt. organic fertilizer comprising livestock and poultry manures, e.g. chicken manure, sheep manure or pig manure. The volume ratio of organic fertilizer and peat is 1:1-2. The volume ratio of livestock and poultry manure is 1:4-6.    USE - Seed potatoes soil matrix.    ADVANTAGE - The soil matrix has low cost and high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soil matrix by mixing livestock and poultry manures with peat in a heap, controlling moisture content to 60-70%, fermenting to 50-70 degrees C for 15-20 days, spreading, and drying to 20-30 degrees C for 15-20 days to obtain organic fertilizer, crushing, and sieving through 80-100 mesh sieve; and mixing with peat, loosening agent, and inorganic ash, and stirring at 85-300 revolutions/ minute for 0.2-0.5 hours.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically a natural cooling efficient one prilling tower, include a tower body, the tower body is set on the upper end of melting chamber and connected machine at the end of lower melting chamber, lower end of said tower body is a discharging end, wherein the tower body is also set with surrounding granulator set of spraying tube, said spraying tube set with upper spray hole, because using the said structure, the utility model is new type a rear one of a natural cooling granulating tower granulation can be efficient for the inner tower for spraying and dust-removing process to prevent the dust pollution to air, and not for low secondary granulation would produce, improve the whole mass of fertilizer, at the same time, cleaning of dust through different discharge port of discharge to prevent mixing to material in chemical fertilizer.
NOVELTY - This utility new type belongs to the new energy source preparation device field, claims a one marsh gas preparation biology natural gas of a decarburization device, comprise tower body, gas inlet, gas distributor, gas outlet, high pressure water inlet, a high pressure water distributor, a high pressure water outlet, a filler, a thermometer and foam, the device the desulphurization purification gas uniformity distribute ascending from the bottom in the device, high pressure water uniformity distribute falling in the device is composed of an upper, rear marsh gas and water counter-current contact in the device, marsh gas in the high solubility of carbon dioxide dissolve in the water, low solubility gas discharged gas outlet. Using the new device use a gas removing treatment, small floor area, processing efficiency is high, operation is convenient, and the absorbing carrier is water, without adding any absorbent, processing cost is low, at the same time, water for each component in a gas of there is no chemical reaction, device for corrosion.
NOVELTY - A high-temperature methanation catalyst comprises carrier, active component and additives. Carrier is ceria, alumina and/or zirconia. Active component is nickel. Additives are alkaline earth metal oxide, including calcium oxide and/or magnesium oxide; and transition metal oxide, including chromium(III) oxide and/or manganese(II) oxide.    USE - High-temperature methanation catalyst for coal gas (claimed).    ADVANTAGE - The catalyst has high strength, large specific surface area, good heat resistance, high catalytic activity and thermal stability, and improved dispersibility. It promotes nickel oxide reduction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-temperature methanation catalyst comprising taking cerium nitrate, aluminum nitrate and zirconium nitrate, reacting at 70-80 degrees C, adding precipitating agent, adjusting pH value of 8.0-9.5, reacting for 1-2 hours, filtering, washing, drying, calcining, soaking in solution containing nitrate salt of chromium, manganese, nickel, calcium and/or magnesium, drying, baking, and optionally pressing.
NOVELTY - A low-temperature high-activity methanation catalyst comprises active component, carrier, additive and coagent. Active component is nickel. Carrier is alumina. Additive is magnesium oxide. Coagents are lanthanum rare earth metal and manganese metal. Catalyst contains 18-45 wt.% nickel oxide, 40-70 wt.% alumina, 5-30 wt.% magnesium oxide, 0.4-5 wt.% lanthanum oxide and 0.1-5 wt.% manganese dioxide.    USE - Low-temperature high-activity methanation catalyst used for coke oven gas, coal synthesis gas and exhaust gas rich in carbon monoxide, carbon dioxide and hydrogen.    ADVANTAGE - The catalyst has large surface area, uniform nickel dispersion, good thermal stability, strong antioxidant activity, and adaptable to low hydrogen-to-carbon ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of low-temperature high-activity methanation catalyst comprising:    (A) taking alumina and magnesium salt, adding water, heating to 60-90 degrees C, stirring, adding precipitating agent, and reacting for 2-3 hours;    (B) adjusting pH value to 6.5-7.5, filtering, heating at 180-220 degrees C for 10-25 hours, and washing;    (C) taking nickel nitrate hexahydrate, adding water, stirring at 60-90 degrees C, adding coagent salt, mixing, adding carrier, and stirring for 0.5-1 hour;    (D) adding precipitating agent, reacting for 1-5 hours, adjusting pH value to 6.5-7.5, filtering, washing, drying, calcining at 400-500 degrees C, and sieving; and    (E) adding 5-15 wt.% water and 3-5 wt.% lubricant, mixing, pressing, and forming.
NOVELTY - Preparation lanthanum-doped phosphate ion/zirconium oxide composite comprises mixing zirconium chloride powder, lanthanum nitrate and distilled water, stirring for 30 minutes, adding ammonium hydroxide, maintaining pH to obtain white precipitate, aging for 24 hours, filtering, washing, drying at 102 degrees C, adding 85% phosphoric acid solution, soaking for 2 hours, filtering, drying, introducing nitrogen gas and sintering at 400-800 degrees C for 2 hours.    USE - Method for preparing lanthanum-doped phosphate ion/zirconium oxide composite used as biodiesel catalyst (claimed).    ADVANTAGE - The lanthanum-doped phosphate ion/zirconium oxide composite has good selectivity and high catalytic efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of Xanthoceras sorbifolia biodiesel comprising mixing Xanthoceras sorbifolia kernel oil, methanol and biodiesel catalyst at 75 degrees C for 5 hours under water bath, filtering, drying, standing, placing filtrate in separatory funnel to obtain glycerol layer and crude product layer, washing with distilled water, adding anhydrous sodium sulfate to remove water and obtaining Xanthoceras sorbifolia biodiesel.
NOVELTY - Manufacture of organic potassium fertilizer comprises taking corn stalk after harvesting, crop waste, such as wheat straw and rice straw, crushing into granule, putting into a tank, pressing, sealing, naturally fermenting for 16 days, and continuously storing in the tank.    USE - Manufacture of organic potassium fertilizer used for fertilizing grapefruit and orange at fruiting time (claimed).    ADVANTAGE - The organic potassium fertilizer provides sweet and delicious fruit, is easy for crop absorption, convenient to store and use, and suitable for long-term storage, has simple preparation and reduced production cost, improves the quality and yield of fruit, and reduces environmental pollution.
NOVELTY - Rural organic waste composting fermentation comprises mixing crop straw, poultry cultivation waste and rural solid domestic garbage of organic rotten component, obtaining composting ferment raw material, adding organic matter-decomposing inoculant agent to obtain stack material, processing first fermentation obtain first fermentation stack material, carrying-out second fermentation to obtain second fermentation stack material, and turning third fermentation to obtain organic fertilizer.    USE - Method of rural organic waste composting fermentation (claimed).
NOVELTY - Biological organic fertilizer comprises 10-30 pts. wt. animal manure, 10-30 pts. wt. crop straw, 1-3 pts. wt. chitin, 5-15 pts. wt. moss, 10-30 pts. wt. pine needle, 10-20 pts. wt. carbamide, 1-3 pts. wt. biological enzyme and 1-3 pts. wt. organic fertilizer fermenting agent.    USE - Biological organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic fertilizer comprising crushing animal manure, crop straw, chitin, moss and pine needle, putting into fermenting tank, adding with biological enzyme, organic fertilizer fermenting agent and adding water, stirring for 30 minutes, sealing, and fermenting; and adding to chitin, fermenting at 50 degrees C for 20-30 days, and adding urea; and adding fermentation product of urea in shady place, until water content of less than 5%, drying, and adding pelletizer to obtain biological organic fertilizer.
NOVELTY - Fermentation of livestock excrement comprises adding livestock excrement in flour factory low material, stirring, adding 45-55% water, controlling nitrogen ratio of more than 30, adding in fermenting tank, and processing aerobic fermentation.    USE - Method of fermentation of livestock excrement (claimed).
NOVELTY - Aerobic composting device comprises perforated plate, segmentation container into upper lower two parts, compost reactor at upper part, detachable seal cover, air outlet, gas sampling port, greenhouse gas sampling opening on upper seal cover, temperature sensor, air room equipped with vent-pipe, air tube through rotor flow meter and electromagnetic valve connecting air outlet of air compressor, and electromagnetic valve electrically connected to programmable logic controller (PLC) in PLC automatic control system.    USE - Aerobic composting device.    ADVANTAGE - The device is easy to control.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the aerobic composting device.
NOVELTY - An ecological fertilizer comprises 8-12 pts. wt. phosphate rock powder, 30-40 pts. wt. straw ash, 15-30 pts. wt. plant stems and leaves, 10-20 pts. wt. animal manure, 15-25 pts. wt. straw, 10-12 pts. wt. rice chaff, and 10-15 pts. wt. urea solution.    USE - Ecological fertilizer.    ADVANTAGE - The fertilizer is safe and environment-friendly and capable of realizing resource regeneration, utilizes easy to obtain raw materials, and has low production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the ecological fertilizer, comprising chopping plant stems and leaves and straw; mixing chopped plant stems and leaves and straw, phosphate rock powder, animal manure and rice chaff, and then uniformly spraying the urea solution onto the mixture; and stacking and seal fermenting for 40 days to obtain the ecological fertilizer product.
NOVELTY - A fertilizer composition comprises 8-10 wt.% chestnut tree leaf, 30-40 wt.% bean cake, 20-30 wt.% rice water, 8-10 wt.% fern, 5-8 wt.% expanded perlite, and balance auxiliary material.    USE - Fertilizer composition used for orchid cultivation.    ADVANTAGE - The fertilizer composition has low manufacturing cost, is convenient to use, and contains nitrogen, phosphorus and potassium needed for orchid cultivation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fertilizer composition, comprising collecting semi-rotten chestnut tree leaf, cleaning sundries using clear water and soaking for 3-5 days, then grinding and crushing; mixing bean cake and rice water and fermenting; adding the crushed chestnut tree leaf and fern and the fermented bean cake and rice water, and then adding expanded perlite; and putting mixture into bag or jar and sealing and storing for 1-3 months.
NOVELTY - A compound organic fertilizer is prepared by mixing straw, weathered coal, peat, flour, rice husk powder and sweet potato flour, crushing through 60 mesh sieve, adding mixture of urea, molasses, glycerol and mixed bacteria powder, stirring uniformly with added 1000 pts. wt. water, carrying out high temperature steam sterilization at 120-130 degrees C for 30 minutes, cooling to 30 degrees C, putting in fermentation tank at 28-37 degrees C for 48 hours, adding EDTA and fulvic acid, mixing, granulating, and drying at 20-40 degrees C.    USE - Method for preparing compound organic fertilizer (claimed).    ADVANTAGE - The method has easy operation, low cost, and can be produced in large scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compound organic fertilizer comprising 45-60 pts. wt. straw, 15-20 pts. wt. weathered coal, 10-15 pts. wt. peat, 15-30 pts. wt. flour, 20-30 pts. wt. rice husk powder, 15-20 pts. wt. sweet potato flour, 5-10 pts. wt. urea, 5-10 pts. wt. molasses, 5-30 pts. wt. glycerol, 5-8 pts. wt. EDTA, 8-12 pts. wt. fulvic acid, and 1-5 pts. wt. mixed bacteria powder.
NOVELTY - Organic compound fertilizer comprises 10-15 pts. wt. ammonium nitrate fertilizer, 6-8 pts. wt. calcium magnesium phosphate fertilizer, and 80-120 pts. wt. organic fertilizer.    USE - Organic compound fertilizer used as planting fertilizer, preferably vegetable fertilizer.    ADVANTAGE - The organic compound fertilizer promotes growth of vegetable and herbs, shortens maturity of cucumber, and improves and increases production yield of vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic compound fertilizer by collecting traditional Chinese medicine dregs, straw and wheat bran; crushing into granule with diameter of 0.4-0.8 cm; exposing traditional Chinese medicine dregs in low light for 10-12 hours; adding bran and uniformly stirring; spraying fungal liquid; uniformly mixing; piling and fermenting at normal temperature for 3-5 weeks with turning once every 5-10 days; spraying bacterial liquid according to proportion; uniformly mixing; further piling and fermenting at normal temperature for 3-4 weeks with turning once every 3-5 days; drying to obtain fermented organic fertilizer; adding fermented organic fertilizer with ammonium nitrate fertilizer and calcium-magnesia phosphate fertilizer according to proportion; uniformly mixing; and drying to obtain organic compound fertilizer.
NOVELTY - Straw decomposing agent comprises bran, major elements consisting of ferrous sulfate, potassium chloride and magnesium sulfate, and trace element consisting of potassium iodide, sodium borate, manganese sulfate, zinc sulfate, copper sulfate, and ammonium sulfate. It preferably comprises 2000 g bran, 100 g ferrous sulfate, 100 g potassium chloride, 360 g magnesium sulfate, 76 g potassium iodide, 66 g sodium borate, 27 g manganese sulfate, 23.1 g zinc sulfate, 29.25 g copper sulfate, and 23.75 g ammonium sulfate for decomposing 1000 kg straw.    USE - Straw decomposing agent.    ADVANTAGE - The straw decomposing agent is easy to use, has small investment, and can quickly and completely decompose straw, thus solving problem of existing agricultural straw waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of straw decomposing agent by dissolving straw decomposing agent in water according to weight ratio of 1:1.5 to obtain straw decomposing solution; digging decomposing pit; laying first layer of rice straw accounted for 1/3 of total amount; spraying 1/4 volume of straw decomposing solution; laying second layer of straw accounted for 1/3 of total amount; spraying with another 1/4 volume of straw decomposing solution of 1/4 volume; laying third layer of straw accounted for 1/3 of total amount; and spraying remaining 1/2 volume of straw decomposing solution.
NOVELTY - Tea tree foliar fertilizer comprises 50-60% concentrated biogas, 10-20% plant source composite amino acid, 10-20% biochemical fulvic acid, 1-5% phosphate, and 1-5% urea.    USE - Tea tree foliar fertilizer.    ADVANTAGE - The tea tree foliar fertilizer is environment-friendly. It achieves early germination of tea bud and early harvest period of 8-15 days, shortens picking cycle, accelerates growth, and increases production by 30%. It improves tea quality, bud germination, and tea amino acids content. It produces tea with sweet taste, brew resistant, and has long lasting fragrant. It also improves resistant of tea from pest, cold, drought, and diseases, thus reducing adverse effects of natural disasters in tea plantations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of tea tree foliar fertilizer by heating concentrated biogas in water bath at 70 degrees C; sequentially adding plant source composite amino acid, biochemical fulvic acid, phosphate, and urea; and fully stirring for 1 hour to dissolve completely.
NOVELTY - A spray-type microorganism fertilizer comprises boric acid, potassium carbonate, ammonium molybdate, citric acid, trace element, and composite microbial inoculum.    USE - Spray-type microorganism fertilizer used for reducing production of plant diseases and insect pests.    ADVANTAGE - The fertilizer increases crop leaf photosynthesis intensity, chlorophyll component and crop stress resistance, and inhibits growth of harmful bacteria.
NOVELTY - An organic tea tree biologically controlled release fertilizer comprises 30-45 pts. wt. chicken manure, 25-30 pts. wt. mica powder, 15-20 pts. wt. ammonium nitrate, 9-14 pts. wt. kaolin, 20-25 pts. wt. rice hull ash, 8-15 pts. wt. bauxite, 3-6 pts. wt. tripolyphosphate, 2-6 pts. wt. sodium hexametaphosphate, 7-14 pts. wt. disodium hydrogen phosphate, 0.001-0.002 pt. wt. Bacillus thuringiensis powder, 25-30 pts. wt. soybean straw powder, 11-20 pts. wt. lemon, 5-8 pts. wt. oilseed straw powder, and 14-19 pts. wt. vine green straw powder.    USE - Organic tea tree biologically controlled release fertilizer.    ADVANTAGE - The fertilizer is environment-friendly, has high utilization rate, and improves tea quality and soil.
NOVELTY - A biofertilizer comprises 15-20 pts. wt. rapeseed, 3-9 pts. wt. dipotassium hydrogen phosphate, 1-2 pts. wt. sodium pyrophosphate, 3-9 pts. wt. sodium dihydrogen phosphate, 11-16 pts. wt. disodium hydrogen phosphate, 12-15 pts. wt. rice hull powder, 68 pts. wt. peat, 25-35 pts. wt. chicken manure, 15-30 pts. wt. soybean cake meal, and 1-2 pts. wt. Bacillus subtilis.    USE - Biofertilizer used for promoting tea growth (claimed).    ADVANTAGE - The biofertilizer is non-toxic, has no side effect and no drug resistance, improves tea quality and soil, and increases human body content in tea leaves.
NOVELTY - A food green tea biofertilizer comprises urea, ammonium chloride, diammonium hydrogen phosphate, weathered coal, bamboo charcoal powder, photosynthetic bacteria powder, Rhizopus stolonifer powder, Bacillus licheniformis powder, duck manure, cotton straw powder, oil seed straw powder, goose dung, Sarcandra glabra, ash bark, radix stemonae, potassium sulfate, sodium chloride, calcium superphosphate, and ammonium molybdate.    USE - Food green tea biofertilizer.    ADVANTAGE - The biofertilizer increases yield and improve soil quality.    DETAILED DESCRIPTION - A food green tea biofertilizer comprises 35-40 pts. wt. urea, 11-16 pts. wt. ammonium chloride, 15-26 pts. wt. diammonium hydrogen phosphate, 25-30 pts. wt. weathered coal, 15-30 pts. wt. bamboo charcoal powder, 0.0001 pt. wt. photosynthetic bacteria powder, 0.0001 pt. wt. Rhizopus stolonifer powder, 0.0001 pt. wt. Bacillus licheniformis powder, 25-30 pts. wt. duck manure, 15-20 pts. wt. cotton straw powder, 25-30 pts. wt. oil seed straw powder, 15-20 pts. wt. goose dung, 15-20 pts. wt. Sarcandra glabra, 3-6 pts. wt. ash bark, 3-5 pts. wt. radix stemonae, 11-20 pts. wt. potassium sulfate, 10-20 pts. wt. sodium chloride, 1-2 pts. wt. calcium superphosphate, and 3-6 pts. wt. ammonium molybdate.
NOVELTY - A mountain tea tree biological controlled-release fertilizer comprises 3-9 pts. wt. ammonium molybdate, 2-5 pts. wt. ferrous sulfate, 10-12 pts. wt. stone powder, 20-25 pts. wt. grass carbon powder, 30-40 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 15-20 pts. wt. wheat bran, 10-20 pts. wt. rice straw powder, 10-15 pts. wt. corn straw powder, 0.001-0.002 pt. wt. silicate bacteria powder, 0.002 pt. wt. Bacillus cereus powder, 3-6 pts. wt. calcium superphosphate, 1-5 pts. wt. potassium sulfate, 3-6 pts. wt. calcium nitrate, 10-12 pts. wt. kieselguhr, and 16-20 pts. wt. peat soil.    USE - Mountain tea tree biological controlled-release fertilizer.    ADVANTAGE - The fertilizer has organic and inorganic nutrient, and can improve soil and tea quality and reduce cost.
NOVELTY - A high-quality tea planting biofertilizer comprises 15-20 pts. wt. rape rice bran, 5-10 pts. wt. conch shell powder, 5-9 pts. wt. clam shell powder, 9-14 pts. wt. calcium monohydrogen phosphate, 3-6 pts. wt. calcium superphosphate, 3-5 pts. wt. potassium nitrate, 2-6 pts. wt. ammonium nitrate, 1-2 pts. wt. nitric acid, 10-15 pts. wt. rape cake meal, 15-20 pts. wt. soybean cake meal, 15-30 pts. wt. soybean rice bran, and 1-2 pts. wt. Bacillus subtilis bud.    USE - High-quality tea planting biofertilizer.    ADVANTAGE - The fertilizer is rich in organic and inorganic fertilizer, non-toxic, has no side effect, no residue and no drug resistance, and can improve tea quality and soil and increases human body.
NOVELTY - A tea tree biological fertilizer comprises 15-20 pts. wt. rapeseed cake cypress, 5-10 pts. wt. conch shell powder, 5-9 pts. wt. clam shell powder, 9-14 pts. wt. dicalcium phosphate, 3-6 pts. wt. calcium superphosphate, 3-5 pts. wt. potassium nitrate, 15-20 pts. wt. turnip straw powder, 25-30 pts. wt. mustard large straw powder, 25-30 pts. wt. flax straw powder, 0.0001 pts. wt. plant activating enzyme, 0.001-0.002 pts. wt. Trichoderma, 0.003 pts. wt. Bacillus subtilis, and 11-16 pts. wt. potassium sulfate.    USE - Tea tree biological fertilizer.    ADVANTAGE - The fertilizer is rich in nutrition which improves quality and growth of tea, easy to use, recyclable and environment-friendly, reduces pests and labor intensity, and has low cost.
NOVELTY - An organic tea fertilizer comprises 25-30 pts. wt. urea, 25-30 pts. wt. mica powder, 15-20 pts. wt. ammonium nitrate, 9-14 pts. wt. kaolin, 20-25 pts. wt. rice hull ash, 8-15 pts. wt. bauxite, 3-6 pts. wt. potassium tripolyphosphate, 2-6 pts. wt. sodium hexametaphosphate, 7-14 pts. wt. disodium hydrogen phosphate, 0.001-0.002 pts. wt. Bacillus thuringiensis powder, 25-30 pts. wt. soybean straw powder, 25-30 pts. wt. potato straw powder, 10-15 pts. wt. clam shell powder, 15-20 pts. wt. castor cake, 10-13 pts. wt. talc, and 15-20 pts. wt. calcium superphosphate.    USE - Organic tea fertilizer.    ADVANTAGE - The organic fertilizers has nitrogen, phosphorus, potassium, mineral nutrients, trace elements and organic matter content, reduces tea diseases, and has low cost and high economic efficiency.
NOVELTY - A green tea organic fertilizer comprises Bacillus subtilis, calcium dihydrogen phosphate, diammonium phosphate, plant activating enzymes, calcium nitrate, Bacillus thuringiensis powder, dipotassium hydrogen phosphate, sodium acid pyrophosphate, sodium dihydrogen phosphate, disodium hydrogen phosphate, chicken manure, potassium chloride, Candida powder, cotton straw powder, and oilseeds straw powder.    USE - Green tea organic fertilizer.    ADVANTAGE - The fertilizer has broad formulation which contains nitrogen, phosphorus, potassium other nutrients, and trace elements, strong specificity, comprehensive nutrition, and better and practical application.    DETAILED DESCRIPTION - A green tea organic fertilizer comprises 0.003 pts. wt. Bacillus subtilis, 8-14 pts. wt. calcium dihydrogen phosphate, 9-11 pts. wt. diammonium phosphate, 0.0001 pts. wt. plant activating enzymes, 3-5 pts. wt. calcium nitrate, 0.001-0.003 pts. wt. Bacillus thuringiensis powder, 3-9 pts. wt. dipotassium hydrogen phosphate, 1-2 pts. wt. sodium acid pyrophosphate, 3-9 pts. wt. sodium dihydrogen phosphate, 11-16 pts. wt. disodium hydrogen phosphate, 25-30 pts. wt. chicken manure, 15-20 pts. wt. potassium chloride, 0.1-0.3 pts. wt. Candida powder, 25-29 pts. wt. cotton straw powder, and 15-20 pts. wt. oilseeds straw powder.
NOVELTY - Biofertilizer comprises 25-30 pts. wt. potato straw powder, 30-40 pts. wt. highland barley straw powder, 15-20 pts. wt. broad bean straw powder, 5-10 pts. wt. conch shell powder, 5-9 pts. wt. clam shell powder, 9-14 pts. wt. calcium monohydrogen phosphate, 3-6 pts. wt. calcium superphosphate, 3-5 pts. wt. potassium nitrate, 2-6 pts. wt. ammonium nitrate, 1-2 pts. wt. nitric acid, 10-15 pts. wt. rapeseed cake, 15-20 pts. wt. soybean powder, 0.001-0.003 pts. wt. Bacillus thuringiensis, 0.001-0.003 pts. wt. Aschersonia powder, and 0.001-0.003 pts. wt. caterpillar fungus powder.    USE - Biofertilizer used for promoting tea growth (claimed).    ADVANTAGE - The fertilizer is environment-friendly, improves tea quality and soil, and has no toxic side effect, residue and drug resistance.
NOVELTY - A liquid compound microbial fertilizer comprises Penicillium and sodium selenite.    USE - Liquid compound microbial fertilizer used for vegetable.    ADVANTAGE - The fertilizer improves product quality, environment-friendly and kills harmful pathogenic bacteria.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of liquid compound microbial fertilizer comprising mixing 20 pts. wt. soluble starch, 31 pts. wt. potassium nitrate, 0.5 pt. wt. potassium hydrogen phosphate, 0.5 pt. wt. epsomite, 0.5 pt. wt. sodium chloride and 0.01 pt. wt. iron sulfate, adding 1000 pts. wt. distilled water, adjusting pH at 7-7.2, sterilizing at 1.05 kg/cm2 for 20 minutes to obtain solution, preprocessing sample soil, separating Penicillium, purifying, crushing, screening, adding 0.5 mg/L sodium selenite, and fermenting at 28 degrees C for 5 days; and (2) application of liquid compound microbial fertilizer comprising diluting with water, soaking, and spraying leaf or root.
NOVELTY - Composite biofertilizer includes 10-20 pts. wt. ammonium dihydrogen phosphate, 0.0001-0.0006 pt. wt. calcium EDTA, 0.0001-0.0002 pt. wt. magnesium EDTA, 0.0002-0.0008 pt. wt. magnesium, 0.0168-0.7665 pt. wt. iron EDTA, 0.0001-0.0425 pt. wt. zinc sulfate, 0.0021-0.0877 pt. wt. manganese sulfate, 0.0001-0.0047 pt. wt. ammonium molybdate, 0.2 pt. wt. humic acid, 2 pts. wt. Aloe vera juice, 1 pt. wt. soy protein, 0.4 pt. wt. seaweed powder, 20-30 pts. wt. Bacillus thuringiensis, 25-30 pts. wt. Bacillus megaterium and 15-20 pts. wt. Bacillus mucilaginosus.    USE - Composite biofertilizer for tobacco (claimed).    DETAILED DESCRIPTION - Composite biofertilizer comprises 10-20 pts. wt. ammonium dihydrogen phosphate, 0.0001-0.0006 pt. wt. calcium EDTA, 0.0001-0.0002 pt. wt. magnesium EDTA, 0.0002-0.0008 pt. wt. magnesium, 0.0168-0.7665 pt. wt. iron EDTA, 0.0001-0.0425 pt. wt. zinc sulfate, 0.0001-0.0761 pt. wt. zinc sulfate, 0.0054-0.0097 pt. wt. copper EDTA, 0.0011-0.0694 pt. wt. manganese EDTA, 0.0021-0.0877 pt. wt. manganese sulfate, 0.1054-0.2998 pt. wt. boric acid, 0.0001-0.0047 pt. wt. ammonium molybdate, 0.2 pt. wt. humic acid, 2 pts. wt. Aloe vera juice, 1 pt. wt. soy protein, 0.4 pt. wt. seaweed powder, 20-30 pts. wt. Bacillus thuringiensis, 25-30 pts. wt. Bacillus megaterium and 15-20 pts. wt. Bacillus mucilaginosus.
NOVELTY - A special fruit composite biological liquid fertilizer comprises EDTA-calcium fertilizer, EDTA-manganese fertilizer, EDTA-copper fertilizer, EDTA-zinc fertilizer, EDTA-magnesium fertilizer, EDTA-iron fertilizer, zinc sulfate heptahydrate, magnesium sulfate heptahydrate, manganese sulfate monohydrate, boric acid, potassium sulfate, humic acid, soy protein, aloe juice, seaweed powder, sodium silicate, anhydrous ferrous sulfate, brassinolide, Bacillus thuringiensis, Bacillus megaterium, Pseudomonas fluorescens and Streptomyces jingyangensis.    USE - Special fruit composite biological liquid fertilizer used for improving soil composition, preventing pests, stimulating crop growth and improving crop quality.    ADVANTAGE - The fertilizer is low-cost, long-lasting and can be applied to wide range of fruits and crops. It has microbial activity and high yield.    DETAILED DESCRIPTION - A special fruit composite biological liquid fertilizer comprises 25.2-26.3 pts. wt. calcium fertilizer EDTA-calcium, 0.25-0.37 pt. wt. manganese fertilizer EDTA-manganese, 0.052-0.073 pt. wt. copper fertilizer EDTA-copper, 0.082-0.093 pt. wt. zinc fertilizer EDTA-zinc, 30.02-31.18 pts. wt. magnesium fertilizer EDTA-magnesium, 0.85-0.91 pt. wt. iron fertilizer EDTA-iron, 0.052-0.073 pt. wt. zinc sulfate heptahydrate, 18.6-20.32 pts. wt. magnesium sulfate heptahydrate, 0.009-0.12 pt. wt. manganese sulfate monohydrate, 0.15-0.23 pt. wt. boric acid, 0.102-0.215 pt. wt. potassium sulfate, 0.83-0.95 pt. wt. humic acid, 4.58-4.85 pts. wt. soy protein, 8.5-9.5 pts. wt. aloe juice, 1.73-1.89 pts. wt. seaweed powder, 0.021-0.031 pt. wt. sodium silicate, 0.18-0.22 pt. wt. anhydrous ferrous sulfate, 0.85-0.95 pt. wt. brassinolide, 42.58-43.85 pts. wt. Bacillus thuringiensis, 8.2-9.3 pts. wt. Bacillus megaterium, 42.58-43.85 pts. wt. Pseudomonas fluorescens and 4.25-4.38 pts. wt. Streptomyces jingyangensis.
NOVELTY - An organic chelate fertilizer comprises 30-40 pts. wt. low monosodium glutamate leftovers, 20-30 pts. wt. boric magnesium ore slag, 10-20 pts. wt. humic acid, 1-2 pts. wt. borate, 5-6 pts. wt. magnesium sulfate, 3-5 pts. wt. zinc sulfate, 1-2 pts. wt. imidacloprid, and 0.1-0.5 pts. wt. Bacillus thuringiensis.    USE - An organic chelate fertilizer.    ADVANTAGE - The fertilizer can loosen soil and prevent soil plate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic chelate fertilizer comprising: (A) adding 10 pts. wt. monosodium glutamate leftovers, 10-20 pts. wt. humic acid, 1-2 pts. wt. borate, 5-6 pts. wt. magnesium sulfate and 3-5 pts. wt. zinc sulfate in the reaction kettle, adding 100 pts. wt. water at 80-90 degrees C for 60-90 minutes, filtering and drying in prepared microelement chelate; and (B) crushing boric magnesium slag to 80-100 meshes to obtain boric magnesium slag granule, adding 0.1-0.5 pts. wt. Bacillus thuringiensis, 20-30 pts. wt. monosodium glutamate leftovers, and 20-30 pts. wt. boric magnesium slag and preparing the trace element chelate fertilizer in mixed material of the granulator in 1-2 pts. wt. imidacloprid, preparing into solution for mixing material, and taking machine spray granulation to obtain the organic chelate fertilizer.
NOVELTY - The device has a rake drying machine (1) that is set with a feeding port (11) and a discharging port (12). The vacuum device (2) is connected with rake drying machine through pipeline (3). The vacuumizing device is connected with the condenser through pipeline. The condenser is connected to the solvent storage tank (4) which is connected with the rake dryer. The drying machine is set with rake for heating material of jacket.    USE - Device for recovering carbaryl residue.    ADVANTAGE - The efficiency and safety recovery of the carbaryl residue recovering device is improved. The energy consumption can be reduced and the yield of carbaryl can be improved. The amount of residue can be reduced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbaryl residue recovering device.    Rake drying machine (1)    Vacuum device (2)    Pipeline (3)    Solvent storage tank (4)    Feeding port (11)    Discharging port (12)
NOVELTY - Manufacture of dicyclohexyl disulfide involves reacting disulfide solution with cyclohexane reaction, mixing reaction mixture in a mixed solvent, and preparing mixed solvent of polar solvent and polar non-protonic solvent. The polar solvent is water, methanol or ethanol. The polar non-proton solvent is sulfone, sulfoxide or dimethylformamide. The volume ratio of polar solvent and polar aprotic solvent is 1:1-2.    USE - Manufacture of dicyclohexyl disulfide is used in chemical field.    ADVANTAGE - The dicyclohexyl disulfide is efficiently prepared with high conversion rate and safety without polluting the environment.
NOVELTY - Amino antipyrine liquor and saturated ammonium sulfate solution are mixed, and upper layer containing amino antipyrine oil is separated. Water is mixed with oil, and concentrated sulfuric acid is dropped to obtain mixed liquid. Chloroform is added to mixed liquid, supernatant is heated, activated carbon is added, and filtered. The filtrate is concentrated, liquid ammonia is added, and heated. Saturated ammonium sulfate solution is added to resulting mixture, to obtain antipyrine oil. Water is added to antipyrine oil, cooled, and recrystallized, to obtain amino antipyrine liquor.    USE - Recycling of amino antipyrine liquor (claimed).    ADVANTAGE - The method economically and environmentally-friendly recycles amino antipyrine liquor with high yield, by a simple process.    DETAILED DESCRIPTION - Amino antipyrine liquor and saturated ammonium sulfate solution are mixed, stirred for 15-20 minutes, and upper layer containing amino antipyrine oil is separated. Water is mixed with amino antipyrine oil, concentrated sulfuric acid is dropped, and pH of resulting mixture is adjusted to obtain mixed liquid. Chloroform is added to mixed liquid, temperature of upper layer is maintained at 50-55 degrees C, layer-separated, upper layer is retained, supernatant is heated at 60-80 degrees C, activated carbon is added, heated to 50-90 degrees C for 35-45 minutes, and filtered. The filtrate is concentrated to 60-80 degrees C, liquid ammonia is added, pH is adjusted, and the resulting mixture is heated at 85-90 degrees C. Saturated ammonium sulfate solution is added to the resulting mixture, mixture is poured into separation funnel, and layered to obtain antipyrine oil. Water is added to antipyrine oil, stirred, cooled in tap water to 35 degrees C, and ice cubes to 10-25 degrees C, centrifuged and recrystallized, to obtain amino antipyrine liquor.
NOVELTY - Ethyl chloro oxime (I) and 1,1-diphenylethylene (II) are reacted under the action of alkali metal compound in presence of solvent, to obtain isoxadifen (III).    USE - Synthesis of isoxadifen used as herbicide safener.    ADVANTAGE - The method environmentally-friendly provides isoxadifen with high yield, under mild reaction condition, by a simple process.    DETAILED DESCRIPTION - Ethyl chloro oxime of formula (I) and 1,1-diphenylethylene of formula (II) are reacted under the action of alkali metal compound in presence of solvent, to obtain isoxadifen of formula (III).
NOVELTY - Preparation of lignin-based polyoxyethylene ether involves heating 100-400 pts. wt. polyethylene glycol to 40-60 degrees C, melting, adding 1-3 pts. wt. catalyst, adding 10-40 pts. wt. epichlorohydrin for 30-60 minutes, reacting at 40-60 degrees C for 1-2 hours, obtaining modified polyethylene glycol intermediate, separately mixing water and 100 pts. wt. alkali lignin, adjusting pH to 10-13, adding modified polyethylene glycol intermediate for 1-2 hours, reacting at 70-90 degrees C for 2-4 hours, adjusting pH to 6-8, cooling to room temperature and spray-drying.    USE - Preparation of lignin-based polyoxyethylene ether used for pesticide.    ADVANTAGE - The method efficiently enables preparation of lignin-based polyoxyethylene ether having excellent water solubility by environmentally-friendly process in short period of time.    DETAILED DESCRIPTION - Preparation of lignin-based polyoxyethylene ether involves heating 100-400 pts. wt. polyethylene glycol to 40-60 degrees C, melting, adding 1-3 pts. wt. catalyst, adding 10-40 pts. wt. epichlorohydrin for 30-60 minutes, reacting at 40-60 degrees C for 1-2 hours, obtaining modified polyethylene glycol intermediate, separately mixing water and 100 pts. wt. alkali lignin, adjusting pH to 10-13, adding modified polyethylene glycol intermediate for 1-2 hours, reacting at 70-90 degrees C for 2-4 hours, adjusting pH to 6-8, cooling to room temperature and spray-drying. The catalyst is chosen from antimony pentafluoride, boron trifluoride diethyl ether complex, aluminum chloride, tin tetrachloride, antimony pentachloride and tetrabutylammonium bromide.
NOVELTY - Production of pesticide comprises using dry solid of phosphorus-containing waste and/or liquid phosphorus-containing waste to obtain phosphorus-containing solid material in thermal cracking device, thermal cracking organic gas, carrying out combustion of organic gas into the combustion device, quenching, hot cracking phosphorus-containing solid waste and/or phosphorus-containing solid material, carbonizing at high temperature, purifying, obtaining high purity phosphate, and producing gas into the combustion device.    USE - Method for producing pesticide (claimed).    ADVANTAGE - The method avoids the use of medicine preparation, does not produce secondary waste, and is environment-friendly.
NOVELTY - A carbon gas heat cogeneration device comprises pyrolysis and gasification furnace. An air inlet and a feeding port are on upper part of the pyrolysis and gasification furnace. The device further comprises high temperature smoke channel with inlet end connected to combustion room and outlet end connected to first waste heat boiler; and combustion chamber.    USE - Carbon gas heat cogeneration device.    ADVANTAGE - The device has high efficiency by using biomass resource, produces high quality gas, and has high energy utilization ratio.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the carbon gas heat cogeneration device.
NOVELTY - High energy alcohol base fuel oil is prepared by adding 90-95% pure methanol to highly efficient synthetic fuel additive, stirring, and mixing with main fuel oil and remaining materials.    USE - Preparation of high energy alcohol base fuel oil for factory, industrial enterprises, construction site, offices, schools, restaurants, and food stalls.    ADVANTAGE - The prepared high energy alcohol base fuel oil is low cost, conserves energy, reduces emission, does not produce smoke, and has no smell.
NOVELTY - Methanol diesel is prepared by ultrasonically dispersing auxiliary agents at 80 kHz frequency for 10-30 minutes, uniformly mixing with methanol to obtain mixture, adding to diesel fuel, and uniformly stirring.    USE - Preparation of methanol diesel (claimed).    ADVANTAGE - The preparation of methanol diesel is simple, uses readily available raw materials, and yields energy-saving and emission-reducing stable product with high lubricating property.
NOVELTY - Biodiesel is manufactured by using animal and plant oil and waste oil, tanneries, plant scrap, and animal fats as raw material, removing impurities, purifying, dehydrating, placing in reaction container, heating to 40-55 degrees C (S101), adding 2 wt.% composite catalyst i.e. sodium hydroxide, 3 wt.% cosolvent i.e. dimethyl ether, and 10-20 wt.% methanol with respect to weight of raw material, rapidly esterifying to obtain fatty acid methyl ester (S102), maintaining temperature, stirring for 30-60 minutes, standing for 3 hours to form layers, collecting upper liquid, and adding 5% light oil (S103).    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The manufacture of biodiesel is environment-friendly, fast, saves energy, and has high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of manufacture of biodiesel. (Drawing includes non-English language text).    Cleaning, purifying, dehydrating and heating oil raw material (S101)    Esterification (S102)    Heat preservation, standing, and collecting light oil (S103)
NOVELTY - Biological gasoline is prepared by mixing Aspergillus niger biomass with aqueous hydrochloric acid, soaking in sodium hydroxide (NaOH) solution, washing until neutral, adding aqueous hydrogen peroxide (H2O2) decoloring solution to obtain chitin, adding to aqueous zinc chloride solution, adding aluminum chloride, reacting, extracting with petroleum ether, rotary evaporating to obtain 5-(hydroxymethyl)furfural, adding to ethanol containing phosphotungstic acid, reacting, distilling reaction solution to obtain 5-ethoxymethylfurfural, mixing with ethanol blended gasoline or gasoline.    USE - Preparation of biological gasoline (claimed).    ADVANTAGE - The preparation of biological gasoline is environment-friendly, low cost, and yields product which produces less coke, and has stable combustion and high energy density.    DETAILED DESCRIPTION - Biological gasoline is prepared by mixing Aspergillus niger biomass with 1-10% aqueous hydrochloric acid with mass ratio biomass:hydrochloric acid of 1:2-4 at constant temperature of 50-100 degrees C for 0.5-3 hours, soaking in 15% NaOH solution with mass ratio NaOH solution:biomass of 1:2-4 at constant temperature of 90-100 degrees C for 1-3 hours to remove protein, washing until neutral, adding 5% aqueous H2O2 decoloring solution to obtain chitin, adding to 30-70% aqueous zinc chloride solution, adding catalytic amount of aluminum chloride which is 10-20 mass%, reacting at constant temperature of 60-100 degrees C for 1-3 hours, extracting with petroleum ether, rotary evaporating to obtain 5-(hydroxymethyl)furfural, recovering zinc chloride, catalyst, and petroleum ether, adding to ethanol containing phosphotungstic acid with is 30 mass% with respect to 5-(hydroxymethyl)furfural, reacting at 60-100 degrees C for 6-15 hours, distilling reaction solution to obtain 5-ethoxymethylfurfural, mixing with 5-ethoxymethylfurfural and ethanol blended gasoline or gasoline with ratio of 1:0.1-10.
NOVELTY - A sulfur and nitrogen fixing sludge lignite molding fuel contains 10-20 pts. wt. domestic sludge, 55-81 pts. wt. lignite, 4-10 pts. wt. aluminum sludge, and 5-15 pts. wt. additives i.e. 65-92 wt.% calcium oxide, 3-20 wt.% potassium carbonate, and 5-15 wt.% potassium hydroxide.    USE - A sulfur and nitrogen fixing sludge lignite molding fuel (claimed).    ADVANTAGE - The sulfur and nitrogen fixing sludge lignite molding fuel reduces nitrogen oxide, sulfur oxide, and mercury emissions, improves coal ash melting point and combustion, reduces boiler slag, saves water, and has improved sulfur-fixing effect and simple processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sulfur and nitrogen fixing sludge lignite molding fuel which involves crushing lignite and domestic sludge to less than or equal to 0.5 mm particle size, crushing additives to less than or equal to 90 mu m particle size, mixing crushed domestic sludge and lignite, aluminum sludge, and additives, blending in stirrer, and feeding to press molding machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of preparation of sulfur and nitrogen fixing sludge lignite molding fuel. (Drawing includes non-English language text).
NOVELTY - A biomass fuel dense forming automatic production is processed by screening dry material (S1) in roller sieve a, transferring to inclined feeding machine, performing modulation forming (S3) by sequentially feeding and modulating dry material in spiral sub-feeder and spiral modulator and performing extrusion forming in extrusion molding machine to obtain finished product pressed block, screening finished product pressed block (S4) in sieving mechanism, screening out low density finished product pressed block, and cooling finished product pressed block (S5) in cooling conveyor.    USE - Biomass fuel dense forming automatic production process (claimed).    ADVANTAGE - Production process is labor-saving, has greatly improved production efficiency and yield and reduced production cost, and realizes continuous production, uniform feeding and discharging, and direct bagging.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a biomass fuel dense forming automatic production process. (Drawing includes non-English language text).    Screening dry material (S1)    Modulation forming (S3)    Screening finished product pressed block (S4)    Cooling finished product pressed block (S5)
NOVELTY - A biodiesel is prepared by subjecting oil to esterification at 105-130 degrees C using 0.05-0.2% acidic catalyst, stirring, adding 10-200% methanol dropwise for 1-8 hours in which unreacted methanol is condensed, reacting for 10-20 minutes, distilling mixture to remove water and methanol and obtain crude biodiesel, and distilling at 210-250 degrees C and - 0.1 MPa pressure.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The preparation method is simple, fast, high-yielding, and low in energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of method for preparation of biodiesel. (Drawing includes non-English language text).
NOVELTY - This utility new type relates to a one for making hydrogen and storing hydrogen as a whole of integrated hydrogen supply device, comprising a hydrogen production device, hydrogen storage device, pneuma pipeline system is composed of three parts. Hydrogen producing device is composed of shell, box type liner, square seal flange cover. Hydrogen storage device is composed of a square shell, a seal flange cover, an internal hydrogen storage insulating layer. Inlet and outlet system of pneuma hydrogen output system of rear water vapour input system, hydrogen output system, purification. This utility new type hydrogen making device is installed on the hydrogen storage device, can be valid to solve the hydrogen storage device the hydrogen source. Dryer, hydrogen storage interlayer is installed on the said integrated hydrogen supply device, is dry purification of hydrogen provide convenient condition. This utility new type also solves the hydrolysis reaction can not be control of device. The hydrogen-making and hydrogen-storing integrated as one whole, the design is simple, saves space, is convenient to control, different type battery provide fuel of relatively pure hydrogen fuel, is suitable for industrial production.
NOVELTY - This new type utility claims one a small kitchen waste processing device of biological fermentation container structure, include the garbage bucket body, a spiral stirring strip and baffle plate, spiral stirring strip and a baffle plate is vertically welded on the inner wall surface of the garbage bucket body, a baffle uniformly distributed upper material channel between the spiral stirring with form of. This utility new type kitchen of the small stirring device in the garbage treatment device biological fermentation container is designed to be spiral belt manner, solves the problem that in the existing technology the stirring shaft and the stirring blade of easy to break, reduces the stress of the stirring process, and improves the operation reliability and the stirring efficiency and stirring effect is better.
NOVELTY - This utility new type household food waste through ozone odour-removing rear convert raw material processing device, wherein the bottom of the food garbage crushing tank is crushed sheet a electric machine fixing plate, crushing plate a electric machine fixing plate and the crushing plate control motor, the crushing plate control electric machine is connected with the crushing food garbage crushing the bottom right side mounting food waste crushing tank, food garbage crushing tank through pipeline with the separating tank, separating tank middle mounted with a filter net, a separating tank left side mounting food waste outlet separating tank, a separating tank right side is separation tank water outlet, the upper part in the shell is ozone generator, ozone generator and the food garbage crushing tank through ozone inlet tube is connected, the device is equipped with ozone generator, ozone has a sterilizing and decomposing function of peculiar smell and ensure the device for a long time use will not produce internal insects and peculiar smell.
NOVELTY - This utility new type household waste wood and waste through ozone removing and recycling device, wherein the left side of shell is equipped with switch and rear processing, switch and temperature control module is connected with the shell upper part is equipped with ozone generator, ozone generator is connected with the air inlet is connected with the air inlet and the decomposition chamber shell is composed of decomposition chamber, a carbonization chamber, a heating disk, the decomposition chamber with the carbonization chamber through clapboard, the carbonization chamber and the heating disk is connected with right side of shell is equipped with transparent plastic, the right side shell is connected with smoke evacuation is connected with shell side connecting part. The utility model is new type for waste wood and waste treatment process, to remove the waste wood and peculiar smell of waste paper and a sterilizing, improving home environment, and the waste wood and waste paper can be converted into organic fertilizer, the utilizing the water again in at home, one is a protecting environment and saving energy of device.
NOVELTY - This utility new type relates to compost ventilation and accelerating composting of device. One a compost ventilation corrosion accelerating tube, include tube body, set with ventilation hole on the upper tube body, a ventilation cover set with the two end tube body of the said tube body two end 0.5 to 1 m not provided with a vent hole. This utility new type reduces the turning frequency can continuously stack center to provide a cover of air, can be according to temperature of compost or different composting stage regulating ventilation strength and effectively inhibits the anaerobic bacteria, quickens the speed of decomposed compost, stack temperature over-high of when further can be properly reduced temperature, shortens the period of whole rotten compost, at the same time, saves the labour input of manual turning, futher of, greatly reduces the device investment and field working condition, use is flexible and convenient, can use a fast area.
NOVELTY - This utility new type claims a one machinery device, a feeding system is one that a organic waste aerobic fermentation treatment device of. This utility new type include, hoisting device, device and a guiding device and so on, wherein said of frame is a triangular frame structure, inclined installation, through motor mounting fixing base is welded with the electric motor connected with the through bolt connecting pulley and the guide pulley I is connected with the bracket through a welding guide device is directly connected with the connecting, feeding rail inclined against the upper frame. This utility new type has the advantages that it can successfully of the material feeding process of unload the roller in rotating process, using the bottom-opening door, operation is convenient, rate of a feeding save a lot of labour, at the same time, timing and quantifying of to avoid how feeding of material, improve the working efficiency of the fermentation cylinder.
NOVELTY - This utility new type claims a machinery device one, a one is a type for composting organic compost production of pile-turning machine. This utility new type comprise machine frame, a walking mechanism, turning plate mechanism, a lifting system, and automatic control system and so on, wherein the lower part of the front rack and rear end is equipped with a set of driven wheel and one of a driving wheel, the driving wheel one by one group of the running motor, one group of the running motor through main shaft connecting, driving wheel is set on the walking track of the walking mechanism up, at the same time, turning plate mechanism, a lifting system by corresponding motor drives to realize the system coordinates the operation. This utility new type has the advantages of the 2 walking motor control, so it can ensure the continuous operation of device, using rotation of hook tooth chain-type polishing scattering mechanism for turning the pile of compost material in the fermenting groove a throwing, aeration, stirring, efficiency is high, the turning distance is long, turning completely can be valid shortens fermentation period, improves the compost mass, device has stronger adaptability and flexibility.
NOVELTY - This utility new type belongs to biomass resource use, especially a one hot sodium de-oil the, the semi-coke combustion double-circulation combination system. This utility new type bed as the fast pyrolysis furnace, to circulation fluidized bed is semi-coke combustion using device, to circulation fluidized bed of hot ash generated by burning and circulation non-condensable pneuma as pyrolysis furnace of hot carrier. Alginate fragment heated decomposition gas by separating rear forming bio-oil and non-condensable gas in the pyrolysis furnace, fast bed of semi-coke outlet is directly sent to the circulation fluidized bed combustion, the generated high temperature smoke entering into pneuma pneuma solid separator, separated fly ash of the reciprocating material valve so as to entering into pyrolysis bed as hot carrier, of pneuma rear smoke dust-removing through the tail heating surface, and finally discharged into the atmosphere, the tail heating surface heating produce of steam used for power generation and heat supply. So as to really realize the seaweed biomass comprehensive;
NOVELTY - This new type utility claims one hot a high conversion efficiency of straw carbonization furnace, comprise a furnace body, the furnace body is set on one side of big door and small door, a big furnace door of big furnace door seal through pressure pole and big furnace door hinge with the furnace body, the small furnace through small door seal pressure pole and small furnace with the big furnace door, hearth is set in the said of furnace body, wherein a water interlayer of furnace body around said hearth, the interlayer is provided with a water outlet and a water inlet, the interlayer of upper end of said hearth is provided with the upper end of a flue water interlayer is equipped with a water interlayer is connected with hot water outlet tube and hot water pump on the lower end of said furnace body is provided with a temperature detection probe in the said hearth is equipped with a temperature detecting probe of a device connecting the said upper furnace body.
NOVELTY - This utility new type claims a new-type one-making device and thermal cracking of biomass, include device main body, the device main body comprise a feeding device, said feeding device below the cylinder reaction furnace is connected with a cylindrical outer reaction furnace set with the inner wall of the temperature control system, the cylinder reaction furnace with blowing system, reaction furnace outlet connecting the condensing system. This utility new type fixed bed thermal cracking reactor can be used for processing all wood category biomass, such as straw, rice hull, cotton pole, corn core, wood and so on, for the adaptability of raw material. The pyrolysis reactor of preparation of biological oil yield can reach 45wt % ~ 52wt%, by-product of reaction is gas product and solid carbon product, wherein gas product rich in CO, H2 and CH4, it can be used as natural gas directly use of solid carbon product fuel or raw material of preparation activity. This utility new type reasonable structure layout, using of energy efficiency is high and the production process of energy saving and high efficiency, safety and environment-friendly.
NOVELTY - This utility new type belongs to the gasification furnace of auxiliary device field, claims a one a pneuma for furnace building furnace auxiliary device, include gasification furnace body, is provided with at least one of connected pipeline between the liquid seal, liquid seal gasification furnace and the gasification furnace body of one side, the liquid seal tank is provided with water, a liquid sealing tank of upper wall of one side of a one-way air inlet valve, liquid seal is arranged beside a purification tank, a purification tank through pipeline with liquid seal connected. This utility new type structure for combustion energy-saving furnace with biomass straw gasification furnace can be valid of a seal to prevent gas leakage, ensure smooth of gas collecting. At the same time, the pressure increase of the inner gasification furnace or time is reduced, capable of pressure in the gasification furnace for a proper regulating, of the pressure in the gasification furnace in the reasonable range of, the pressure change of the gasification furnace for gasification furnace caused by the excessive damage to affect the use service life of the gasification furnace.
NOVELTY - This utility new type belongs to marsh gas separating purification field, specific relates to a one end marsh gas desulfurization purification device. The device comprise tube, gas inlet, gas distributor, marsh gas outlet, an overflow port, upper liquid level meter interface, lower liquid level meter interface, a solution inlet, a spraying device, a solution outlet and foam destroyer, up a tube middle part side wall set with marsh gas inlet, a gas inlet tube connected in the middle part is of marsh gas distributor, marsh gas distributor a lower part of one side of upper side wall set with an overflow port and the solution outlet, the other one side of upper side wall is provided with a lower interface and a liquid level meter upper liquid level meter interface, a tube upper part side wall set with upper solution inlet, a solution inlet connected upper part in the tube is of spraying device, said spraying device upper part set with demister. The device has reasonable design, simple structure, can better in removing and purification process of the doctor of impurity is normal stable operation of subsequent marsh gas storage device and provide beneficial condition.
NOVELTY - This utility new type belongs to the new energy preparation technology field, especially relates to a one for to marsh gas preparation of compressed biology natural gas of drying device. Include dehydration device I and dehydrating device II, the compressor is equipped with the dewatering device I and II, a water elution carbon tower before the dewatering device I, the finished product pneuma output pipeline set with the dehydrating device II an air outlet, a dehydration device I and II are skid-mounted structure, device I and II comprise a gas drying pipe in turn along the one is provided with a filter, a drying tower A and drying tower B and filter two, further comprise a system, a filter upper part one and a drying tower A and B connected at the bottom, a filter upper part a second connected with the drying tower A and B top, at the same time, set with pneuma counter-current regeneration heating regeneration pipeline between the drying tower A and B, heating up regeneration pipeline is equipped with closed heater, cooling separator regeneration pneuma. This utility new type has simple structure, processing efficiency is high, operation is convenient, it can according to different of use and reasonable configuration, valid reduce the running cost on the premise of ensuring low mass of processing, and it is very suitable for popularization.
NOVELTY - This utility new type claims a sludge into one of the fuel processing system, comprising a sludge include receive diluting device, mixing modified stirring device, machinery pressing dewatering device, drying device and biomass powder mixing device and granulating device forming one-way connecting in turn; It has treatment effect is good, the device arrangement is reasonable, the practicability is strong, the sludge into low high, no pollution, the sludge of municipal into fuel can be used, and the economic benefit is obvious and resource use of municipal sludge, municipal obtain ecological environment of greatly improved, therefore, it is a system device a technical and economical efficiency are one of excellent.
NOVELTY - This new type utility claims one based on a waste of biology drying derived fuel production system, belonging to the circulation economic field. The system include receive system garbage, the garbage front processing system, drying system, RDF production system, processing system, ozone purification system and related auxiliary system, wherein the rear garbage front processing system for a aritificial protogenous rubbish, machinery sorting and crushing treatment, treatment of garbage is sent to the microbial-drying system a homogenizing drying dehydration, drying and rear of garbage entering into RDF production system, through screening, extrusion moulding refuse derived fuel RDF as substitute fossil fuel. This utility new type of refuse derived fuel production system is especially suitable for mixed garbage, it can overcome the defect that the traditional hot dry need the hot source device and drying odour need purification and so on, so as to improve the economic benefit.
NOVELTY - This utility new type relates to one a palm oil residue and acidified oil refining biological diesel of device, include catalytic cracking device, pre-esterification reaction device, a rectifying device, a tail gas boiler pneuma and water treatment system. This utility new type of the following beneficial effects: This utility new type through cracking reaction, the pre-esterification prior to reaction of the raw material oil in which contains a large amount of olefin, alkane such as diesel component, pre-esterification reaction rear, of fatty acid in raw material oil into fatty acid methyl ester and fatty acid alkyl ester such as typical diesel component, so as to make into biological diesel product directly without need of later period, and can be any proportion and diesel are mixed to use.
NOVELTY - This utility new type relates to rural marsh gas application and biogas fertilizer production technology field, aiming at rural marsh gas production of limited by the season, winter low temperature to marsh gas production rate is greatly reduced, provide the one of a high producing marsh gas fermenting device, mainly is improved through marsh gas tank is arranged on the periphery of circular heat preservation pool for marsh gas tank in winter heating and heat preservation process the marsh gas yield of low temperature seasons marsh gas pool, this utility new type futher as complete for supporting facilities of marsh gas tank. Peripheral additional marsh gas tank for heating and heat preservation function of heat preservation pool, marsh gas tank in winter can be maintained to ensure stable of temperature, so as to maintain the stable yield of marsh gas in winter.
NOVELTY - Collecting device comprises hydrogen generating device, water outlet, tap water inlet device and gas collecting device, where gas collecting device is connected to pipeline. The connected pipeline, water outlet device and tap water inlet device are provided with upper valve and control valve (6). The hydrogen generating device is connected with the circuit control device.    USE - Collecting device for hydrogen production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of collecting device.    Pure water replenishing device (1)    Anode water box (2)    Cathode water box (3)    Oxygen generator (4)    Hydrogen collecting pneuma bucket (5)    Control valve (6)    Water bucket (7)
NOVELTY - This new type utility claims one hot a high conversion efficiency of carbonized straw hot water furnace, comprise a furnace body, the furnace body is set on one side of big door and small door, a big furnace door of big furnace door seal through pressure pole and big furnace door hinge with the furnace body, the small furnace through small door seal pressure pole and small furnace with the big furnace door, hearth is set in the said of furnace body, wherein a water interlayer of furnace body around said hearth, the interlayer is provided with a water outlet and a water inlet, the interlayer of upper end of said hearth is provided with the upper end of a flue water interlayer is equipped with a water interlayer is connected with hot water outlet tube and hot water pump on the lower end of said furnace body is provided with a temperature detection probe in the said hearth is equipped with a temperature detecting probe of a device connecting the said upper furnace body is provided with a water foam dedusting device on said upper furnace body.
NOVELTY - This new type utility claims one hot a high conversion efficiency of energy-saving straw carbonizing hot water furnace, comprise a furnace body, the furnace body is set on one side of big door and small door, a big furnace door of big furnace door seal through pressure pole and big furnace door hinge with the furnace body, the small furnace through small door seal pressure pole and small furnace with the big furnace door, hearth is set in the said of furnace body, wherein a water interlayer of furnace body around said hearth, the interlayer is provided with a water outlet and a water inlet, the interlayer of upper end of said hearth is provided with the upper end of a flue water interlayer is equipped with a water interlayer is connected with hot water outlet tube and hot water pump on the lower end of said furnace body is provided with a temperature detection probe in the said hearth is equipped with a temperature detecting probe of a device connecting the said upper furnace body.
NOVELTY - This utility new type provide the one a coal slime drying system, include scattering pre-dry machine, drying at low temperature furnace, forming machine, dust removing device and used for the said scattering pre-dry machine and a low temperature drying furnace 250 following of hot air heating device, a scattering pre-dry machine and a low temperature drying furnace is connected with a low temperature drying furnace of upper part through an exhaust pipeline and a dust-removing device is connecting, a low temperature drying furnace of lower part and a forming machine is connected with a heat supply device through heat supply pipeline a and a scattering pre-dry machine and a low temperature drying furnace. The operation safety, high efficiency, no pollution, large production.
NOVELTY - Bio-enzyme fertilizer comprises 4-6 pts. wt. bio-enzyme, 290-310 pts. wt. agricultural waste, 310-330 pts. wt. livestock and poultry manure, 40-60 pts. wt. amino acids, 90-110 pts. wt. humic acid, 40-60 pts. wt. plant ash, 15-25 pts. wt. shell powder, 4-6 pts. wt. fermentation enzyme agent, 40-60 pts. wt. mineral powder and 90-110 pts. wt. boron soil powder.    USE - Used as bio-enzyme fertilizer.    ADVANTAGE - The fertilizer is simple to prepare, rich in nutrients and environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing bio-enzyme fertilizer, comprising: (i) crushing the raw materials and uniformly mixing to obtain a mixture; (ii) fermenting the mixture from room temperature until 60-65 degrees C internal temperature to obtain fermentation mixture; and (iii) crushing the fermentation mixture, granulating and drying.
NOVELTY - A one beer production waste water treatment system, comprise pre-aeration regulating tank, a pre-aeration regulating tank through lifting pump connecting IC anaerobic reaction tank, a IC anaerobic reaction tank and then connect the anaerobic sedimentation tank, said anaerobic sedimentation tank connect sludge discharging system and a water discharging system, a IC anaerobic reaction tank through an exhaust tube connecting with a marsh gas burning furnace, a methane combustion furnace is installed on the pre-aeration regulating tank. Compared with the existing technology, this utility new type of beer production waste water treatment system, through the methane combustion furnace in the system, the waste water of organic matter in reaction generated a marsh gas to the combustion furnace, a methane combustion furnace produce energy for the reaction tank of normal working of the temperature, at the same time of saving energy also speeds up the processing efficiency of system.
NOVELTY - This utility new type refers to a high-speed activating kettle and one comprise the high speed activation kettle of high speed activation device, a high-speed activating kettle of wherein said high speed activation kettle comprising a kettle body of one material inlet, one to multi-groups of C-type stirrer. Kettle top with a plurality of liquid additive inlet and one containing double pneuma lock valve of solid additive. Along the bottom with a steam inlet. Kettle to the discharging port. At the activating kettle outlet connected with one buffer tank. Buffer tank inlet and outlet are respectively provided with automatic time control valve for regulating an activation kettle of the material and to the proper frequency explosion to swelling. Swelling is a second cone, middle upper big lower end. Cone along the middle around the air inlet to adjust expansion device pressure. The air inlet and outlet with a baffle plate to avoid material sprayed in the expansion device. Expansion device with a steam collecting opening upper end, lower end with a spiral conveyor rear swelling of organic fertilizer is used for transporting material. This utility new type high speed activation of device aims to treat organic solid waste and the recycling the organic fertilizer.
NOVELTY - This utility new type one a biomass pyrolysis device relates to one used for biomass continuous pyrolysis of a device. The purpose is to provide a simple structure, one reaction material fully, it can continuous process test of pyrolysis device. This utility new type one biomass pyrolysis device comprise a feeding machine, heating device, tube, an outer sleeve and discharging port of temperature controller, a feeding machine connecting with one of the joint, joint lower end and upper end tube, said tube is cylindrical type, said outer sleeve tube is installed on the outside middle part tube and the outer sleeve is set with a heating device and temperature controller, the cylinder body bottom end connecting with machine feeding port. In addition, the utility model is new type biomass pyrolysis device further comprise air inlet valve and exhaust fan, said air inlet valve is installed on the said upper end joint, a exhaust fan and tube extends out the lower part of pipeline.
NOVELTY - This utility new type one a blocking type biomass pyrolysis device the purpose is to provide a one-clogging property, simple structure, simple and convenient operation of the pyrolysis device. This utility new type one a type biomass pyrolysis device comprise anti-blocking feeder machine, temperature control device, reactor and outer heat preservation layer, a discharge hole of feeding machine is equipped with one of the joint, joint lower end and upper end reactor. Reactor is cylindrical type, comprise shaft set and tube. The outer heat preservation layer is installed on the reactor, reactor and outer heat preservation layer is mounted between the temperature control device, reactor bottom end connecting with machine feeding port. In addition system further comprise stirring shaft, the stirring shaft comprise upper lower two section, stirring shaft upper section upper annular bearing platform is processed on the shaft set up of reactor of the shaft sleeve for locating a stirring shaft, the stirring shaft lower section upper section is connected with the stirring shaft. Stirring shaft lower section with external spiral blade, spiral blade diameter slightly smaller than tube diameter.
NOVELTY - This utility new type claims a one preparing fermentable reducing sugar from biomass carbon producing pneuma device, comprise bucket body, a bucket body is set with upper cover, and the upper end lower end set with lower sealing head, a bucket body one side upper part set with a spraying opening, lower part set with an air inlet, a bucket while the other lower side part set with charging hole, said upper sealing head top part set with an air outlet, a bottom end set with a sewage outlet, said air outlet in upper wall set with at least one of first baffle plate, at least one of second baffle, said first baffle and said second baffle are staggered. This utility new type provide of preparing fermentable reducing sugar from biomass carbon producing pneuma device, solves the problem that in the existing technology the air gas flow rate, high temperature of, and can be for a gas purification treatment, the midway time charging, would not because the gas high temperature caused by the operator;
NOVELTY - Organic planting method of Pimenta, involves (a) obtaining field waste including dry branches and fallen leaves of Pimenta and weed, farm pig manure and chicken manure, peanut bran, other minerals, microbial leaven including effective microorganisms (EM), prepared biological fermented compost as base fertilizer, and self-made high quality organic fertilizer containing nitrogen, phosphorus and potassium, and organic matter, and (b) artificially preventing and controlling e.g. Trichogramma and other pests of Pimenta.    USE - The organic planting method is useful for Pimenta and preventing and controlling insect pests, and plant diseases e.g. root rot and anthracnose of Pimenta (all claimed).    ADVANTAGE - The method does not cause pollution as caused by continuous use of chemical fertilizer, farm chemical and hormone, prevents damage of agricultural environment and hence protects agricultural environment, is cost-effective, improves yield and quality of Pimenta, maintains balance of forest and agricultural ecological system, achieves agricultural economic development, and provides economic benefit and social benefit.    DETAILED DESCRIPTION - Organic planting method of Pimenta, involves (a) obtaining 40-50% field waste including dry branches and fallen leaves of Pimenta and weed, 40-50% farm pig manure and chicken manure, 5-8% peanut bran, 0.5-1% other minerals, 0.5-1% microbial leaven including effective microorganisms (EM), prepared biological fermented compost as base fertilizer to improve soil fertility, and self-made high quality organic fertilizer containing nitrogen, phosphorus and potassium content of 4-7%, and 25-35% organic matter, and (b) artificially preventing and controlling e.g. Trichogramma and other pests of Pimenta or controlling natural pest through ecological system.
NOVELTY - Black fungus cultivation material comprises 55-65 wt.% sawdust, 30-40 wt.% mulberry, 0.8-1.2 wt.% gypsum powder, 2-3 wt.% wheat bran, 0.009-0.012 wt.% mushroom, and suitable amount of water, where above-mentioned raw materials are mixed with 55-60 wt.% water.    USE - As black fungus cultivation material.    ADVANTAGE - The black fungus cultivation material is good in color and taste, and produces fungus in high yield and high quality.
NOVELTY - Synthesis of 2-amino-4,6-dimethoxypyrimidine (I) involves dissolving 2-chloro-4,6-dimethoxypyrimidine (II) in solvent, providing the resultant product into autoclave, carrying out pressurized amination reaction using ammonia (NH3) at 20-120 degrees C for 3-10 hours under 5000-8000 kpa, cooling the resultant product, then carrying out solid-liquid separation process, and drying the resultant product.    USE - Synthesis of 2-amino-4,6-dimethoxypyrimidine (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides 2-amino-4,6-dimethoxypyrimidine with high yield, and high quality, by simple process.    DETAILED DESCRIPTION - Synthesis of 2-amino-4,6-dimethoxypyrimidine of formula (I) involves dissolving 2-chloro-4,6-dimethoxypyrimidine of formula (II) in solvent, providing the resultant product into autoclave, carrying out pressurized amination reaction using ammonia (NH3) at 20-120 degrees C for 3-10 hours under 5000-8000 kpa, cooling the resultant product, then carrying out solid-liquid separation process, and drying the resultant product.
NOVELTY - Cultivation substrate comprises (in vol.%): coconut shell powder base material (15-30), alcohol ferment biogas residue (15-30), straw (5-10), carbonized rice hull (5-10), permafrost soil (3-5), perlite (5-10) and vermiculite (20-25).    USE - Cultivation substrate.    ADVANTAGE - The cultivation substrate is soilless, cost-effective and nutritious.
NOVELTY - Preparation of organic fertilizer comprises mixing 90-110 pts. wt. with moisture content of 70-80% and 10-15 pts. wt. bran, adding fermenting agents and ash, mixing, adjusting water content to 50-60%, piling mixture into windrow shape with width of 1.8 m and height of 1.2-1.6 m, carrying out aerobic fermentation for 15-20 days, adjusting water content to 20-30%, crushing, sieving and processing into powder or granules.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The product has good antibacterial effect and has high level of nutrients.
NOVELTY - Composite biofertilizer comprises 0.4-0.6 pt. wt. fermentation bacteria, 15-25 pts. wt. crop straw, 20-30 pts. wt. pepper, 10-20 pts. wt. humic acid, 5-15 pts. wt. organic potassium, 0.5-1.5 pts. wt. flour, 1-3 pts. wt. distillers grain, 9-11 pts. wt. rock phosphate powder and water.    USE - Composite biofertilizer.    ADVANTAGE - The product is low-cost and environment-friendly.
NOVELTY - An alcohol-based liquid fuel contains methanol, additives i.e. 31-35 mass% water, 5 mass% sodium hydroxide, 5 mass% sodium acetate, 35 mass% glycerol, 18 mass% hydrogen peroxide, and 2-6 mass% ferric nitrate, and catalyst i.e. ferrocene.    USE - An alcohol-based liquid fuel (claimed).    ADVANTAGE - The alcohol-based liquid fuel has simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based liquid fuel which involves mixing water, sodium hydroxide, sodium acetate, glycerol, hydrogen peroxide, and ferric nitrate additives, adding methanol, uniformly mixing, and adding ferrocene.
NOVELTY - A seed oil biodiesel is produced by performing hydration degumming treatment, removing seed oil, placing in water bath, adding boiling water, stirring, heating, standing, centrifuging to obtain raw oil in upper layer and glue and impurity mixture in lower layer, performing transterification reaction by mixing seed oil and short chain alcohol, adding heteropolyacid catalyst, placing in microwave, cooling, separating heteropolyacid catalyst from liquid product by performing vacuum filtration to obtain biodiesel in upper phase and glycerol in lower phase, and performing vacuum rotary evaporation.    USE - Production of seed oil biodiesel (claimed).    ADVANTAGE - The method uses extensive source of raw materials and catalyst which can be recycled, and is low cost.    DETAILED DESCRIPTION - A seed oil biodiesel is produced by performing hydration degumming treatment, removing seed oil, placing in constant temperature water bath at 60 degrees C, adding 1-4% amount of boiling water, stirring quickly for 10-20 minutes, raising temperature to 90 degrees C, standing for 6 hours, centrifuging to obtain raw oil in upper layer and glue and impurity mixture in lower layer, performing transterification reaction by mixing seed oil and short chain alcohol at mass ratio of seed oil to short chain alcohol of (0.5-1)-(1:1), adding 3% heteropolyacid catalyst, placing in microwave at 300-700 W, 150-300 rpm and 40-70 degrees C for 10-60 minutes, cooling to room temperature, separating solid heteropolyacid catalyst from liquid product by performing vacuum filtration to obtain biodiesel in upper phase and glycerol in lower phase, and performing vacuum rotary evaporation.
NOVELTY - Low-temperature coal tar processing method comprises removing solid residues of low-temperature coal tar, processing to a diameter of 25-100 mu m, preprocessing; fractionating to obtain phenol oil, water and heavy oil; processing phenol oil to remove oil and obtain refined phenol; mixing removed oil in fluidized bed reactor for hydrogenation reaction, to obtain modified heavy oil, sulfur and ammonia gas by-products; hydrogenation refining modified heavy oil, hydrogenation cracking to obtain dry gas, liquefied gas, naphtha, diesel oil and tail oil.    USE - Method for low-temperature coal tar processing (claimed).    ADVANTAGE - The method improves property of oil product.
NOVELTY - Preparation of seaweed bio-organic fertilizer comprises mixing seaweed with auxiliary materials and 20-30% microbial agents where dosage of microbial agent is 1 kg per 0.5-1.2 tons of raw materials, spraying, mixing, controlling moisture content to 55-65%, carrying out fermentation in well-ventilated area at 15-20 degrees C, heating at 50 degrees C until no peculiar smell is produced, adjusting pH value to 5.5-8.5, pulverizing or granulating and drying at low temperature to moisture content of 30-40%.    USE - Method for preparing seaweed bio-organic fertilizer (claimed) used for improving crop quality, crop yield and soil structure.    ADVANTAGE - The method is simple and cost-saving.
NOVELTY - Ultra-high-temperature aerobic fermentation of a sludge comprises fermenting sludge, mixing and stirring, and adding a fermentation initiating agent; and carrying out static fermentation.    USE - Method for ultra-high-temperature aerobic fermentation of a sludge including municipal sludge, livestock manure, crop straw, domestic waste, garden dry branches, and fallen leaves (claimed).    ADVANTAGE - The method is fast, has high fermentation temperature, kills pathogenic bacteria, has short fermentation period, completely avoids odor pollution, and has investment and operation cost reduced by more than 15%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fermentation initiating agent, comprising activating strain in an inclined plane activation culture medium flat plate, and culturing; preparing fermenting seed liquid by expanding strain amplification culture; mixing auxiliary material and conditioning agent, inoculating fermentation seed liquid, drying, and sieving.
NOVELTY - A cultivation substrate comprises 50-60 mass% white mulberry branch, 20-30 mass% cotton seed hull, 10-20 mass% Ganoderma lucidum, 5-10 mass% bran, 1-5 mass% corn flour, and 1-3 mass% calcium carbonate.    USE - Cultivation substrate for lucid ganoderma (claimed).    ADVANTAGE - The substrate has low cost and reduced production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivation of lucid ganoderma comprising preparing mulberry branch, air drying and crushing; mixing mulberry, lucid ganoderma dregs, bran, corn powder and calcium carbonate, adding water, and mixing; fermenting; packaging; sterilizing; and culturing.
NOVELTY - Producing 5-(2-(methylthio) ethyl)-hydantoin comprises taking methane, ammonia and oxygen as raw materials, mixing in a synthesis column, removing ammonia hydrocyanic acid mixture, adding methylthiopropanal base into a autoclave reactor, introducing hydrocyanic acid mixture into the first tank reactor, then introducing residual gas into vessel type reactor, performing catalysis reaction, passing propionaldehyde and a base group with reacted material, passing hydrogen cyanide into the mixture, and adding the mixture into the static mixing reactor.    USE - The method is useful for producing 5-(2-(methylthio) ethyl)-hydantoin (claimed).    ADVANTAGE - The method is capable of producing 5-(2-(methylthio) ethyl)-hydantoin in cost-effective and eco-friendly manner with high efficiency.    DETAILED DESCRIPTION - Producing 5-(2-(methylthio) ethyl)-hydantoin comprises taking methane, ammonia and oxygen as raw materials, mixing in a hydrogen cyanide synthesis column, adding hydrocyanic acid mixture into column for removal of ammonia, adding methylthiopropanal base from a multi-stage series tank reactor into a autoclave reactor, then progressively transferring to first tank reactor, introducing hydrocyanic acid mixture into the first tank reactor, then progressively introducing residual gas towards into discharge vessel type reactor, performing catalysis reaction to hydrocyanic acid and methylthiopropanal base, completing reaction of methylthiopropanal first tank reactor to produce 2-hydroxy-4-(methylthio) butyronitrile, passing propionaldehyde and a base group with reacted material into an autoclave reactor, continuously passing hydrogen cyanide into the mixture, adding the mixture into the static mixing reactor, passing two-hydroxy-4-(methylthio) butyronitrile with bicarbonate in an aqueous medium. An INDEPENDENT CLAIM is included for an apparatus for producing 5-(2-(methylthio) ethyl)-hydantoin.
NOVELTY - Oil of denier seed cake is extracted, and filtered until the relative density is 1.1-1.4, to obtain fluid extract. Obtained fluid extract is mixed with remaining water suspension, filtered, and obtained filtrate is concentrated, and extracted. The obtained aqueous phase layer is mixed with macroporous absorption resin, eluted with water, and then using ethanol aqueous solution and eluent is collected and mixed at 70-80 degrees C until the relative density is more than 1.40, to obtain fluid extract. Obtained extract is then dried to obtain sieboldianoside A.    USE - Extraction of sieboldianoside A (claimed).    ADVANTAGE - The method efficiently and economically provides high yield of sieboldianoside A having high productivity, using recyclable macroporous resin by simple method without affecting the environment.    DETAILED DESCRIPTION - Oil of denier seed cake is extracted using ethanol aqueous solution having concentration of 20-80 volume%, by cold soaking or reflux extracting. The resultant mixture is filtered at 70-80 degrees C under vacuum pressure of 0.05-0.10 MPa until the relative density is 1.1-1.4, to obtain fluid extract. The obtained fluid extract is mixed with remaining water suspension, filtered, and the obtained filtrate is concentrated, and extracted using ethyl acetate for 2-5 times, to obtain aqueous phase layer. The obtained aqueous phase layer is mixed with macroporous absorption resin, eluted with water, and then using ethanol aqueous solution having concentration of 20-90% and eluent is collected. The obtained eluent is mixed at 70-80 degrees C under vacuum pressure of 0.05-0.1 MPa until the relative density is more than 1.40, to obtain fluid extract. The obtained extract is then dried to obtain sieboldianoside A.
NOVELTY - A biomass methanol diesel oil comprises 100 pts. wt. diesel, 40-60 pts. wt. fatty acid methyl ester, 15-40 pts. wt. methanol and 2-20 pts. wt. cosolvent.    USE - Biomass methanol diesel oil.    ADVANTAGE - The diesel oil is cheap and environment-friendly. It has high flash point and cetane number, and good water resistance property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass methanol diesel oil comprising heating diesel at 25-50 degrees C, adding cosolvent, stirring, gradually adding fatty acid methyl ester and methanol, and mixing.
NOVELTY - Triflusal compounds (I) are new.    USE - (I) are useful for reducing thrombus formation and inhibiting increased platelet cyclic adenosine monophosphate levels.    ADVANTAGE - (I) can be easily prepared with high yield and purity in an eco-friendly manner.    DETAILED DESCRIPTION - Triflusal compounds of formula (Zn(2-OH-4-(CF3)-benzoicacid)2(pyrazole)2) (I) are new. An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - A high capacity hydrogen storage alloy comprises multi-component alloy of rare earth elements, zirconium, and magnesium in which copper is used to replace part of nickel.    USE - A high capacity hydrogen storage alloy for nickel-MH battery electrode (claimed).    ADVANTAGE - Thermal stability and electrochemical hydrogen adsorption and desorption at low temperature are improved, and ability of amorphous alloy formed by rapid quenching is increased, making it easy to obtain nanocrystalline amorphous structure.    DETAILED DESCRIPTION - A high capacity hydrogen storage alloy comprises multi-component alloy of rare earth elements, zirconium, and magnesium of formula Mg24-xREx-yZryNi12-zCuz in which copper is used to replace part of nickel.    RE=La, Sm, Nd, Pr, Y, and/or Ce;    x=3-8;    y=1-3; and    z=1-5.    An INDEPENDENT CLAIM is included for preparation of high capacity hydrogen storage electrode alloy which involves injecting molten alloy into casting mold to obtain cylindrical alloy cast ingot, placing ingot into quartz tube, induction heating to melt alloy under inert gas protection under low pressure to obtain liquid alloy, spraying liquid alloy through slit nozzle at the bottom of quartz tube while continuously rotating water-cooled copper surface of roller to obtain quenched alloy, crushing alloy into vacuum ball milling tank filled with highly pure argon gas, and ball milling in omni-directional planetary ball mill to obtain nanocrystalline alloy powder of amorphous structure.    DESCRIPTION OF DRAWING(S) - The drawing shows an X-ray diffraction spectrum of quenched and ball-milled alloy thin strip. (Drawing includes non-English language text).
NOVELTY - This new type utility claims one a whirlpool filter device, the set with one filtering groove, the filter groove set with water input end and output end connecting to the containing space, at least one guide base is set in the containing space, the guide base and the space between the form with one outer flow channel, the stream guidance base set with one inner flow channel, at least one power unit is set on the filtering groove, a produce one water flow or gas for the external flow channel and internal flow channel pushing pressure, one first filter unit in the inner flow channel in one separated first space, the first space is equipped with multi-first biological carrier, one of the second filtering unit in the outer flow channel separated in one second space, the second space is equipped with multi the second bio-carrier, the first and second biological carrier can be fully with the sewage, so as to improve the nitrifying bacteria decomposition efficiency and growth speed, capable of purifying the water quality so as to reach the function of water supply.
NOVELTY - This utility new type relates to used for biological treatment of sewage clarification device, include water, biological flocculation,, clarifier, sludge reflux area and sludge concentration area. Through matching of the six function area, the clarification device can form sludge circulating, which is helpful to reduce the carbon source, improving the microorganism concentration, hydrolysis, the hydrolysis acidification bacteria the sewage of the biodegradability, which is good for subsequent biological denitrification treatment to remove total nitrogen, a function to remove the suspended matter of primary traditional sedimentation tank.
NOVELTY - This utility new type relates to a energy-saving one bamboo charcoal firing system, include a furnace and a detachable of the carbonization in the furnace of a burning device, a carbonization kettle of top part set with a thermometer and an air outlet, wherein said air outlet through exhaust pipeline connecting filter of an inlet, the bottom of said filter is set with liquid phase outlet, the top part of said filter is set with gas pipeline, the gas pipeline connecting gas re-distributing device, wherein the fuel gas re-distributing device through air pipeline connecting a furnace of the combustion room, upper air pipeline are set with a flow control valve. This utility new type fuel in the firing process a produce of bamboo rear separating as gas of subsequent process, not only saves the distillate processing step of, at the same time, provide the bamboo carbon by firing of fuel, energy-saving and environment-friendly.
NOVELTY - This utility new type relates to a one agricultural system, especially claims a piggery marsh gas system one. The piggery marsh gas system, include piggery marsh gas tank, and lower part set with the pigsty manure passage, wherein: said excrement channel through vacuum pump is connected with the mixing tank, a mixing tank connect with the other cutter and sanitary processor, a mixing tank back connect with a first cooking pot, the first boiling tank and marsh gas tank. This utility new type of beneficial effects as follows: the piggery marsh gas tank and the contact more closely, a certain of excrement can be manufactured more marsh gas of multi-amount, simple structure, capable of continuous working, for the environment without any pollution, the utilization rate is high, the efficiency is high, piggery manure manufacturing marsh gas indicates the direction.
NOVELTY - This utility new type provide the a one intelligent marsh gas tank, belonging to the technical field of marsh gas. It solves the problem of temperature, pressure and biogas liquid amount in marsh gas tank in the existing technology is not capable of automatically regulating and so on. The intelligent marsh gas tank, marsh gas tank upper fixed with one energy conveying marsh gas conveying tube of the other end conveying tube of the one collecting tank, wherein the marsh gas in the marsh gas tank can be set with marsh gas tank for heating of a heating device, a feeding device for marsh gas tank capable of feeding of process and device can be for a reduced pressure of marsh gas tank, further set with temperature sensor, pressure sensor and liquid level sensor for marsh gas tank, and of a temperature sensor, pressure sensor and liquid level sensor are connected with one PLC programmable controller. This utility new type is capable of for temperature, pressure and biogas liquid amount in the marsh gas tank to realize automatic control.
NOVELTY - Synthesis of branched-chain amino acid nitrate comprises adding nitric acid into reaction container, stirring, slowly heating to 50 degrees C, adding leucine, keeping temperature for 0.5 hour until leucine is completely dissolved, heating to 60 degrees C, adding valine, keeping temperature for 0.5 hour until valine is completely dissolved, heating to 70 degrees C, adding isoleucine, keeping temperature for 0.5 hour until isoleucine is completely dissolved, filtering, cooling, crystallizing, separating crystals and drying at 80 degrees C and - 0.09 MPa.    USE - Method for synthesizing branched-chain amino acid nitrate (claimed).    ADVANTAGE - The simple and easy method has short time, high production efficiency and yield, and no wastewater, waste gas and waste residue. It produces pure product.
NOVELTY - Sequencing batch reactor device comprises sludge fermentation tank (1), fermented liquid separation tank (2), fermented liquid nitrogen and phosphorus pool (3), carbon storage tank (4), municipal sewage tank (5) and sequencing batch reactor (6).    USE - Sequencing batch reactor device used for removing nitrogen and phosphorus from municipal sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of sequencing batch reactor device comprising inoculating, fermenting at 25-30 degrees C and pH of 9-10 for 6-8 days, discharging to separation tank, separating, discharging to pool, adding magnesium salt and phosphate, collecting fatty acids in carbon storage tank, anaerobic mixing, aerobic stirring and discharging.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sequencing batch reactor device.    Sludge fermentation tank (1)    Fermented liquid separation tank (2)    Fermented liquid nitrogen and phosphorus pool (3)    Carbon storage tank (4)    Municipal sewage tank (5)    Sequencing batch reactor (6)
NOVELTY - Removing gallic acid from wastewater using Aspergillus oryzae bacteria involves taking Aspergillus oryzae as starting strain, adding to a test tube containing culture medium, shaking culture liquid, conducting amplification of culture liquid, centrifugally collecting thalli, and then removing gallic acid from wastewater.    USE - For removing gallic acid from wastewater (claimed), where gallic acid is used as hydrophilic small molecular organic acid in drinking water purification; as important raw material in the production of medicines; and for controlling water pollution.    ADVANTAGE - The method effectively removes gallic acid from wastewater; has short process time; and has higher gallic acid removing rate i.e. removes 70-100% of gallic acid. The method provides improved water pollution control.
NOVELTY - A method of degradation of insect wax bacterial gallic acid involves: taking insect wax bacteria analogue culture as starting strain in test tube, shaking the liquid culture, amplification the culture liquid, centrifugally collecting the bacterial cell, and then removing the bacterial gallic acid in waste water.    USE - In the degradation of insect wax bacterial gallic acid in waste water (claimed).    ADVANTAGE - The method shows gallic acid removing rate of 70-100%.
NOVELTY - Removing gallic acid from wastewater using Phanerochaete chrysosporium fungus involves taking Phanerochaete chrysosporium as starting strain, adding to a test tube containing culture medium, shaking culture liquid, conducting amplification of culture liquid, centrifugally collecting thalli, and then removing gallic acid from wastewater.    USE - For removing gallic acid from wastewater (claimed), where gallic acid is used as hydrophilic small molecular organic acid in drinking water purification; as important raw material in the production of medicines; and for controlling water pollution.    ADVANTAGE - The method effectively removes gallic acid from wastewater; has short process time; and has higher gallic acid removing rate i.e. removes 70-100% of gallic acid. The method provides improved water pollution control.
NOVELTY - A method of degradation of Phanerochete chrysosporium gallic acid involves: taking Phanerochete chrysosporium culture as starting strain in test tube, shaking the liquid culture, amplification the culture liquid, and liquid fermentation to remove gallic acid in waste water.    USE - In the degradation of Phanerochete chrysosporium gallic acid in waste water (claimed).    ADVANTAGE - The method shows gallic acid removal rate of 60-100%.
NOVELTY - Continuous sludge denitrification device comprises water tank (1), water inlet (2), reactor (3), sedimentation tank (4), sieve filter (5), filter screen (6), overflow weir (7), sludge reflux pump (8), overflow port (9), valve (10), fixed filler (11), dissolved oxygen monitor (12), stirrer (13), air compressor (14) and gas flow meter (15).    USE - Continuous sludge denitrification device.    ADVANTAGE - The device has ammonia removal efficiency of not less than 90% and nitrogen removal efficiency of not less than 50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the continuous denitrification of sludge comprises soaking polyurethane filler, partial nitrifying-anaerobic ammonia oxidizing, adsorbing, mixing with activated sludge at concentration of 3000-5000 mg/L in reactor (3), vaccinating, nitrifying wastewater at dissolved oxygen of 0.5 mg/L, drying to remove 0.1 kg ammonia, feeding water from water tank (1), mixing at dissolved oxygen of 0.2-0.3 mg/L and sludge recycle ratio of 50-100%, mixing, increasing water in bioreactor at water concentration of not greater than 50 mg/L and nitrite concentration of 1 mg/L to remove 0.8 kg nitrogen, adjusting gas flow meter (15), maintaining dissolved oxygen at 0.5-0.8 mg/L, filtering mixture at aperture diameter of 0.5 mm, filtering at 0.18 mesh, and monitoring dissolved oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of continuous sludge denitrification device.    Water tank (1)    Water inlet (2)    Reactor (3)    Sedimentation tank (4)    Sieve filter (5)    Filter screen (6)    Overflow weir (7)    Sludge reflux pump (8)    Overflow port (9)    Valve (10)    Fixed filler (11)    Dissolved oxygen monitor (12)    Stirrer (13)    Air compressor (14)    Gas flow meter (15)
NOVELTY - Sewage flocculant comprises polyacrylamide, citric acid, composite microorganism, polymerized ferric chloride and bentonite.    USE - Sewage flocculant used for reducing sewage turbidity.    ADVANTAGE - The flocculant improves sewage treatment efficiency.
NOVELTY - Rotating disk device comprises rotating disk unit (1), return unit (2), water inlet (3), rotating shaft (4), sludge collecting groove (5), solid-liquid separating unit inlet (6), solid-liquid separating unit outlet (7), sludge reflux tube (8), electromagnetic valve relay (9), return tube (10), outer reflux pipeline (11), wastewater inlet (12), rotating disk sheet (13), unit water inlet and sludge outlet (14), and unit sludge supernatant outlet (15).    USE - Rotating disk device used for enhanced denitrifying and handling sludge.    ADVANTAGE - The convenient and energy-saving device has high denitrifying efficiency and low sludge yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of rotating disk device.    Rotating disk unit (1)    Return unit (2)    Water inlet (3)    Rotating shaft (4)    Sludge collecting groove (5)    Solid-liquid separating unit inlet (6)    Solid-liquid separating unit outlet (7)    Sludge reflux tube (8)    Electromagnetic valve relay (9)    Return tube (10)    Outer reflux pipeline (11)    Wastewater inlet (12)    Rotating disk sheet (13)    Unit water inlet and sludge outlet (14)    Unit sludge supernatant outlet (15)
NOVELTY - Treatment of wastewater from food industry comprises introducing wastewater into tank, determining pH, adjusting pH to 6.5-7.5, adding physical water purifying agent at mass ratio of 1:0-80, stirring, standing for 30-60 minutes, filtering to remove residue, introducing hydrogen peroxide into filtrate at mass ratio of 1:150-300, treating with enzyme at 1/300-1/200 times the weight of wastewater, adsorbing impurities, metal ions and bacteria using activated carbon, performing upflow anaerobic sludge bed treatment, and discharging treated wastewater.    USE - Method for treating wastewater from food industry (claimed).    ADVANTAGE - The method has good treatment effect with reduced pH, chroma, COD, BOD5, sulfides, nitrides and organic phosphorus levels compared to required standards.    DETAILED DESCRIPTION - Treatment of wastewater from food industry comprises introducing wastewater into tank, determining pH, adjusting pH to 6.5-7.5 by adding base into acidic wastewater or adding acid and/or injecting carbon dioxide gas into alkaline wastewater, adding physical water purifying agent comprising diatomite, calcium aluminate and aluminum chlorohydrate at mass ratio of 1:0-80, stirring, standing for 30-60 minutes, filtering to remove residue, introducing hydrogen peroxide into filtrate at mass ratio of 1:150-300, treating with enzyme by adding catalase, laccase, lipoxygenase and phytase at 1/300-1/200 times the weight of wastewater, adsorbing impurities, metal ions and bacteria using activated carbon, performing upflow anaerobic sludge bed treatment, and discharging treated wastewater.
NOVELTY - Ecological organic fertilizer and its preparation method, are claimed. The ecological organic fertilizer comprises 60-80 pts. wt. livestock manure, 5-15 pts. wt. adsorbent, 5-20 pts. wt. calcium oxide, and 1-10 pts. wt. trace element.    USE - The ecological organic fertilizer is useful for improving soil and crop quality.    ADVANTAGE - The ecological organic fertilizer can be used for long period of time, and does not cause pollution.
NOVELTY - Composite fertilizer comprises straw, weathered coal, peat, powdered rock phosphate, potassium mineral powder, EDTA, potassium fulvate, rice hull powder, sweet potato powder, mixed strain powder, carbamide, and urea.    USE - The composite fertilizer is useful for improving soil texture, and preventing soil-borne disease.    ADVANTAGE - The fertilizer acts for long period of time and cost-effective, contains no residue, and causes no pollution.
NOVELTY - Organic fertilizer contains 16-26 pts. wt. potassium dihydrogen phosphate, 35-45 pts. wt. urea, 15-20 pts. wt. ammonium dihydrogen phosphate, 0.001-0.002 pts. wt. Trichoderma powder, 0.001-0.002 pts. wt. yeast powder, 2-8 pts. wt. potassium powder (potassium ore), 1-4 pts. wt. stone powder, 3-6 pts. wt. grass powder, 2-8 pts. wt. conch shell powder, 25-30 pts. wt. mustard straw powder, 3-5 pts. wt. clamshell powder, 11-20 pts. wt. clamshell powder, 15-20 pts. wt. straw powder, and 15-20 pts. wt. clamshell powder.    USE - The organic fertilizer is useful for tea (claimed).    ADVANTAGE - The organic fertilizer contains nitrogen, phosphorus, potassium, and trace elements, and provides balanced nutrients.    DETAILED DESCRIPTION - Organic fertilizer comprises 16-26 pts. wt. potassium dihydrogen phosphate, 35-45 pts. wt. urea, 15-20 pts. wt. ammonium dihydrogen phosphate, 0.001-0.002 pts. wt. Trichoderma powder, 0.001-0.002 pts. wt. yeast powder, 2-8 pts. wt. potassium powder (potassium ore), 1-4 pts. wt. stone powder, 3-6 pts. wt. grass powder, 2-8 pts. wt. conch shell powder, 25-30 pts. wt. mustard straw powder, 3-5 pts. wt. clamshell powder, 11-20 pts. wt. clamshell powder, 15-20 pts. wt. straw powder, 15-20 pts. wt. clamshell powder, 5-9 pts. wt. sawdust, 5-9 pts. wt. cypress powder, and 0.001-0.002 pts. wt. actinomycetes powder.
NOVELTY - Preparation of poly-substituted fused ring compound involves reacting N-acyl (II) and aromatic amine (III) as raw material, rhodium salt as catalyst, and copper salt as oxidant, and heating the reaction in the organic solvent.    USE - Preparation of poly-substituted fused ring compound used in organic semiconductor maerial and light emitting material.    ADVANTAGE - The poly-substituted fused ring compound is economically prepared with high economical efficiency without polluting the environment, by a simple method.    DETAILED DESCRIPTION - Preparation of poly-substituted fused ring compound involves reacting N-acyl of formula (II) and aromatic amine of formula: R2-CC-R3 (III) as raw material, rhodium salt as catalyst, and copper salt as oxidant, and heating the reaction in the organic solvent. The poly-substituted fused ring compound is of formula (I).    R=alkyl or aryl;    R1=H, alkyl, aryl, alkoxy, halo, cyanomethyl or acid group;and    R2,R3=alkyl, alkenyl, alkynyl or aryl.
NOVELTY - Methanol gasoline stabilizer comprises 18.0-31.0 mass% 2-octylamine, 15.0-29.5 mass% N-tert-butyl-piperazine, 15.0-24.5 mass% 4-N-butoxy-benzonitrile, 13.0-24.0 mass% allyl phenoxyacetate, 10.0-20.5 mass% 1,3-acetone dicarboxylic acid diethyl ester, and 9.0-19.5 mass% 3-dimethylaminoanisole.    USE - Methanol gasoline stabilizer.    ADVANTAGE - The methanol gasoline stabilizer greatly improves the methanol gasoline storage stability and anti-water phase separation property based on engine bench testing and actual road driving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of methanol gasoline stabilizer comprising adding 0.4-0.8 mass% methanol gasoline stabilizer to methanol, ultrasonically processing to mix uniformly, and remodulating.
NOVELTY - Biodiesel is produced by reacting oil (A) and dimethyl carbonate in microstructured reactor in the presence of liquid alkali catalyst to rapidly generate biodiesel product comprising fatty acid methyl ester and glycerol carbonate.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method is simple, fast and can achieve a biodiesel product yield of more than 95 %. It employs microstructured reactor to promote good raw material mass transfer so as to greatly shorten the reaction time. It uses dimethyl carbonate as replacement for low-carbon alcohol transesterification reagent (such as methanol or ethanol) employed in the prior art, thus eliminating the generation of glycerol by-product and improving the product quality. Further, the catalyst employed does not cause device corrosion and can be used repeatedly, thus realizing clean production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microstructured reactor employed in producing biodiesel, comprising micromixer unit and microreactor unit.
NOVELTY - Sealing structure for marsh gas fermentation tank (1) having 20 cm deep water tank (5), comprises cover (2) inserted into the marsh gas fermentation tank, which functions as a water seal to prevent gas leakage.    USE - As seal for marsh gas fermentation tank to prevent the leakage of biogas generated from e.g. organic matter, human and animal manure, kitchen garbage, paper, pulp waste, sewage and sludge.    ADVANTAGE - The system has simple and eco-friendly structure; provides high air tightness; has safe and easy handling; is convenient and practical; and has low construction cost.    DESCRIPTION OF DRAWING(S) - The figure shows schematic diagram of sealing structure for marsh gas fermentation tank.    Tank body (1)    Cover (2)    Handle (3)    Air outlet (4)    Water tank (5)
NOVELTY - A conical small-sized methane generator comprises a methane generator tank body (1), a cover (2), a handle (3), a gas outlet (4), a water tank (5), a discharge port (6), and a bracket (7).    USE - As conical small-sized methane generator (claimed).    ADVANTAGE - The conical small-sized methane generator is simple in structure, convenient and practical; has easy management, and low cost; saves ground space; and has safety and no pollution to the environment.    DESCRIPTION OF DRAWING(S) - The figure shows a view of the conical small-sized methane generator.    Methane generator tank body (1)    Cover (2)    Handle (3)    Gas outlet (4)    Water tank (5)    Discharge port (6)    Bracket (7)
NOVELTY - Automatic biogas transformer comprises two floating cylinders (2) in a rectangular water tank (1), where two-point power supply is connected with power-driven pulley (12, 13) for automatic operation of double floating-cylinders and automatic conversion to methane gas.    USE - As double floating-cylinder automatic transformer for low-pressure gas production such as biogas and marsh gas i.e. methane gas.    ADVANTAGE - The system has dual automatic swing pieces of floating cylinders which can automatically convert the material of biogas fermentation tanks into the methane gas by using low-pressure.    DESCRIPTION OF DRAWING(S) - The figure shows schematic diagram of double floating-cylinder automatic transformer.    Water tank (1)    Float cylinder (2)    Valves (5, 6, 7, 8)    Pulley (12, 13)    Floating jar (14, 15)    Outlet tube (16)
NOVELTY - A single-piece floating cylinder transformer (1) comprises single floating cylinder (3), a water tank (2), a bracket (8), a pulley (7), and a steel wire rope (6) composed of moving parts floating cylinder pressure transformation.    USE - As single-piece floating cylinder transformer (claimed) for producing biogas at low pressure, for pressing a bottom of marsh gas device.    ADVANTAGE - The single-piece floating cylinder transformer is effective for producing biogas e.g. methane at low pressure.    DESCRIPTION OF DRAWING(S) - The figure shows a view of the single-piece floating cylinder transformer.    Single-piece floating cylinder transformer (1)    Water tank (2)    Floating cylinder (3)    Air tube (4)    Wire rope (6)    Pulley (7)    Bracket (8)
NOVELTY - A marsh gas collecting and storing device for collecting and storing marsh gas, comprises: a collecting cover (40), a support frame, marsh gas tank, and an exhaust port (42); where the collecting cover is set with the heavy object (41) at periphery of the support frame; where the collecting cover is provided with an upper end of the exhaust port, and where the air outlet is set with valve.    USE - For collecting and storing marsh gas (claimed) use in the poultry and livestock excrement processing field.    ADVANTAGE - The marsh gas collecting and storing device has simple structure, and is economical.    DESCRIPTION OF DRAWING(S) - The figure shows a marsh gas collecting and storing device.    Collecting cover (40)    Heavy object (41)    Exhaust port (42); (42)    Pipeline (50)    Storage bin (60)
NOVELTY - Bacillus cereus strain GIGAN2 has a preservation number (CCTCC NO: M2013395), and is new.    USE - Bacillus cereus strain used for degrading dimethyl disulfide (claimed).    ADVANTAGE - The Bacillus cereus strain is eco-friendly in nature and efficiently degrades dimethyl disulfide present in air, water or soil.
NOVELTY - A facultative anaerobic Sinibacillussoli strain GD05 (CGMCC 1.12538), is new.    USE - The facultative anaerobic Sinibacillussoli strain GD05 is useful in biological bleaching agents for azo dyes (all claimed) e.g. azo gold and azo orange in wastewater biological systems.    ADVANTAGE - The facultative anaerobic Sinibacillussoli strain GD05 has bleaching rate of 83%.
NOVELTY - A Pseudomonas stutzeri KY-02 strain is new.    USE - As Pseudomonas stutzeri KY-02 strain for degradation of epichlorohydrin in industrial waste water (claimed).    ADVANTAGE - The Pseudomonas stutzeri KY-02, without influencing the anaerobic digestion reaction system of stability, can improve the efficiency and sludge biogas anaerobic decomposition rate of organic matter. Compared with chemical methods, has low cost, long duration, no secondary pollution, training and easy to use, for industrial wastewater biological treatment technologies, especially further promotes and popularizes anaerobic digestion technology to make a positive contribution in the field of wastewater treatment, and has broad application prospects.    DETAILED DESCRIPTION - A Pseudomonas stutzeri KY-02 strain is new. The Pseudomonas stutzeri KY-02 strain is obtained by: isolating strain from activated sludge to give a white edge tidy flat, moist sticky, gram-negative strain; through 16SrDNA and Biolog Microbial Identification System identification, identified as Pseudomonas stutzeri (Peudomonas stutzeri KY-02), which has a sequence containing 1434 base pairs (SEQ ID NO: 1) as given in the specification. An INDEPENDENT CLAIM is included for degradation of epichlorohydrin involving inoculating Peudomonas stutzeri KY-02 strain to LB medium at 30 degrees C, shaking culture to bacteria concentration 0.D of 2.0 and inoculum size of 1-5%, inoculating with epoxy chloropropane waste water, culturing at 20-30 degrees C for 1-3 days to maintain the dissolved oxygen content of more than 3.0 parts per million (ppm) to achieve epoxy chloropropane degradation.
NOVELTY - Preparation of fuel involves: preproces organic waste, feeding it to anaerobic fermentation tank and secondary anaerobic fermentation tank, then desulfurizing to obtain pure marsh gas, subjecting the pure marsh gas into a buffer tank, filtering the gas through three-level filter, heating the obtained marsh gas at 50 degrees C, performing decarburization into separation membrane module, discharging the isolated impurity from the system, separating out natural gas, compressing it to compressed natural gas (CNG), or delivering to air column or a natural gas intake manifold.    USE - For the preparation of fuel which is useful for vehicles (claimed).    ADVANTAGE - The present method by using common organic waste produces methane biogas with purity increased to 97% greater than the national standards of vehicle gas; and is simple and environmental-friendly.    DETAILED DESCRIPTION - Preparation of fuel involves: preprocessing organic waste, feeding it to anaerobic fermentation tank and secondary anaerobic fermentation tank, then desulfurizing to obtain pure marsh gas, subjecting the pure marsh gas into a buffer tank, filtering the gas through three-level filter, heating the obtained marsh gas at 50 degrees C, performing decarburization into separation membrane module, discharging the isolated impurity from the system, separating out natural gas, compressing the natural gas to compressed natural gas (CNG) at pressure of 1.5-2MPa, preferably 1.7 MPa, or delivering to air column or a natural gas intake manifold for automotive use. The first anaerobic fermentation temperature is 53-57 degrees C, and fermentation period is 15-20 day, with pH level of 6.8-7.4.
NOVELTY - Preparing biogas fermentation additive involves: (1) drying and grinding fresh sweet potato into powder, adding water and mixing, and then adding potassium sulfate, heating, to obtain extracting mixed suspension; (2) filtering the suspension to obtain a filtrate; (3) adding cellulose, agar, stearic acid, peptone and water in the resulting filtrate, raising the temperature and then cooling to obtain mixture (m1); (4) adding organic acid, methyl oleate, soya bean lecithin, surface active agent and water, in the mixture (m1), followed by heating, concentrating and drying.    USE - For preparing biogas fermentation additive (claimed).    ADVANTAGE - The method provides additive in short fermentation period, and improves marsh gas production.    DETAILED DESCRIPTION - A method of preparing biogas fermentation additive, involves: (1) taking 10-15 pts.wt. of fresh sweet potato, drying, grinding into powder, adding 40-60 pts.wt. of water and mixing uniformly, and then adding 1-2 pts.wt. of potassium sulfate, heating at 40-50 degrees C for 3-5 hours, cooling to room temperature, to obtain extracting mixed suspension; (2) filtering the suspension through a plate and frame filter press to obtain a filtrate; (3) adding 5-9 pts.wt. of cellulose, 2-3 pts.wt. of agar, 2-3 pts.wt. of stearic acid, 2-3 pts.wt. of peptone and 2-3 pts.wt. of water in the resulting filtrate and stirring, raising the temperature to 40-50 degrees C for 20-40 minutes, and cooling to obtain a mixture (m1); (4) adding 1-3 pts.wt. of organic acid, 1-3 pts.wt. of methyl oleate, 1-3 pts.wt. of soya bean lecithin, 1- 3 pts.wt. of surface active agent, and 1-3 pts.wt. of water, in the mixture (m1), and stirring, raising the temperature to 30-40 degrees C for 20-40 minutes, cooling, concentrating, and spray drying to obtain the additive.
NOVELTY - Preprocessing corn straw, comprises (i) preprocessing corn straw by adding perchloric acid and ethylene glycol into a water preprocessing system; (ii) adding deionized water and regenerated cellulose, and washing regenerated cellulose material thrice with deionized water; (ii) adding 50 mM acetic acid and sodium acetate buffer solution mixed system having pH of 4.8; (iv) adding 5% corn straw substrate and 0.3% cellulase enzyme, subjecting to oscillating reaction at 180 rotations/minute in a shaker, and performing enzymatic hydrolysis to achieve high efficient saccharification of corn straw.    USE - The method is useful for preprocessing corn straw (claimed).    ADVANTAGE - The method reduces sugar yield by more than 65%; and is simple, and economical; and produces less waste.    DETAILED DESCRIPTION - Preprocessing corn straw, comprises (i) preprocessing corn straw at 110-130 degrees C for 15-60 minutes by adding perchloric acid, ethylene glycol and water forming a preprocessing system; (ii) adding deionized water and regenerated cellulose raw material, and washing regenerated cellulose material thrice with deionized water; (ii) adding 50 mM acetic acid and sodium acetate buffer solution mixed system having pH of 4.8; (iv) adding 5% corn straw substrate and 0.3% cellulase enzyme, subjecting to oscillating reaction at 180 rotations/minute under constant temperature in a shaker, and performing enzymatic hydrolysis to achieve high efficient saccharification of corn straw.
NOVELTY - Method for producing biohydrogen from oraganic waste involves (a) anaerobically digesting sewage sludge in sewage treatment plant, (b) adding a nutrient solution of soluble starch as reaction substrate, (c) placing the sewage sludge and the reaction substrate in a fermantation vessel, fermenting by controlling the temperature at 35-36 degrees C, maintaining pH at 5-6, and stirring the mixture, and (d) collecting the gas emitted after fermentation using airbags, and measuring the volume gas emitted using saturated salt solution.    USE - The method is useful for producing biohydrogen from organic waste (claimed).    ADVANTAGE - The method not only makes waste reusable but also cleans the waste, requires less equipments, is easy, and operates under mild conditions.
NOVELTY - The device (2) has a measuring chamber (4) through which measurement gas is made to flow, and an input arranged at an infrared radiation source (3). A detector is arranged at an output for detecting gas concentration analysis by absorption losses weakened at a light beam and passed to an electronic measured variable processing unit (7). The electronic measured variable processing unit determines the gas concentration of total carbon contained in the measurement gas other than analyzing pollutant components of a spectral region of 1000-3200 per cm.    USE - Optical gas analyzer device for use with an exhaust system i.e. industrial chimney, of a waste-incineration plant.    ADVANTAGE - The electronic measured variable processing unit determines the gas concentration of total carbon contained in the measurement gas other than analyzing pollutant components of the spectral region of 1000-3200 per cm, so that the device analyzes the pollutant components of exhaust gases in a simple manner from the total carbon with small effort and high accuracy.    DETAILED DESCRIPTION - The pollutant components are selected from a pollutant component group consisting of carbon monoxide, sulfur dioxide and nitrogen oxide. An INDEPENDENT CLAIM is also included for a method for operating an optical gas analyzer device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block circuit diagram of an optical gas analyzer device at a waste-incineration plant.    Exhaust system (1)    Optical gas analyzer device (2)    Infrared radiation source (3)    Measuring chamber (4)    Electronic measured variable processing unit (7)
NOVELTY - Preparation of a functional seaweed fertilizer comprises preparing 6-8 mass% alkaline protease enzyme; and carrying out anaerobic fermentation of microorganism in exogenous high protein content, rich polypeptide, peptide, amino acid, and organic acid, low probiotics, phytic acid, and tannin, and low anti-nutritional content factors.    USE - Method for the preparation of a functional seaweed fertilizer (claimed).    ADVANTAGE - The method is inexpensive. The fertilizer keeps rich nutrient substance in seaweeds.
NOVELTY - This utility new type provide a multifunctional low-tension water-cooling jacket one gasification furnace, said furnace body comprises a furnace chamber and is provided with an outer wall of the furnace chamber water cooling jacket, a furnace body upper part is provided with an inlet, the bottom is provided with a slag water outlet, a furnace chamber comprising a gasification room and lower chilling room of upper part, a gasification room and the chilling room is provided with a water cooling disk tube mouth, the lower part of said water cooling jacket is provided with a jacket water inlet, the top part is provided with a jacket water outlet, upper part of said water cooling jacket is provided with a expansion of the corrugated furnace shell, a chilling room of upper side wall form a gas outlet. Said gasification furnace is compact in design, an expansion uniformity, temperature distribute reasonable. Capable of binding powder coal, water-coal-slurry and biomass fuels such as process process test, up the control and operation of the temperature is simple and feasible, device structure is simple, the operation effect is good.
NOVELTY - This utility new type claims a one tail gas recycling preparation of liquefied natural gas device, comprising a raw material gas purifying unit, refrigerating compressor unit, liquefied unit, LNG storage unit, unit, raw material gas purifying unit, the raw material gas for operation process, and the rear of liquefied gas to process liquefied operation unit, refrigerating compressor unit, for taking the nitrogen pressurizing cooling operation, and rear refrigeration by expansion of low temperature gas to the liquefaction unit, liquefaction unit, of LNG for receive raw material gas from the of operation and operation of low temperature compressed gas, rear control raw material gas at low temperature gas cooling process separating operation, and the separating and conveying to the storage operation, this utility new type can, can be recycled and preparation of liquefied natural gas in the tail gas of method can be valid energy-saving measure of enterprise, reduces the resource consumption of the energy of the enterprise.
NOVELTY - This new type utility claims one methane of a preparation system, comprising a raw material gas purifying unit, refrigerating compressor unit, liquefied unit, LNG storage unit, raw material gas purifying unit, the raw material gas for purifying process operation, and the rear purifying of liquefied gas to process liquefied operation unit, refrigerating compressor unit, for taking the nitrogen pressurizing cooling operation, and rear refrigeration by expansion of low temperature gas to the liquefaction unit, liquefaction unit, of LNG for receive raw material gas from the purifying operation of and operation of low temperature compressed gas, rear control raw material gas at low temperature gas cooling process separating operation, and the separating and conveying to the storage operation, this utility new type can, can be recycled and preparation of liquefied natural gas in the tail gas of method can be valid energy-saving measure of enterprise, reduces the resource consumption of the energy of the enterprise.
NOVELTY - Method for recovering progesterone from progesterone producing mother liquid involves pre-treating mother liquid by performing distillation process, evaporating the progesterone producing mother liquor using solvent, performing oxidation on the mother liquid, increasing the purity of the progesterone in the obtained liquid, refluxing and separating the progesterone, and adding e.g. cyclohexanone, extracting the product, and adding e.g. crystallized solvent, and alumina, cooling and crystallizing the mixture, and refining the crude product.    USE - The method is useful for recovering progesterone from progesterone producing mother liquid (claimed).    ADVANTAGE - The method enables to recover progesterone environmentally-friendly with improved yield of 4%.    DETAILED DESCRIPTION - Method for recovering progesterone from progesterone producing mother liquid involves pre-treating mother liquid by performing distillation on progesterone producing mother liquid, evaporating the progesterone producing mother liquor in solvent and recording the residual weight Ml, performing oxidation on the mother liquid, dissolving the residues using solvent to obtain mother liquid, removing impurities and washing the liquid using diluted acid solution, until the pH is more than 6, increasing the purity of the progesterone in the obtained solution by refluxing and separating the progesterone using absolute ethyl alcohol, measuring and calculating the weight of water (M2) and progesterone (M3), adding isobutyl ketone, cyclohexanone and aluminum isopropoxide to the separated progesterone, extracting the product by adding oxidized acid solution to the progesterone, washing the mixture, and evaporating solvent, adding crystallized solvent, activated carbon, and alumina, filtering, cooling and crystallizing the mixture to obtain crude product of progesterone, and refining the crude product.
NOVELTY - Described is a method of preparing a catalyst for oxidative condensation of methane to C2+ hydrocarbons, which involves depositing manganese and sodium tungstate on a silicon dioxide support via successive impregnation thereof with aqueous solutions of manganese nitrate and then sodium tungstate, followed by calcination in air at temperature of 800 degrees C, wherein the obtained composition Mn - Na2WO4/SiO2 with total content of manganese of 1-2 wt % and sodium tungstate of 3-5 wt % is mixed with an inert material which actively absorbs microwave energy, based on a metal carbide with weight ratio of components of 2-4:1, respectively. Described is a method for oxidative condensation of methane to C2+ hydrocarbons in the presence of a catalyst obtained using the method described above.    USE - Chemistry.    ADVANTAGE - High conversion of methane and high selectivity with respect to C2+ hydrocarbons.6 cl, 2 tbl, 2 ex
NOVELTY - Decomposition of water from power plant involves supplying pressurized reactants including water and carbon dioxide to a reactor arranged in a hermetic vessel comprising catalyst, obtaining product by reacting hydrogen, and oxygen in reactor having separator in presence of catalyst, and separating reaction products from reactants, and obtained intermediate reaction products by releasing hydrogen from gaseous phase.    USE - Decomposition of water from power plant from power plant (claimed).    ADVANTAGE - The method enables efficient decomposition of water and recovery of carbon dioxide and hydrogen.
NOVELTY - Catalyst comprising an alumina catalyst support in which a surface is modified with magnesium oxide, an active component including nickel and cobalt, and a catalyst promoter including calcium oxide is new. The active component and the catalyst promoter are supported on the catalyst support. The surface has spinel structure (I).    USE - The catalyst is useful for steam reforming methane within COG (all claimed) in a blast furnace for the preparation of hydrogen fuel.    ADVANTAGE - The catalyst has good dispersibility and sintering resistivity, and improves quality of the hydrogen fuel.    DETAILED DESCRIPTION - Catalyst comprising an alumina catalyst support in which a surface is modified with magnesium oxide, an active component including nickel and cobalt, and a catalyst promoter including calcium oxide is new. The active component and the catalyst promoter are supported on the catalyst support. The surface has spinel structure of formula (CaO-Ni-Co/MgO-Al2O3) (I). INDEPENDENT CLAIMS are included for:    (1) producing catalyst; and    (2) steam reforming a methane contained in coke oven gas (COG) by supplying the catalyst.
NOVELTY - Genetically modified Saccharomyces cerevisiae is obtained by using strains of yeast i.e. Saccharomyces cerevisiae and bacteria, where the bacteria provides plasmid that encode xylose isomerase of Burkholderia cenocepacia. Saccharomyces cerevisiae comprises genes that express xylose reductase, xylitol dehydrogenase and xylulokinase. xylA gene of Burkholderia cenocepacia is inserted via plasmid vector (PGK-pYEP). Saccharomyces cerevisiae is provided for expressing xylose isomerase (XI).    USE - Genetically modified Saccharomyces cerevisiae used for glucose and xylose fermentation of biomass hydrolysates for producing ethanol (all claimed).
NOVELTY - In preparation of glycosidase inhibitor medicine for preventing and treating II type diabetes, 3 alpha -akebonolic acid is used.    USE - For preparing used in preparation of glycosidase inhibitor medicine for preventing and treating II type diabetes.    ADVANTAGE - The preparation process is simple, easy to operation, and the time using plant fruit extraction process also can make plant itself without being damaged and obtain a long time, at the same time obtains good economic benefit of also can for is environment-friendly, and the monomer compound is stable and easy to store. The alpha -glycosidase inhibition activity of the compound is higher than even clinical medicine acarbose.    DETAILED DESCRIPTION - In preparation of glycosidase inhibitor medicine for preventing and treating II type diabetes, 3 alpha -akebonolic acid of formula (I) is used. An INDEPENDENT CLAIM is included for preparing 3 alpha -akebonolic acid involving preparing total extract of the caulis akebiae, crushing Akebia Stem or long through stem, leaf or fruit using ethanol aqueous solution, ethanol, acetone water solution or acetone leaching, extraction liquid is concentrated to remove ethanol or acetone, obtain the total extract, the total extract crude extract is suspended in water, using petroleum ether, petroleum ether extract, concentrating the rear obtain total petroleum ether extract, separating and purifying the total extract by petroleum ether and the silicon glue column chromatography, eluant to petroleum ether/acetone, from the volume ratio of 100:0, 20:1, 5:1, 2:1, 1:1, 0:100 gradient elution, collecting fraction of petroleum ether/acetone 5:1 vol./vol.%, the gel LH-20 column chromatography separation, eluting acetone and re-crystallizing and purifying to obtain compound 3 alpha -akebonolic acid.
NOVELTY - Applying biomineralization of soil involves adding suitable bacteria in soil for promoting biomineralization of soil nutrient.    USE - Method for applying biomineralization of soil for improving soil (claimed).    ADVANTAGE - The method enables to improve soils geotechnical properties and provide improved hydraulic and mechanical behavior.
NOVELTY - Preparation of ruthenium (III) complex comprises reacting indazole bromide-trans-(tetrachloro-(1H-indazole) ruthenate), hydrochloric acid, and sodium chloride in water and chloroform solvent and under protection of nitrogen; cooling mixture; removing excess indazole hydrochloride using water layer by chloroform; precipitating liquid to obtain pale yellow crude product; and refining by ethanol to obtain sodium-trans-(tetrachloro-(1H-indazole) ruthenate).    USE - Preparation of ruthenium (III) complex, i.e. sodium-trans-(tetrachloro-(1H-indazole) ruthenate) used for treating tumor (claimed).    ADVANTAGE - The method has simple and easy operation, provides product with high yield and purity as compared to existing product, has cheap and easy to obtain raw materials, has reduced production cost, provides effective conversion rate, simple post treatment, uses recyclable solvent, and environment friendly.
NOVELTY - The device has a decomposing chamber (6) formed with an inlet (1) for inflow of sludge particles (2). A sludge blanket (3) is connected with the decomposing chamber. A biogas collector (7) collects biogas that is sent to a boiler. Biogas outlet (8) is utilized to release the biogas from the decomposing chamber. A power generator generates electrical energy using the biogas.    USE - Biogas treating device for urban power generation.    ADVANTAGE - The device completely utilizes the biogas to improve power generation efficiency in a simple manner, reduces environmental pollution, and avoids damage to installed equipments.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas treating device.    Inlet (1)    Sludge particles (2)    Sludge blanket (3)    Decomposing chamber (6)    Biogas collector (7)    Biogas outlet (8)
NOVELTY - The compost comprises ash obtained from incineration of plant and biomass, where amount of the compost is 0.5-10 wt%.    USE - Compost.
NOVELTY - Producing Streptomyces JSD-1 strain by straw degradation comprises preserving strain at 20 degrees C or low temperature freezing preservation method to reduce metabolism speed so as to achieve preservation strain; strain activation by using yeast extract malt extract (YEME) liquid culture medium; and inoculating the strain to gradually adapt culturing environment process.    USE - The method is useful for producing Streptomyces JSD-1 strain by straw degradation. The Streptomyces JSD-1 strain is used for biological prevention and control of plant pathogenic bacteria such as tomato and rice bakanae disease (all claimed).    ADVANTAGE - The Streptomyces JSD-1 strain provides strong resistance to plant pathogen (such as tomato and rice bakanae disease), and has good application potential in high temperature fertilizer.
NOVELTY - The device control method involves establishing a fuzzy logic (FL) control rule base in a controller. An input signal conditioning circuit converts an aerobic fermentation environment signal into a digital signal. The digital signal is transferred to the controller to generate a first grade output quantity and an FL control amount. The output quantity and the control amount generates an output digital control quantity by parity. The output digital control quantity is converted into a simulate control signal by an output signal conditioning circuit to control an executing mechanism.    USE - Aerobic fermentation device control method for organic wastes fermentation field.    ADVANTAGE - Achieves a flexible and precise control method by using a multivariable FL control to determine required environmental factors and the best aerobic fermentation conditions.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of an aerobic fermentation device control method. (Drawing includes non-English language text).
NOVELTY - Lesinurad intermediates (A) are new.    USE - (A) are useful in preparing Lesinurad drug for treating gout disease.    ADVANTAGE - (A): are more economical, efficient and safer in producing lesinurad; and are environment-friendly. The production of lesinurad using the intermediates: has simple operation, simple product separation and purification steps, and high product yield; utilizes cheap and easily available raw materials, and avoids use of harmful heavy metals and solvents; and is suitable for large-scale production.    DETAILED DESCRIPTION - Lesinurad intermediates (A) of formula (I) and (II) are new. INDEPENDENT CLAIMS are also included for    (1) preparation of lesinurad intermediates of formula (III), comprising carrying out bromination of (I); and    (2) preparation of lesinurad, comprising a step of preparing (III).    R = H, COCH3 or CH2R1;    R1 = 1-6C alkyl (optionally substituted), ester group, cyano, CH2OH or phenyl substituted with halo; and    R2 = cyclopropyl, halo or triflate.
NOVELTY - A composition of carbon-based organic solution called LR-1 solution to curb the growth of bacteria, particularly Leuconostoc that causes an inversion in the sugar cane waste and bacteria that cause the odor, the composition of the solution consists of: coconut shell charcoal 5% (w/w), alcohol 2.5% (w/w), and liquid smoke 20% (w/w), and water 72.5% (w/w).    USE - The composition of carbon-based organic solution called LR-1 solution is useful for curbing the growth of bacteria, particularly Leconostoc that causes an inversion in the sugar cane waste (claimed).    ADVANTAGE - The composition is environment friendly, enables the increase of sugar production, and is able to withstand the growth of harmful bacteria.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for using the composition in white sugar crystallization process, which involves: LR-1 is applied at the first milking sap (NPP) at a dose of 15-30 ppm with dilution using water with a ratio of 1:50, AF-1 is applied in the raw juice at a dose of 15-30 ppm and dilution using water in the ratio 1:50, HC is applied to sugarcane in emplacement by spraying evenly with dilution using water with a ratio of 1:150, and CONS is applied in viscous sap 10-15 ppm and pan cuisine with a dose of 15-20 ppm.
NOVELTY - Separating and purifying adenine and 6-isoinosine from Trichosanthes kirilowii maxim peel comprises (i) preparing Trichosanthes kirilowii maxim peel crude extract; (ii) loading the crude extract on reverse-phase C18 column, eluting using water, then performing gradient elution methanol-water as mobile phase, and concentrating to obtain sample I; and (iii) separating and purifying the sample I using semi-preparative high performance liquid chromatography, collecting fractions and vacuum concentrating to obtain monomeric compound.    USE - The method is useful for separating and purifying adenine and 6-isoinosine from Trichosanthes kirilowii maxim peel (claimed).    ADVANTAGE - The method produces product with high purity, is environmentally friendly, and is economical.    DETAILED DESCRIPTION - Separating and purifying adenine and 6-isoinosine from Trichosanthes kirilowii maxim peel comprises (i) crushing Trichosanthes kirilowii maxim peel, ultrasonic extracting using 1% sulfuric acid solution, filtering, vacuum concentrating the extracting solution to 1/10 of the original volume, adjusting pH to 9-10 using concentrated sodium hydroxide solution, extracting using water saturated n-butanol to obtain n-butanol extraction solution and vacuum concentrating to obtain crude extract; (ii) loading the crude extract on reverse-phase C18 column, eluting using water, then performing gradient elution using 10%, 30%, 50%, 70% and 100% methanol-water as mobile phase, collecting fractions at 10% methanol elution and concentrating to obtain sample I; and (iii) separating and purifying the sample I using semi-preparative high performance liquid chromatography, where the chromatographic column is C18 SMB 100 column, the mobile phase is methanol-water (15:85, vol./vol.), and the detection wavelength is 254nm, collecting target component fractions and vacuum concentrating to obtain monomeric compound.
NOVELTY - One outside a water tank heating hydrogen removing device, include one cover device of hydrogen collector in the electrolytic electrode group and guide tube of the hydrogen collector up, the guide tube one end extend air outlet seal tank cover of water tank; the hydrogen collector is one shell, middle part forming cavity, an electrolytic electrode group is set in the cavity in the upper chamber lower shell wall forming a plurality of water inlet hole, the top end of matching hole chamber top end of cavity set with electrolytic groove connect through further forming of the tube with air of an air outlet hole, an air chamber between the upper part and the top forming hydrogen. Electrolysing and sterilizing time, water is still of the produce of hydrogen flow upwards automatically, through hydrogen collector and through guide tube only can flow, hydrogen would run out of it in the atmosphere, eliminating the small closed space aggregation to produce hydrogen, the danger of explosion, at the same time, the discharge of hydrogen is more complete, after sterilizing, water pool and a circulation, making disinfectant water tank in uniformity.
NOVELTY - This utility new type claims a one for sewage purification and continuous power generation synchronization of device, down flow tank and the uplink flow tank through marsh internal wall is divided into two sections, down flow tank and the bottom of flow tank through lower uplink, uplink flow tank connected, sewage water inlet tube and the sewage distributing pipe connecting between the anode current collector one end embedded plant root, collecting the uplink flow tank conductive filler layer surface through the uplink flow tank, uplink flow tank seal cover is located at water collector upper part, a cathode collector one end embedded uplink flow tank in conductive filler layer, and the other end passes through the uplink flow tank seal cover, anode current collector passes down-flow tank conductive filler layer and the lead, the cathode collector through one uplink flow tank end seal cover of the lead is connected with load is located between the anode collector and the cathode collector, two end a connecting lead. Realizing of sewage purification, power generating microorganism through the solar energy into electric energy to rear; one to form a module of generating electricity with renewable resources.
NOVELTY - This utility new type relates to one the lake at a light source pollution treatment system of sewage treatment efficiency include battery lamp bracket and lamp, a lamp is set on the lamp frame upper, battery through lead connect with the lamp. Under said lamp bracket is provided with a bracket. Said lamp frame is provided with section of telescopic structure, and the upper telescopic structure is provided with a locking device. Time during the day with sunlight, photosynthetic bacteria can use solar light a photosynthesis for sewage treatment process, to night or cloudy day, use multi-group of lake pollution control night light source system for sewage water treatment process, the illumination system of photosynthetic bacteria light photosynthesis process sewage treatment process continuously process, improves the sewage processing efficiency.
NOVELTY - This utility new type claims a new-type high compression, one self-sucking full nutrition fertilizer brick, straw layer, material layer up the animal waste raw material layer, there is provided an organic matter-decomposing inoculant layer up the straw layer, material layer, agent layer on the upper layer of organic matter-decomposing inoculant. Using self-sucking high concentration fertilizer brick production, it can realize saving water and fertilizer, improve the utilization ratio of fertilizer utilization rate and agricultural organic waste resource utilization rate. Self-sucking high concentration compost is one easily give play to microorganism resource base of population, nutrient source and promoting biological metabolism library of soil microorganism, it can adjust metabolic function and structure of soil microorganism, improve the soil mass, for the growth and development of crops has promoting effect, and has a certain preventing effect. Using self-sucking high concentration fertilizer brick into flower, vegetable planting basin bottom, it can realize planting water-absorbing function, and the fertilizer, valid .
NOVELTY - This new type utility claims one a slow/controlled release fertilizer using alternative photo-curing coating roller, include cylinder body, a material collecting system, bag film material spraying system, a light irradiation system. Wherein, the said material collecting system is two end opened, the bottom open unloading of lengthways set with V-shaped aggregate bin and a fixing frame fixed on the upper part of said bag film material spraying system in the roller main body include spray gun and matched conveying tube, a light irradiation system is ultraviolet radiation device, include the one-shaped ultraviolet lamp and two end wall of V-shaped belt; a spray gun and ultraviolet radiation device are set on one side below the unloading groove, horizontal face of falling off of unloading material, a spray gun and ultraviolet radiation device are alternately arranged, repeating 3 to 8 times. This utility new type one of a slow/controlled release fertilizer using alternative light-cured coating has low energy consumption, high efficiency, large yield, low cost, simple technique and so on.
NOVELTY - This utility new type one a biomass pyrolysis device, belonging to the biomass energy utilization technology field, wherein include pyrolysis chamber, a combustion chamber, a discharging pipe, a cyclone dust collector, a heat exchanger, a circulating pump, a condenser, a settling chamber, a burner, a burner is mounted at the bottom of burning room, is mounted at the bottom of the pyrolysis room, a combustion chamber set on the outside of the pyrolysis room, a pyrolysis chamber through the outlet tube is connecting with the cyclone, a condenser settling room is connected with the burner, a circulating oil pump inlet by the pipeline connecting to the side wall of the condenser, a circulating oil pump through the heat exchanger and the condenser upper part connect. This utility new type can make use of biomass raw material pyrolysis fuel oil and obtain biomass carbon, and it does not need additional system to provide hot source, it has stable operation, no second pollution and low cost and so on, compared with the existing pyrolysis technology, it is easy to be popularized and applied.
NOVELTY - This utility new type relates to a one by using biomass tar catalytic cracking for preparing fuel oil of device, belonging to the new energy field, include through pipeline orderly connected of the raw material oil storage tank, pressure filter, dehydration groove, a tar pump, a heating furnace, a reaction tower, a fractionating tower, a condenser, a gas-liquid separator and oil storage tank, pressure filter, reaction tower and fractionating tower connecting with a tar residue storage tank, each tank and tar fractionating tower is a connecting with fuel oil storage tank, the utility model is new type gasification process to produce of tar as raw material, using current catalytic cracking technology a deoxidizing and refining, to obtain high quality of fuel oil, it not only solves the problem that the biomass gasification product for the environment of negative influence also brings good economic benefit of, promoting our country biomass gasification technology development and use.
NOVELTY - This utility new type claims a one integral straw gasification furnace, gasification device include, a furnace bottom central air supply device, a fan, and, wherein gasification of device comprising lower furnace body, the upper part thereof set with annular gas distribution channel of the outer upper part set with a smoke outlet and a smoke outlet switch control, a middle set with air blower, one end with the central air supply device bottom furnace connecting, one end with the distribution channel connecting, and set with an air amount regulating valve and air distribution switch up in the air, a furnace disk and the furnace cover are integrated is directly set on the upper furnace body, pipeline is set with the switch, using the asbestos plug. This utility new type rational design, does not need special is provided with one gas, low cost, and small occupied space, convenient use, it is convenient to the second gas pipeline is not is not easy to be blocked, not using cleaning tar and water vapour, use time is long, can be of gasification status in proportion, gasification device gasification regulating amount and air amount of stable, the combustion effect is very good.
NOVELTY - This utility new type relates to one a medical treatment garbage gasification and combustion device, feeding can be set with a feeding port sealing of seal cover, and is condensed water recycling box seal cover bottom, the top surface of a gasification furnace body is the high two end lower arc-shaped, and set with condensed water recycling groove under the end of arc top surface, the condensed water recycling groove by the condensed water pipe and condensed water leading-out tube seal groove is set on the outer wall of the furnace body of the gasification connecting, said exhaust port through the exhaust tube and the gas recycling processing connecting mechanism, a burning mechanism burning room include the combustion of gasification disk in the room to the gasification disk into the air of the air inlet pipeline, and set with upper ignition hole on the outer wall of the combustion room. This utility new type medical waste can be fully gasified form gas seal in the gasification furnace, through guide exhaust in the fuel gas discharging tube, then using special low hot value of burner for fuel gas complete combustion, a rear combustion of hot can produce is a boiler or hot-blast stove.
NOVELTY - This new type utility claims one gasification furnace multilayer feeding box and a door device is equipped with lower feeding plate at the inlet of the furnace body top end centre of the lower door of the lower feeding plate upper end surface configuration and the lower feeding plate is point contact, at the end of each fan in the lower door connecting with lower push-pull rod, lower connecting box at the feeding inlet of the top panel. The feeding port at the top end of the feeding box is equipped with a lower upper feeding plate, the upper door of upper feeding plate upper end surface arranged between the upper feeding plate is point contact, each upper end of door leaf connecting with push pull rod, connecting with a feeding box at the upper port of the lower feed box top panel, a feeding inlet of upper cover is placed on the top of the feeding box upper panel. A gasification furnace of multi-layer feeding box and door device can ensure the biomass gasification furnace without furnace lower continuous to the gasification furnace adding irregular material, seal effect, good safety performance, and it can be popularized to domestic sludge gasification treatment or cold rolling waste mineral oil gasification treatment of gasification furnace using up.
NOVELTY - One a biomass hot gas alkali metal removing device, relating to a one purifying device, especially a one hot in the biomass fuel gas of alkali metal removing of device. This utility new type of biomass hot gas alkali metal removing device, wherein the device include hot gas inlet, heat exchanger, air interlayer, the hot gas outlet, a cold air inlet, a hot air outlet, a dust conveying tube, hot gas inlet is set at the upper part and heat exchanger into heat exchanger, an air interlayer is covered on the heat exchanger, the hot gas outlet is set at the top of the heat exchanger, the cold air inlet is set at the top of the air interlayer hot air outlet is set at the bottom of heat exchanger is provided with an air interlayer dust transporting tube. This utility new type of biomass hot gas alkali metal removing device, the structure is simple, the design is scientific, convenient use, separating out according to rule of alkali metal in biomass, through cooling method for hot gas of reasonable, non-contact cooling of the alkali metal steam status.
NOVELTY - A methane-rich gas one rectifying dehydrogenation nitrogen and production of liquefied natural gas device, the device include the condenser and liquid separating tank, top of the cold box, four throttle device and a rectifying tower, the rectifying tower include bottom of tower. Use process of the device include liquefied gas with low temperature and single-tower rectifying and separating two part, part of the liquefied gas with low temperature in the cold box, rectifying and separating part using single-tower rectifying process to remove hydrogen, nitrogen and may contain of carbon monoxide, obtain in LNG product of hydrogen content is not more than 500 ppm, nitrogen content is not more than 2%, carbon monoxide is not more than 2%. This utility new type provide the a one the methane gas liquefying liquefied natural gas production of hydrogen, nitrogen, and removing device, the flow of carbon monoxide is simple and device investment cost is low.
NOVELTY - This utility new type claims a one agriculture and forestry waste drying forming composite production device to form include two parallel set the waste carbon rod is set of device (15) and the carbon rod device (15) is set with flue (12), a flue (12) through the centrifugal fan connecting with a de-dusting device (13), dust device (13) connecting with desulphurization device (14). This utility new type can be large amount of dust and smoke scale production, and the production process in produce of centralized recycling and through flue gas purifying and processing rear and emptying, reducing the atmospheric pollution.
NOVELTY - This utility new type claims a one drying papermaking sludge fuel of device preparation, include, mixing device, a spiral conveying machine, a rotary dryer, a cyclone dust collector, a hoisting machine, a feeding pipeline, a return pipeline, a storage silo, one end a rotary dryer of a boiler dust remover connected and gas source, feeding machine, mixing device, a spiral conveying machine, a rotary drying machine order, the hoisting machine, a feeding pipeline, a storage silo connected sequence, a return pipeline connected with storage and mixing device, a cyclone dust collector connected rotary dryer. The device can realize good of paper making sludge drying effect and saves the coal, better protection of the mineral resources and environment better economic and social of normal fluctuation is large, so the technology control is difficult, the effect is large deviation, the rear processing of waste water the second time pollution.
NOVELTY - One a biodiesel deodorizing tower, light component outlet tube is set on the top part of the tower body, the top low temperature detector, the top of the negative pressure meter, middle part is bald ring filler tower body of lower filling plate, set in bald ring filler of filler in plate, set with corrugated filler of upper padding plate between the bald ring filler and up in bald ring filler is coarse methyl ester distilling tube and upper gas-liquid separator, a filler plate and lower in bald ring filler is two circulating distillation set fire tube steam boiling tube and lower gas-liquid distributor, a tower body, the tower body of the left side upper part upper collector temperature monitor is set up a product outlet tube, lower collector temperature monitor, low product outlet tube, the left side of the lower part temperature detector outside the tower body and liquid level meter, a lower tower body end is set two circulating distilling tube. The tower body upper part is set one level condenser and second level condenser, a first-stage condenser and the second level condenser second level condenser set with upper collector, upper filler plate is set above the top plate, upper top plate .
NOVELTY - This utility new type relates to a production biological diesel oil of one clapboard type reaction kettle, which include mixed liquor inlet tube, a reaction kettle, a heating device, a sampling port tube, outlet tube, liquid outlet tube, a liquid catalyst and reaction by-product outlet tube, temperature meter, pressure meter and gas-liquid circulating device, a reaction kettle set with multi-filling layer, the bottom of said stuffing layer is support plate, the top part of said filling layer is a pressing plate, of a filler in the filler layer is made of stainless steel pompon and a filler layer set with reaction liquid re-distributor. This utility new type can obviously improve the conversion rate, the reaction time of the mixed reaction liquid is greatly shortened, production efficiency is high, good quality and high yield and the economic benefit is high.
NOVELTY - This utility new type relates to one a biological diesel oil production device, include mixed liquor inlet tube, a reaction kettle, a heating device, a sampling port tube, outlet tube, liquid outlet tube, a liquid catalyst and reaction by-product outlet tube, temperature meter, pressure meter, it also include one gas-liquid circulating device, a gas-liquid circulating device is a peristaltic pump, the mixed liquid circulating conveying tube, spraying device, a spraying device of hanger plate, a liquid inlet tube, an annular tube, a spray head. This utility new type using gas-liquid circulating device, the reaction is not completely mixed liquid of reaction device is sent to the top part of the spray device from up downwards fog spraying, obviously improves the conversion rate and reaction time of mixing reaction liquid is greatly shortened, production efficiency is high.
NOVELTY - A one bio-diesel esterification reactor, a stirrer is set on the top end of the reaction kettle, the raw material adding valve, a catalyst inlet valve, a reaction kettle of right side wall upper part set up temperature monitor, right side wall middle part set sampling valve, right side wall temperature monitor, a reaction kettle steam coil pipe is set in the reaction kettle of the left side wall of the upper part is liquid level meter, left side wall in middle part is temperature monitor, the lower end side wall of the reaction kettle is a discharging valve, the lower end is discharge valve. The reaction kettle is cylinder, the lower end of the reaction kettle is the reaction kettle low end is set with cone inner wall of methanol tube, upper tube is processed with methanol, the top of reaction kettle is equipped with foam destroyer of methanol outlet valve. This utility new type has reasonable design, esterification reaction efficiency is high, the utilization rate of the raw material is high, it can be used for preparation;
NOVELTY - This utility new type claims a intermittent one ester exchange preparation biological diesel oil device, include the reaction tank, the condenser, the methanol tank, methanol rectifying tower, a pump, a depositing tank, a filter, a reaction tank through the condenser and the connecting methanol tank, methanol tank through valve I and the methanol rectifying tower connecting, in reaction tank is provided with a centre tube, methanol rectifying tower through of center tube in pump and reaction tank connected, reaction tank through sedimentation tank and the filter connecting the upper reaction tank is provided with a feeding port, the device through adding methanol to realize mixing of the material in the reaction tank, device is simple, environment-friendly and convenient use and saves the cost.
NOVELTY - This utility new type provide the used for making hydrogen by water-electrolysis of hydrogen-oxygen washer, set on the separator and the gas cooler, in particular, washer main body is one of the washing cabin of electrolysis raw material containing water, washing cabin is connected with an air inlet pipeline on the upper side wall, an air inlet pipeline one end of separator is connected with the exhaust port, the air inlet pipeline and the other end extending to the electrolysis raw material in washing cabin water level following washing cabin top part set with an air outlet, and the washing cabin side wall set with separator connected with the overflow port. This utility new type of hydrogen-oxygen washer, valid reduces the amount of alkali-containing product gas, and recycling alkali repeatedly used greatly reduces the water electrolysis hydrogen production device of base loss and operation cost, at the same time reduces the temperature of gas, reduces the burden of the subsequent gas cooler so that the temperature and humidity of the final product gas futher.
NOVELTY - This utility new type one a marsh gas power generation system, belonging to the field of organic waste processing technical field, wherein the fermentation tank, second level fermentation tank rear part are orderly mounted biological desulfurizing tower, desulfurizing tower, a booster fan, an air storage cabinet and internal combustion generating unit, an internal combustion generator rear part are orderly arranged drying machine, cyclone dust collector, bag-type dust remover, a draught fan and a chimney, using this utility new type design of marsh gas power generation system, it not only can the excrement, straws, sewage and organic waste into rear electric energy of high quality, at the same time, the fermentation residue is used for organic fertilizer production, it has high efficiency, stable operation, no pollution and so on.
NOVELTY - The method comprises mixing additives with food waste water to obtain a mixed solution, and subjecting the mixed solution to anaerobic fermentation for producing methane. The additive comprises sodium ions, potassium ions, calcium ions, magnesium ions, manganese ions and zinc ions. The weight ratio of the additives and solids content of the food waste water is 0.0075-0.45:1. The method further comprises mixing carbon source and nitrogen source of 25-35:1 in the solution.    USE - The method is useful for producing biogas from food waste water (claimed).    ADVANTAGE - The method is capable of increasing the rate of methane production.    DETAILED DESCRIPTION - The method comprises mixing additives with food waste water to obtain a mixed solution, and subjecting the mixed solution to anaerobic fermentation for producing methane. The additive comprises sodium ions, potassium ions, calcium ions, magnesium ions, manganese ions and zinc ions. The weight ratio of the additives and solids content of the food waste water is 0.0075-0.45:1. The method further comprises mixing carbon source and nitrogen source of 25-35:1 in the solution. The concentration of the carbon in the mixed solution is 30-40 g/l. The fermentation step is carried out using an inoculum of 30-200% at 30-65 degrees C for 4-50 days. The pH value of anaerobic fermentation liquid is 5-10.
NOVELTY - A vertical continuous solid-state fermentation device comprises tower body (7) with solid-liquid mixing unit, fermentation unit and drying unit. The fermentation unit has plate (8), circulating fan (15a), atomizing tube (18), blower tube (19), and temperature and humidity sensor (20).    USE - Vertical continuous solid-state fermentation device.    ADVANTAGE - The device saves energy, ensures good mixing of materials, and has simple structure, easy operation, good solid-state fermentation efficiency, and good economic, social and ecological benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of vertical continuous solid-state fermentation device.    Tower body (7)    Plate (8)    Circulating fan (15a)    Atomizing tube (18)    Blower tube (19)    Temperature and humidity sensor (20)
NOVELTY - Liquefaction of organic fertilizer comprises adding organic fertilizer into liquefied tank, injecting water by enabling liquefaction tank bottom, agitating while ventilating, filtering, and applying to farmland through drip irrigation system.    USE - Method for liquefaction of organic fertilizer (claimed).    ADVANTAGE - The method can greatly saves labor force, cultures protozoa and fungi with special functions, avoids deposition of debris at bottom of cell body, and has more thorough fermentation.
NOVELTY - Auxiliary turning feeder comprises left and right connecting piece (1), which includes a connecting plate. The connecting plate is equipped with arc-shaped mounting plate on the upper part and a mounting plate at the lower part. A turning plate (2) is set between the left and right connecting piece and the mounting plate. The turning plate is L-shaped, whose one side on the upper part is provided with a frangible bar (3).    USE - The auxiliary turning feeder is useful for polishing machine (claimed).    ADVANTAGE - The auxiliary turning feeder improves the working area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the auxiliary turning feeder.    Left and right connecting piece (1)    Turning plate (2)    Frangible bar (3)
NOVELTY - Production of low sulfur briquette comprises mixing 30-50 pts. wt. coal powder, 10-20 pts. wt. herbivorous animal manure, 1-5 pts. wt. desulfurization agent, and 5-10 pts. wt. briquette binder, adding water, and extrusion molding. The briquette binder comprises 36-60 pts. wt. humic acid, 2-8 pts. wt. sodium hydroxide, 36-60 pts. wt. bauxite, 5-30 pts. wt. modified wood ash, and 25-30 pts. wt. water.    USE - Method for producing low sulfur briquette (claimed).    ADVANTAGE - The briquette has low cost and is environment-friendly.    DETAILED DESCRIPTION - Production of low sulfur briquette comprises mixing 30-50 pts. wt. coal powder, 10-20 pts. wt. herbivorous animal manure, 1-5 pts. wt. desulfurization agent, and 5-10 pts. wt. briquette binder, adding water, and extrusion molding. The briquette binder comprises 36-60 pts. wt. humic acid, 2-8 pts. wt. sodium hydroxide, 36-60 pts. wt. bauxite, 5-30 pts. wt. modified wood ash, and 25-30 pts. wt. water. The modified wood ash is prepared by soaking 100 pts. wt. ash tree in 10-15% hydrogen peroxide for 3-4 hours, rinsing with deionized water, soaking in 10-12% sodium hydroxide solution for 3-4 hours, washing with deionized water until neutral, and drying; and adding 2-3 wt.% sodium lauryl sulfate, 10-20 wt.% nano carbon, 2- 3 wt.% polyisobutene, and 3-5 wt.% alum powder, high speed stirring at 1200-1500 revolutions/minute, drying and crushing. An INDEPENDENT CLAIM is included for the preparation of briquette binder comprising crushing humic acid and sodium hydroxide to more than 60 meshes powder at weight ratio of 36-60:2-8 and uniformly stirring; cooling, grinding with bauxite into 100 meshes powder, mixing powder with alum powder at weight ratio of 38-68:36-60; and adding modified wood ash and water, stirring, reacting at 90-100 degrees C for 1-2 hours, and discharging.
NOVELTY - Organic game soil comprises fully fermented processed straw, reed, coconut peat, biogas residue alcohol, vermicompost or humus, river pond mud, rice husk ash or plant ash, and turf or peat; prepared by straw, reed, coconut husk, and biogas residue alcohol at a volume ratio of 2:2:2:2.    USE - Organic game soil used for storing killifish eggs.    ADVANTAGE - The soil is full of nutrients, and has light texture and moderate moisture.    DETAILED DESCRIPTION - Organic game soil comprises fully fermented processed straw, reed, coconut peat, biogas residue alcohol, vermicompost or humus, river pond mud, rice husk ash or plant ash, and turf or peat; prepared by straw, reed, coconut husk, and biogas residue alcohol at a volume ratio of 2:2:2:2. The game soil comprises 30-50 pts. wt. fermented mixed organic material, 10-20 pts. wt. vermicompost or humus, 10-20 pts. wt. river pond mud, 5-10 pts. wt. rice husk ash plant ash, and 5-10 pts. wt. turf or peat. The games soil has water content of less than or equal to 30%, total porosity of 65-85%, organic matter content of greater than or equal to 20%, total nutrient content of 1-2%, bulk density of 0.2-0.8 g/cm3, gas-water ratio of 1:1.5-3, electrical conductivity (EC) value of 1-2.5 mS/cm, pH value of 5.8-7.5, and grain size of 0.1-3 mm. Fermentation is carried out by using high-temperature fast rotting agent for straw, reed powder, coconut, alcohol residue of organic matter and decomposing for 120-180 days. The high-temperature fast rotting agent comprises actinomycetes, saccharomycetes, lactic acid bacteria, and Bacillus. The effective active bacterial content is 0.5-1 hundred million units/g, where actinomycetes accounts for 40-60%. The method further comprises adding 0.15-0.2 kg preservative per cubic meter material, drying and crushing to water content of less than or equal to 30% and grain diameter of less than or equal to 3 mm.
NOVELTY - This utility new type belongs to living garbage processing field, especially domestic garbage of solar energy and low-temperature dry distillation system. Domestic garbage solar energy low-temperature dry distillation system, include energy system (001), a monitoring system (002) and operating system (003), said energy system (001), include the lighting system (01), capable of adjusting system (02) and transmission system (03), the operation system (003), include, cleaning workshop (31), sorting workshop (43), a pressing block workshop (706), drying room (44) and solar energy low-temperature dry distillation room (97), the cleaning workshop (31), using water washing, the household garbage is divided into organic and inorganic component of the pressure room (706), the random loose of the organic household garbage, compressed volume and water, pressing into block, convenient dry distillation, a household garbage of solar energy low-temperature dry distillation system, using clean energy solar energy to realize the solid waste reduction, harmless and resource processing dry distillation, waste into valuable, the nation, the innovation.
NOVELTY - Purifying and recycling secondary gas that generated in steam drive-oil extraction method involves desulphurization of the secondary gas with desulfurizing agent in the desulfurizing tower; removing heavy hydrocarbon impurities in absorption tower having carbon adsorbent; the passing the secondary gas through absorption tower having silicon glue as adsorbent to remove carbon dioxide (CO2); removing methane (CH4) product that used as oil field fuel; and converting carbon dioxide into industrial liquid CO2 product.    USE - For purifying and recycling secondary gas that generated in steam drive-oil extraction method (claimed).    ADVANTAGE - The method recycles natural gas, reduces energy waste, purifies gas and removes organic sulfur, reduces the harmful gas and environmental pollution, reduces greenhouse gas discharge, and is environment-friendly.    DETAILED DESCRIPTION - Purifying and recycling secondary gas that generated in steam drive-oil extraction method involves desulphurization: passing the secondary gas through gas-liquid separator for removing liquid, and then air cooling, desulfurizing with desulfurizing agent in the desulfurizing tower and entering into a reaction tower, removing hydrogen sulfide gas; then pressurizing the secondary gas and passing through the compressor to buffer tank, then entering into absorption tower having carbon adsorbent to remove heavy hydrocarbon impurities in the secondary gas; the passing the secondary gas through absorption tower having silicon glue as adsorbent to remove carbon dioxide (CO2); and after separation of CO2, removing methane (CH4) product that used as oil field fuel; and cooling and converting the liquid CO2, drying and dehydrating, rectifying and refining to obtain industrial liquid CO2 product.
NOVELTY - A biomass liquefaction catalyst comprises carrier; and active component. The weight ratio of carrier and active component is 1:(0.01-0.03). The active component is transition metal, e.g. palladium, platinum, ruthenium, nickel or rhodium.    USE - Biomass liquefaction catalyst used for preparing cracked liquefied bio-oil.    ADVANTAGE - The catalyst solves the problem of high utilization of fast pyrolytic carbon product and stronger adaptability of thermal cracking reaction environment, and controls quick biomass pyrolysis liquefaction process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a biomass liquefaction catalyst.
NOVELTY - High-temperature methanation catalyst comprises nickel as an active component, cerium oxide as an auxiliary agent, and a carrier comprising mixture of aluminum oxide, silicon oxide and titanium oxide.    USE - Used as a high-temperature methanation catalyst.    ADVANTAGE - The catalyst has high temperature performance requirements, high intensity, good activity, good thermal stability, and anti-carbon resistance; can meet the coal synthesis natural gas for heat-resistance; reduces the cost of coal synthesis natural gas; solves the problem of insufficient supply of natural gas; and promotes the development of coal gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing catalyst, comprises (i) uniformly mixing 30-40 pts. wt. aluminum oxide, 25-35 pts. wt. silicon oxide, 25-35 pts. wt. titanium oxide and 4 pts. wt. graphite, to obtain a homogeneous mixture containing shaped particles; (ii) molding the shaped particles at 0.8-1 MPa, steaming at 120-160 degrees C environment, and reacting for 4-8 hours to obtain blank; (iii) placing the blank in a muffle furnace, calcining at 500-700 degrees C for 4-6 h ours to obtain the catalyst carrier; (iv) adding raw material liquid into the catalyst carrier, heating the raw material liquid at 70-80 degrees C, maintaining temperature for 0.5-1 hour, heating the catalyst carrier at constant temperature, and taking out the catalyst carrier, heating the catalyst carrier at 110-130 degrees C by placing in oven, to 110, and maintaining at constant temperature for 2-4 hours, to obtain derived products, adding 1 l water into raw material liquid, namely 1170-2340 g nickel(II) nitrate hexahydrate and 150-760 g cerium(III) nitrate hexahydrate.
NOVELTY - Preparing mesoporous carbon-based solid acid catalyst, comprises completely dissolving a carbon source in a solvent, then introducing the carbon source solution into mesoporous silica mold channel, carrying out two-step pre-carbonization to obtain pre-carbonized solid powder, carbonizing to obtain carbon-mesoporous silica composite mold; dissolving the carbon-mesoporous silica composite mold in high alkali solution or acid solution, and then passing the acidic solution through mesoporous carbon and placing into a reaction vessel for carrying out acid functionalization.    USE - The mesoporous carbon-based solid acid catalyst is useful for deacidification of pre-treated biodiesel feedstock (claimed).    ADVANTAGE - The catalyst has large specific surface area and pore volume, and higher acid density.    DETAILED DESCRIPTION - Preparing mesoporous carbon-based solid acid catalyst, comprises completely dissolving a carbon source in a solvent, then introducing the carbon source solution into mesoporous silica mold channel, carrying out two-step pre-carbonization under the protection of inert gas to obtain pre-carbonized solid powder, carbonizing at 500-1100 degrees C at the heating rate of 0.5-20 degrees C/minute, to obtain carbon-mesoporous silica composite mold; dissolving the carbon-mesoporous silica composite mold in high concentration alkali solution or acid solution to remove mesoporous silica mold, and then passing the acidic solution through mesoporous carbon and placing into a reaction vessel for carrying out acid functionalization, filtering, washing, and vacuum drying. An INDEPENDENT CLAIM is also included for use method of the mesoporous carbon-based solid acid catalyst for deacidification of pre-treated biodiesel feedstock, comprising mixing high acid value oil with methanol in the molar ratio of 5:1-20:1, and carrying out esterification reaction at 80 degrees C.
NOVELTY - This utility new type claims a one organic fertilizer fermentation tank, include a tank body, inner wall of the tank body set with spiral conveying blade, external circumferential direction set with the power connecting mechanism of transmission mechanism, right end set with the seal connecting with the end cover of the bottom left end set with roller. The utility model is new in type of organic fertilizer fermentation tank, include a tank body, inner wall of the tank body set with spiral conveying blade, external circumferential direction set with the power connecting mechanism of the transmission mechanism, the fermentation time tank still, the needed time stirring, through power mechanism drives the tank body to rotate, stirring hot radiation effect, does not need to use the device, and the cost is low.
NOVELTY - Opening hydrogenation gas separating butane and propane of preparation device belonging to the preparation device of butane and propane, methanol hydrogen production device, the raw material hydrogenation refining device and liquid-gas separating device, the technical solution of the utility model is a new type of input pipeline of device of hydrogen production by methanol and methanol raw material tank and a steam water tank connect, output pipeline connected with the raw material hydrogenation refining device, raw material hydrogenation refining device set with three input pipeline port, a connecting aromatization rear carbon four raw material tank and four raw material tank, the raw material hydro-refining device output pipeline connecting the liquid gas separating device port two of input pipeline, liquid-gas separating device set with four of the output pipeline. This utility new type through the technical improvement to achieve a beneficial effects: the production cost is low, the production technique is simple, the device has relatively simple structure, and by-product of butane and propane for n-butane and iso-butane process.
NOVELTY - This utility new type claims a one biomass gasification pyrolysis reactor, pyrolysis reactor include main body and used for the pyrolysis reactor main body in the conveying of biomass fuel feeding system, feeding system include a spiral feeding device and the spiral feeding device and the upper part thereof is connected with the storage hopper, of said pyrolysis reactor main body include outer furnace body in the furnace body, and the inner space of said upper down include cracking room in the furnace body, a heat storage room and residue combustion chamber, a biomass material by the feeding system low conveying to cracking room rear, continuously heating the residual combustion chamber, a cracking room in the pyrolysis and pyrolysis reaction, produce hydrogen with high amount of gas. This utility new type the normal pressure low condition of biomass pyrolysis and there is low pressure condition of biomass cracking reaction is combined form can be continuous, stable, strong raw material adaptability of biomass pyrolysis and gasification reaction system.
NOVELTY - The device comprises a self-heating laminate micro reactor, a shell, a cover plate connected with a seal box body, a n-layer reaction carrier provided in the body, where n is 3-6, and two axial gas inlets. The shell is equipped in a bottom surface of the axial gas outlets. An upper portion and a lower portion of the n-layer reaction carrier are connected with a concave plane. The n-layer reaction carrier has a peripheral ring. The concave plane is radially distributed with a micro-dummy club matrix, and is provided with a circular lug boss.    USE - The device is useful for producing hydrogen fuel (claimed).    ADVANTAGE - The device produces the hydrogen fuel with improved production efficiency and reduced voltage drop.    DETAILED DESCRIPTION - The device comprises a self-heating laminate micro reactor, a shell, a cover plate connected with a seal box body, an n-layer reaction carrier provided in the body, where n is 3-6, and two axial gas inlets. The shell is equipped in a bottom surface of the axial gas outlets. An upper portion and a lower portion of the n-layer reaction carrier are connected with a concave plane. The n-layer reaction carrier has a peripheral ring. The concave plane is radially distributed with a micro-dummy club matrix, and is provided with a circular lug boss. The circular lug boss is set with an upper end of the axial gas inlets. The reaction carrier has a circular ring symmetrically arranged with the axial gas outlets, and includes two gas outlets. The gas outlet is set with the concave plane. A notch is connected with an upper part of the concave plane. The circular lug boss has a same height as the concave plane. An O-shaped silicon glue seal is arranged between the circular lug boss and the reaction carrier. The reaction carrier is set between the peripheral ring and a flexible graphite pad.
NOVELTY - Enzyme preparation comprises enzyme, carrier, organic acid, polyethylene imine, inorganic salt, yeast, and water in which enzyme comprises protease, cellulase, oxidoreductase, pectinase, dehydrogenase, and lysozyme.    USE - An enzyme preparation for treating industrial sewage (claimed).    ADVANTAGE - Enzyme preparation has no bacterial contamination, strong sewage treatment capacity, simple use, and high chemical oxygen demand (COD) removal rate and ammonia removal rate, improves sludge settling property, reduces amount of sludge discharge, and improves self-cleaning capacity of water body.
NOVELTY - Comprehensive depth processing of waste water, comprises adding waste water into a regulating tank for aeration process, pumping waste water into a biological treatment system for hydrolysis acidification-anaerobic-aerobic reaction, performing biochemical process to decompose, allowing waste water into a anaerobic hydrolysis acidification tank, deeply removing chemical oxygen demand (COD), allowing oxidation ditch water into the waste water, then discharging into biological carbon filter tank, filtering to remove biodegradation of organic matter, and absorbing ammonia nitrogen.    USE - The method is useful for comprehensive depth processing of waste water (claimed).    ADVANTAGE - The method is capable of comprehensive depth processing of waste water with reduced COD.    DETAILED DESCRIPTION - Comprehensive depth processing of waste water, comprises adding waste water into a regulating tank for aeration process, pumping waste water into a biological treatment system for hydrolysis acidification-anaerobic-aerobic reaction, performing biochemical process to decompose into easily degradable acid and alcohol, biodegradable macromolecule organic matter and waste water through a hydrolysis acidification capillary, obtaining sulfate ion, entering waste water into a anaerobic hydrolysis acidification tank having two phase composite anaerobic reactor of methane producing phase, deeply removing chemical oxygen demand (COD) using oxidation ditch, allowing oxidation ditch water into the waste water for bio-carbon reaction depth treatment, then discharging into a biological carbon filter tank, filtering biodegradation of organic matter using a biological carbon filter cell, and slowly absorbing ammonia nitrogen.
NOVELTY - Treatment of oil sludge involves adding oil-containing sludge into greenhouse drying room, drying for 6-20 days, then mixing mud cake and extracting agent in mass ratio of 30:1, stirring uniformly, rear-extracting the mixture material in solid-liquid separator, recycling the liquid, and rear-separating solid residue and mixing with fuel coal. The extracting agent is composed of 85-100 %(v/v) component (A) having boiling point of 110-135 degrees C as main agent, and component (B) having boiling point of 140-150 degrees C and component (C) having boiling point of 80-100 degrees C as additives.    USE - Treatment of oil sludge (claimed).    ADVANTAGE - The method efficiently and economically treats oil sludge in short flow process, without causing pollution to environment.
NOVELTY - Treatment of oil sludge involves processing sludge in mechanical dewatering device at 0-80 degrees C for 20-50 minutes under pressure of 20-30 MPa, such that resulting moisture content of the cake is decreased to 15-25%, squeezing sludge in wastewater treatment plant, extracting product at 10-70 degrees C for 10-30 minutes using extraction agent with cake quality extractant ratio of 30-1:1, adding product to solid-liquid separator and processing at 110-188 degrees C for 60-85 minutes under pressure of 20-100 KPa.    USE - Treatment of oil sludge (claimed).    ADVANTAGE - The method is carried out efficiently and economically with high sludge-treatment effect and extracting effect.    DETAILED DESCRIPTION - Treatment of oil sludge involves processing sludge in mechanical dewatering device at 0-80 degrees C for 20-50 minutes under pressure of 20-30 MPa, such that resulting moisture content of the cake is decreased to 15-25%, squeezing sludge in wastewater treatment plant, extracting product at 10-70 degrees C for 10-30 minutes using extraction agent with cake quality extractant ratio of 30-1:1, adding product to solid-liquid separator and processing at 110-188 degrees C for 60-85 minutes under pressure of 20-100 KPa. The solid residue obtained is used as fuel. The extracting agent comprises a main agent having boiling point of 110-135 degrees C and distillate content of 85-100% (v/v), vice agent having boiling point of 140-150 degrees C and distillate content of 0-15% (v/v), and additive having boiling point of 80-100 degrees C and distillate content of 0-5% (v/v).
NOVELTY - A bio-organic fertilizer comprises 50-80% animal manure, 20-50% garbage fertilizer, 1-2% of 002 bacterial strain, 10-15% brown sugar, and water. The garbage fertilizer is agricultural waste, leaves, shale, or municipal domestic waste. The 002 bacterial strains include yeast, photosynthetic bacteria, lactic acid bacteria, or actinomycetes.    USE - A bio-organic fertilizer used for dragon fruit (claimed).
NOVELTY - A bio-organic fertilizer comprises 30-35 pts. wt. traditional Chinese medicine waste residue, 13-16 pts. wt. sheep manure, 28-32 pts. wt. slaughter waste, 1-2 pts. wt. Aspergillus niger, 1-2 pts. wt. Trichoderma koningii, 2-3 pts. wt. Bacillus megaterium, 35-42 pts. wt. coal ash, and 100-120 pts. wt. high phosphorus hematite wastewater.    USE - A bio-organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bio-organic fertilizer, comprising crushing traditional Chinese medicine waste residue and sheep manure, adding A. niger, T. koningii, and high phosphorus hematite wastewater, and reacting for 22-25 days; grinding slaughter waste, adding high phosphorus hematite wastewater, and reacting for 26-28 days; uniformly stirring the reaction products, reacting for 6-8 days at 40-45 degrees C; and adding coal ash and high phosphorus hematite wastewater, uniformly stirring for 18-20 days, drying, and packaging.
NOVELTY - A silicone-rich microbial organic fertilizer comprises 40-60 pts. wt. livestock manure, 40-60 pts. wt. silicon-rich plant, 40-60 pts. wt. mushroom waste, 40-60 pts. wt. mineral component, 20-30 pts. wt. vitamin component, and 1-10 pts. wt. composite agent.    USE - Silicone-rich microbial organic fertilizer used for pollution-free food, green food, and organic food.    ADVANTAGE - The fertilizer can provide enough organic silicon mineral substances and vitamins, improves and sterilizes soil which prevents diseases, and conserves social and natural resources which protects environment.    DETAILED DESCRIPTION - A silicone-rich microbial organic fertilizer comprises 40-60 pts. wt. livestock manure, 40-60 pts. wt. silicon-rich plant, 40-60 pts. wt. mushroom waste, 40-60 pts. wt. mineral component, 20-30 pts. wt. vitamin component, and 1-10 pts. wt. composite agent. The mineral component comprises 40-60 pts. wt. silt, 40-60 pts. wt. gangue, 20-30 pts. wt. urea, 20-30 pts. wt. phosphate rock, 20-30 pts. wt. potassium ore, 10-20 pts. wt. silica fume, 1-3 pts. wt. selenite, 1-3 pts. wt. zinc sulfate, 1-3 pts. wt. copper, 1-3 pts. wt. sulfuric acid, 1-3 pts. wt. boric acid, 1-3 pts. wt. sodium molybdate, and 5-10 pts. wt. zeolite powder. The vitamin component comprises 1-2 pts. wt. vitamin B1, 1-2 pts. wt. vitamin B2, 1-2 pts. wt. vitamin B6, 1-2 pts. wt. vitamin B12, and 1-2 pts. wt. vitamin C. The composite agent comprises 1-2 pts. wt. photosynthetic bacteria, 1-2 pts. wt. nitrifying bacteria, 1-2 pts. wt. lactic acid bacteria, 1-2 pts. wt. yeast, 1-2 pts. wt. nitrogen-fixing bacteria, 1-2 pts. wt. actinomycetes, 1-2 pts. wt. phosphate solubilizing bacteria, 1-2 pts. wt. Bacillus subtilis, and 1-2 pts. wt. plant growth promoting bacteria. An INDEPENDENT CLAIM is included for preparation of fertilizer by mixing raw materials, crushing into 20-80 mesh particles, fermenting to 65 degrees C for 12-36 hours, granulating, packaging, and storing.
NOVELTY - Preparation of special composite fertilizer comprises taking cyanobacteria, removing excess water, adding water, adding cellulase and protease, mixing, heating to 40-50 degrees C, enzymolyzing for 2-4 hours, and inactivating enzyme; adding potassium sulfate, heating to 80-90 degrees C for 3-5 hours, cooling, and vacuum concentrating until to 1/3-1/4 of its original volume; and adding sodium humate, potassium humate, urea, ammonium bicarbonate, phosphogypsum, potassium citrate, zinc sulfate, amino acid, polyvinyl alcohol, cellulose, and calcium carbide, stirring, spray drying, and granulating.    USE - Method for preparing special composite fertilizer (claimed) used for promoting growth of Ginkgo tree.    ADVANTAGE - The fertilizer has high leaf yield and amount of active substance.    DETAILED DESCRIPTION - Preparation of special composite fertilizer comprises taking cyanobacteria, removing excess water, adding 10-12 pts. wt. water per 1 pt. wt. cyanobacteria, adding 0.05-0.1 pt. wt. cellulase and 0.05-0.1 pt. wt. protease, mixing, heating to 40-50 degrees C, enzymolyzing for 2-4 hours, and inactivating enzyme; adding 0.05-0.1 pt. wt. potassium sulfate, heating to 80-90 degrees C for 3-5 hours, cooling, and vacuum concentrating until to 1/3-1/4 of its original volume; and adding 0.03-0.06 pt. wt. sodium humate, 0.03-0.06 pt. wt. potassium humate, 0.1-0.15 pt. wt. urea, 0.1-0.2 pt. wt. ammonium bicarbonate, 0.5-0.1 pt. wt. phosphogypsum, 0.05-0.1 pt. wt. potassium citrate, 0.02-0.05 pt. wt. zinc sulfate, 0.02-0.05 pt. wt. amino acid, 0.02-0.05 pt. wt. polyvinyl alcohol, 0.2-0.4 pt. wt. cellulose, and 0.05-0.08 pt. wt. calcium carbide, stirring, spray drying, and granulating.
NOVELTY - A composite organic fertilizer comprises biogas residue, weathered coal, bamboo charcoal powder, photosynthetic bacteria powder, silk powder, Bacillus licheniformis powder, duck manure, cotton powder, oilseed powder, goose manure, coral reef, cortex fraxini, Stemona, potassium sulfate, wheat powder, peanut powder, soybean powder, humic acid, amino acids, chitosan, peanut cake, sodium aluminum phosphate and sepiolite.    USE - Composite organic fertilizer used for tea tree.    ADVANTAGE - The fertilizer is safe and environment-friendly.    DETAILED DESCRIPTION - A composite organic fertilizer comprises 20-30 pts. wt. biogas residue, 25-30 pts. wt. weathered coal, 15-30 pts. wt. bamboo charcoal powder, 0.0001 pt. wt. photosynthetic bacteria powder, 0.0001 pt. wt. silk powder, 0.0001 pt. wt. Bacillus licheniformis powder, 25-30 pts. wt. duck manure, 15-20 pts. wt. cotton powder, 25-30 pts. wt. oilseed powder, 15-20 pts. wt. goose manure, 15-20 pts. wt. coral reef, 3-6 pts. wt. cortex fraxini, 3-5 pts. wt. Stemona, 11-20 pts. wt. potassium sulfate, 10-20 pts. wt. wheat powder, 12-15 pts. wt. peanut powder, 15-19 pts. wt. soybean powder, 1-3 pts. wt. humic acid, 0.1-0.3 pt. wt. amino acids, 0.3-0.6 pt. wt. chitosan, 15-20 pts. wt. peanut cake, 4-8 pts. wt. sodium aluminum phosphate and 2-5 pts. wt. sepiolite.
NOVELTY - Preparation of complex fertilizer comprises taking horse manure, adding microbial agents, composting for 4-7 days, taking animal manure, adding microbial agents, composting for 12-15 days, setting aside, adding urea, ammonium bicarbonate and potassium sulfate, stirring, adding licorice powder, seaweed powder, humus and vermiculite, stirring, adding 10-15 kg talc and stirring.    USE - Method for preparing complex fertilizer (claimed).    ADVANTAGE - The method is simple.
NOVELTY - Preparation of 4,5-dihydroxy-9,10-dioxoanthracene-2-carboxylic acid comprises adding concentrated sulfuric acid and Aloe-emodin to reaction flask; controlling temperature at 80-110 degrees C, slowly dropping 10-70% nitrosylsulfuric acid, and maintaining temperature for 1-3 hours; controlling temperature of reaction mixture at 10-50 degrees C, slowly adding dimethylformamide (DMF) aqueous solution, stirring, maintaining temperature for 2-2.5 hours, filtering, and washing with water; and blast drying at 75-85 degrees C for 15-20 hours.    USE - Method for preparing 4,5-dihydroxy-9,10-dioxoanthracene-2-carboxylic acid (claimed).    ADVANTAGE - The method produces 4,5-dihydroxy-9,10-dioxoanthracene-2-carboxylic acid at high purity and high yield.
NOVELTY - A 2-phenylacetamide derivative (I) is prepared by reacting 1-methyl-2-phenylcyclopropane derivative (II), activating agent, solvent and catalyst to obtain methyl 2-amino-2-(4-pyridyl)acetate dihydrochloride derivative (III), and reacting with phthalimide potassium salt.    USE - Method for preparing 2-phenylacetamide derivative used for L-milnacipran synthesis (claimed).    ADVANTAGE - The simple and environment-friendly method has easy-to-obtain raw materials, mild reaction condition, low impurity and high product yield.    DETAILED DESCRIPTION - A 2-phenylacetamide derivative of formula (I) is prepared by reacting 1-methyl-2-phenylcyclopropane derivative of formula (II), activating agent, solvent and catalyst to obtain methyl 2-amino-2-(4-pyridyl)acetate dihydrochloride derivative of formula (III) at - 10 to 40 degrees C for 10 minutes to 48 hours and 40-150 degrees C for 30 minutes to 48 hours, and reacting with phthalimide potassium salt.    LG=-Cl, -OSO2Me, -OCOCF3, -OSO2C6H4Me and OSO2C6H4NO2 radicals.
NOVELTY - Producing alpha -olefin using biodiesel comprises under hydrogen atmosphere, and pressure of 6 MPa, carrying out catalytic reaction of biodiesel with targeted catalyst at below 400 degrees C; where the targeted catalyst is a supported catalyst, and the catalyst active component includes zinc, copper, manganese or cobalt.    USE - The method is useful for producing alpha -olefin using biodiesel (claimed).    ADVANTAGE - The method yields 98% alpha -olefin, and is suitable for industrial production.
NOVELTY - Polyhydric gas liquefaction refrigerant mixture comprises 2-8 mol.% first group of substances including nitrogen; 22-46 mol.% second group of substances including methane; 3-25 mol.% third group of substances including ethane or ethylene; and balance fourth group of substances including propane or propylene.    USE - Polyhydric gas liquefaction refrigerant mixture used for precooling at - 40 to - 60 degrees C.    ADVANTAGE - The polyhydric gas liquefaction refrigerant mixture provides high thermodynamic efficiency, safety, and environmental protection. It can achieve energy-efficient natural gas liquefaction.
NOVELTY - The method comprises synchronously conveying rubbish in a main combustion gasification furnace through closed rubbish transfer room, allowing high temperature gas into a rubbish carbonization furnace for drying the rubbish, allowing high temperature flame into a waste dry distillation furnace for baking and carbonization of the rubbish to produce dry distillation coal, and then extracting dry distillation coal in a negative pressure container.    USE - The method is useful for extracting pure harmless coal using a double-stack type rubbish combustion furnace (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a double-stack type rubbish combustion furnace.
NOVELTY - The method comprises performing oxidative degradation on rice hull powder and then pre-heating the rice hull powder, performing pyrolysis on the powder in a pyrolysis furnace under the presence of non-condensible gas at 600-750 degrees C, quickly drying the pre-heated powder, freezing the dried powder in a decoking kiln at 300-400 degrees C, condensing the powder using an air-cooled condenser at 130-150 degrees C, cooling the powder with heavy or light oil at 100-120 degrees C, and providing a minor amount of small organic molecules and condensed liquid to the condenser at 50-80 degrees C.    USE - The method is useful for preparing biomass such as methanol (claimed).    ADVANTAGE - The method allows affordable and eco-friendly preparation of the biomass.    DETAILED DESCRIPTION - The method comprises performing oxidative degradation on rice hull powder and then pre-heating the rice hull powder, performing pyrolysis on the powder in a pyrolysis furnace under the presence of non-condensible gas at 600-750 degrees C, quickly drying the pre-heated powder, freezing the dried powder in a decoking kiln at 300-400 degrees C, condensing the powder using an air-cooled condenser at 130-150 degrees C, cooling the powder with heavy or light oil at 100-120 degrees C, providing a minor amount of small organic molecules and condensed liquid to the condenser at 50-80 degrees C, adding methanol and sulfuric acid in a mass ratio of 500:1-100:200 in the powder at a reaction vessel and then sealing, heating the sealed mixture at 70-80 degrees C for 2-4 hours, cooling the mixture with catalyst and calcium carbonate at 40-50 degrees C for 1-2 times, and filtrating the mixture. The pyrolysis is performed at 700 degrees C. The pre-heating step is performed at 350 degrees C. A mass ratio of the methanol, the sulfuric acid and the powder is 100:300:2. The step of filtrating the mixture is performed at constant temperature for 3 hours.
NOVELTY - A biomass pyrolysis device comprises spiral feeding device (1), preprocessing stirrer (2), pyrolysis device (3), steam generator, (4) calcining device (5), combustion device, cavity, serpentine coil, boiling water tank, hot disk tube and fuel chamber.    USE - Biomass pyrolysis device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass pyrolysis device comprising feeding biomass feedstock, mixing biomass materials, heating using superheated steam at 120-150 degrees C, drying, drying under anaerobic conditions, heating at 600-800 degrees C, performing thermal analysis of combustible gas, generating hot flue gas via combustion, and calcining.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass pyrolysis device.    Spiral feeding device (1)    Preprocessing stirrer (2)    Pyrolysis device (3)    Steam generator (4)    Calcining device (5)
NOVELTY - The method involves mixing biomass steam and waste tire pyrolysis steam that are heated to obtain common hot cracking steam. The hot cracking steam is passed through a first-stage condenser that is heated to obtain first-level pyrolysis oil and first-level common hot cracking steam. The first-level common hot cracking steam is heated to obtain liquid product and non-condensable gas. Liquid product delamination process is performed to obtain second-level pyrolysis oil. The first-level pyrolysis oil and the second-level pyrolysis oil are mixed to obtain pyrolysis oil.    USE - Method for preparing biomass and waste tire cracking steam liquefied pyrolysis oil.    ADVANTAGE - The method enables regulating flow rate of the hot cracking steam to control the mixing ratio of the pyrolysis oil. The method enables avoiding heat loss of the biomass steam and waste tire pyrolysis steam due to different hot cracking effects. The method enables improving biomass steam and waste tire pyrolysis steam hot cracking effect so as to improve quality of the pyrolysis oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a biomass and waste tire cracking steam liquefied pyrolysis oil preparing method. '(Drawing includes non-English language text)'
NOVELTY - An environment-friendly alcohol-based fuel comprises 50-80 pts. wt. methanol, 40-60 pts. wt. n-butanol, 10-20 pts. wt. xylene, 40-60 pts. wt. petroleum ether and 10-20 pts. wt. diethyl ether.    USE - Environment-friendly alcohol-based fuel.    ADVANTAGE - The method is low-cost and simple. The fuel is highly flammable.
NOVELTY - An alcohol fuel comprises 60-70 pts. wt. gasoline, 25-30 pts. wt. methanol, 3-7 pts. wt. composite additives and 1-3 pts. wt. core additives.    USE - Alcohol fuel.    ADVANTAGE - The fuel has high octane value and clean discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol fuel comprising mixing core additives and gasoline, stirring for 15-20 minutes, mixing composite additives and methanol, stirring for 15-20 minutes, adding gasoline blend, mixing, and stirring for 35-40 minutes.
NOVELTY - A methanol fuel comprises 15-60 pts. wt. gasoline, 37-84 pts. wt. methanol and methanol-based additive.    USE - Methanol fuel used for vehicles.    ADVANTAGE - The methanol fuel is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass methanol diesel oil comprising methanol fuel by mixing all raw materials, analyzing samples, and inspecting.
NOVELTY - Additive comprises 18-31 wt.% 2,2-diisopropyl-1,3-dioxolane, 15-29.5 wt.% amino diethoxyethylamine, 15-24.5 wt.% 1,3-cyclooctadiene, 13-24 wt.% 1-cyanoethyl-2-ethyl-4-methylimidazole, 10-20.5 wt.% 5-methyl-2-hepten-4-one and 9-19.5 wt.% 1,4-bis(2-phenylethyl)benzene.    USE - Additive used for improving power performance of methanol-based gasoline (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of additive comprising mixing 2,2-diisopropyl-1,3-dioxolane, 1,4-bis(2-phenylethyl)benzene and 1,3-cyclooctadiene in reaction kettle, stirring, adding amino diethoxyethylamine and 5-methyl-2-hepten-4-one and uniformly mixing.
NOVELTY - Methanol-based gasoline additive comprises 3-20 pts. wt. ethylene glycol monomethyl ether oleate, 2-5 pts. wt. diacetone alcohol, 4-10 pts. wt. ethylene glycol monoethyl ether, 10-80 pts. wt. butanol, 5-50 pts. wt. pentanol, 3-20 pts. wt. hexanol, 0.5-10 pts. wt. heptanol and 0.5-10 pts. wt. octanol.    USE - Methanol-based gasoline additive.
NOVELTY - An integrated marsh gas purifying device comprises marsh gas preprocessing filter, air storage tank, air compressor, first reaction tower (4), second reaction tower (5), 2 control meters, 2 refrigeration systems, liquid carbon dioxide storage tank, air outlet, air inlet, separating liquid outlet (15), discharge port, biogas storage tank, carbon dioxide outlet (16) and guide plate (18).    USE - Integrated marsh gas purifying device.    ADVANTAGE - The energy-saving and environment-friendly integrated process has simple structure, automated control, and purification efficiency of more than 95%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purification of marsh gas comprising taking crude marsh gas, filtering, compressing to 15-25 bar, charging into reaction tower, refrigerating to 5-15 degrees C, reacting, condensing, separating impurities, charging into second reaction tower, reacting at 35-55 degrees C under pressure of 15-25 bar, condensing, purifying, separating liquid carbon dioxide and methane, and storing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of integrated marsh gas purifying device.    First reaction tower (4)    Second reaction tower (5)    Separating liquid outlet (15)    Carbon dioxide outlet (16)    Guide plate (18)
NOVELTY - High combustion value biomass particle comprises 25-45 wt.% tree bark, 30-50 wt. tree stem, 20-45 wt.% bamboo shavings and 0.1-1 wt.% oxidant.    USE - High combustion value biomass particle.    ADVANTAGE - The fuel has no hazardous flue gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of high combustion value biomass particle comprising weighing raw materials, crushing tree bark, tree stem and bamboo shavings, drying, screening, controlling moisture content, adding oxidant, mixing, palletizing and cooling.
NOVELTY - Lubricant additive comprises 40-60 wt.% thiophene sulfonic acid derivative (I), 20-30 wt.% organic phosphate vacuum anti-wear agent and 20-30 wt.% mineral diluent oil.    USE - Lubricant additive used for methanol gasoline fuel.    ADVANTAGE - The lubricant additive greatly improves combustion powder performance of vehicle.    DETAILED DESCRIPTION - Lubricant additive comprises thiophene sulfonic acid derivative of formula (I), 20-30 wt.% organic phosphate vacuum anti-wear agent and 20-30 wt.% mineral diluent oil.    R=1-4C alkyl or 1-4C alkoxy;    M=Ca, Mg, Zn, K or Na; and    n=1 or 2.    An INDEPENDENT CLAIM is included for the preparation of lubricant additive comprising mixing sulfur thiophene sulfonic acid derivative (I), organic phosphate vacuum anti-wear agent and mineral diluent oil, heating at 80-120 degrees C for 2 hours, cooling to 40-60 degrees C for 5-8 hours, and clarifying.
NOVELTY - Supercritical carbon dioxide (CO2) extraction of fragrant cinnamon oil comprises picking leaves, drying for 12-16 days, removing impurity, crushing to 20-40 mesh, adding ethanol at ratio of 100 g:200 mL, filling with CO2 at flow rate of 5-10 L/hour, extracting at 40-50 degrees C under pressure of 10-30 MPa for 60-120 minutes, separating at pressure of 10-12 MPa, and removing wax at 40-50 degrees C.    USE - Method for extracting fragrant cinnamon oil using supercritical carbon dioxide (claimed).    ADVANTAGE - The method is simple, easy to control, low-cost, free from residual organic solvent, safe for humans, and non-polluting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fragrant cinnamon oil comprising 25-30 wt.% eucalyptol, 23-25 wt.% terpinyl acetate, 13-15 wt.% linalool, 12-13 wt.% isoeugenol methyl ether, 5-7 wt.% alpha -terpineol, 3-5 wt.% eugenol, 2-4 wt.% beta -phellandrene, 3-5 wt.% alpha -cadinene and 2-4 wt.% bicyclogermacrene.
NOVELTY - Trichoderma viride PF1, with the preservation number CGMCC No. 8434, is new.    USE - The strain is useful in preparing bio-fertilizer for improving physical and chemical properties of soil (all claimed), and crop growth.    ADVANTAGE - The strain can produce rich mycelium, efficiently express beta -1,4-glucan hydrolase, chitinase, cellulase and protease activity of the particular enzymes, produce volatile or nonvolatile active substance for inhibiting the growth of bacteria, and thus suitable for bio-fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of Trichoderma viride PF1 in preparing bio-fertilizer.
NOVELTY - Preparing biogas by Eupatorium adenophorum fermentation, comprises (i) harvesting fresh purple leaves Eupatorium adenophorum, and removing roots, to obtain fermentation raw materials; (ii) composting; (iii) extracting, adding stock solution according to solid-liquid ratio into a biogas tank, and fermenting at 25-50 degrees C; and (iv) collecting the gas produced, exporting biogas after fermentation once the fermentation time reaches a predetermined minimum time to perform fermentation of biogas, and performing detoxification of Eupatorium adenophorum fermentation material.    USE - The method is useful for preparing biogas by Eupatorium adenophorum fermentation (claimed).    ADVANTAGE - The method has simple preparation procedure, easy operation procedure, and low production cost.    DETAILED DESCRIPTION - Preparing biogas by Eupatorium adenophorum fermentation, comprises (i) harvesting fresh purple leaves Eupatorium adenophorum, and removing roots, to obtain fermentation raw materials; (ii) composting the fermentation raw materials under anaerobic environment for 2-4 days; (iii) extracting 320-400 g/l qualified composted fermentation raw materials, adding the stock solution according to solid-liquid ratio into a biogas tank, and fermenting at 25-50 degrees C; and (iv) collecting the gas produced, exporting biogas after fermentation once the fermentation time reaches a predetermined minimum time to perform fermentation of biogas, and performing detoxification of Eupatorium adenophorum fermentation material to obtain the product.
NOVELTY - Extraction and purification of resveratrol comprises pulping knotweed, crushing, performing dynamic countercurrent extraction using 30-90% ethanol at 40-70 degrees C for 6-10 hours, concentrating, performing enzymolysis for 6-15 hours, stirring, filtering crude product, performing methanol extraction, drying to obtain emodin, extracting liquid using column chromatography, crystallizing using ethanol and drying.    USE - Method for extracting and purifying resveratrol (claimed).    ADVANTAGE - The method is environment-friendly, improves extraction rate, shortens conversion time and has wide applicability.
NOVELTY - Preparation of arginine-containing fermentation liquor comprises sterilizing Corynebacterium ammoniagenes at 30 degrees C for 22 hours, inoculating seed culture at 30 degrees C for 18 hours, stirring at 30 degrees C for 14 hours to obtain first stage seed culture medium, stirring at 30 degrees C for 4 hours to obtain second stage seed culture medium, sterilizing culture medium, adding 1 wt.% glucose and nutrient substance, adjusting pH value to 6.7 and standing at 30 degrees C for 70-75 hours.    USE - Method for preparing arginine-containing fermentation liquor (claimed).    ADVANTAGE - The method increases arginine yield, reduces impurities, and minimizes water, acid, alkali and activated carbon wastes.
NOVELTY - Extraction and preparation of arginine comprises culturing Brevibacterium at 30 degrees C for 20 hours, inoculating at 30 degrees C for 22 hours, stirring at 30 degrees C for 18 hours to obtain first stage seed culture medium, stirring at 30 degrees C for 4-6 hours to obtain second stage seed culture medium, adding 2 wt.% glucose, 5 wt.% corn steep liquor, 0.8 wt.% ammonium sulfate, 0.2 wt.% monopotassium sulfate and 0.3 wt.% potassium hydrogen phosphate trihydrate, adjusting pH value to 7.1, and standing for 68-72 hours.    USE - Method for extracting and preparing arginine (claimed).    ADVANTAGE - The method is inexpensive, reduces labor intensity, and minimizes water, acid, alkali and activated carbon wastes.
NOVELTY - Preparation of L-glutamine-containing fermentation liquor comprises culturing Corynebacterium ammoniagenes at 28-32 degrees C for 20-24 hours, inoculating culture medium at 28-32 degrees C for 16-20 hours, stirring at rotating speed of 240 revolutions/minute (rpm) at 28-32 degrees C for 12-16 hours to obtain first stage seed culture medium, stirring at rotating speed of 220 rpm and 28-32 degrees C for 2-6 hours to obtain second stage seed culture medium, sterilizing, adjusting pH value to 7.0-7.2, adjusting pH value to 5.5-5.7 at 12-44 degrees C after 12 hours and controlling sugar content.    USE - Method for preparing L-glutamine-containing fermentation liquor (claimed).    ADVANTAGE - The method improves yield, reduces production cost, and minimizes water, acid, alkali and activated carbon wastes.
NOVELTY - A liquefied hydrogen-rich methane production device comprises mixed refrigerant compressor (1), interstage cooler (2), stage cooler (3), middle gas-liquid separating tank (4), liquid nitrogen compressor (5), heat exchanger, gas-liquid separator refrigerant, heat exchangers, cooling device, denitrification tower, rectifying tower, dehydrogenation tower, evaporator, bottom tower, reboiler set and condenser.    USE - Liquefied hydrogen-rich methane production device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of liquefied hydrogen-rich methane production device.    Mixed refrigerant compressor (1)    Interstage cooler (2)    Stage cooler (3)    Gas-liquid separating tank (4)    Liquid nitrogen compressor (5)
NOVELTY - The device has a main heat exchanger comprising a low-temperature heat exchanger, a low-temperature heat exchanger deep unit and a mixing refrigerant compressor refrigerating system. A refrigeration compressor is provided with a mixing and separating tank. A bottom part of a nitrogen tower is fixed with a rectifying tower reboiler. A dehydrogenation rectifying tower is formed with a reflux liquid inlet that is matched with a gas outlet of a separator. A cold fluid section of the low-temperature heat exchanger deep unit is fixed with a cold fluid section of the low-temperature heat exchanger.    USE - LNG methane-rich gas hydrogen-rich product manufacturing device.    ADVANTAGE - The device realizes single mixed working substance compressor refrigerating process, reduces station coolant compressor utilization cost and isopentane and isobutane mixing refrigerant ratio so as to effectively improve section plate-type flow rate. The device is simple operate, and has better operation reliability, and reduces mixed coolant compressor refrigerating process energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a LNG methane-rich gas hydrogen-rich product manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a LNG methane-rich gas hydrogen-rich product manufacturing device.'(Drawing includes non-English language text)'
NOVELTY - Bamboo procyanidin extract is obtained by cutting red colored bamboo to diameter of plus minus 1cm, extracting using 1% hydrochloric acid-ethanol solution in a weight ratio of 20-40:1, immersing for 48 hours in dark condition, quenching, extracting for 2-4 times, adding extracted filtrate, concentrating at -50 degrees C, to relative density of 1.02-1.2, dissolving obtained concentrate in distilled water, filtering, adjusting pH to 6-8 using sodium hydroxide, eluting mixture using 20-60% ethanol and macroporous adsorption resin, collecting 20-80% ethanol eluent, concentrating and drying.    USE - Bamboo procyanidin extract is used for health care product and food.    ADVANTAGE - The nontoxic bamboo procyanidin extract is economically and environmentally-friendly prepared.
NOVELTY - A sterile soilless cultivation nutrient solution additive comprises 6-8 wt.% microalgae polysaccharides, 4-6 wt.% live luciferase marine organisms, 3-7 wt.% chitin, 6-9 wt.% liquid soybean, 5-7 wt.% green tea extraction solution, 0.5-0.8 wt.% polyhexamethylene guanidine subunit, and balance purified water.    USE - A sterile soilless cultivation nutrient solution additive.    ADVANTAGE - The additive is stable, readily biodegradable and environment-friendly, and reduces hazardous chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sterile soilless cultivation nutrient solution additive comprising:    (A) washing the microalgae, washing, drying, and milling cerium powder obtain the dry powder by ethanol extraction to obtain microalgae polysaccharides;    (B) cleaning the soybean, grinding, filtering, and diluting to obtain soybean liquid;    (C) drying the green tea, crushing, and adding 50% aqueous solution to obtain green tea extraction liquid;    (D) adding the polysaccharide to stirring tank, adding one-half of purified water, and stirring uniformly;    (E) adding slowly the enzyme, chitin, and polyhexamethylene guanidine in stirring tank, and stirring uniformly;    (F) extracting soybean, adding green tea extraction liquid to the solution, adding the other half of water, heating at 35 degrees C, and stirring uniformly, and    (G) aseptic packaging.
NOVELTY - Bioorganic fertilizer comprises 40-50 wt.% monosodium glutamate waste, 5-8 wt.% dinotefuran, 3-4 wt.% tebuconazole, 35-45 wt.% boric acid residue, and 3-5 wt.% Beauveria bassiana spores.    USE - As bioorganic fertilizer (claimed).    ADVANTAGE - The fertilizer is prepared by simple method, and environmentally-friendly, increases soil ventilation property, leaves no residues and can be dried at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing boric acid residue to 100-150 meshes, adding B.bassiana spore to the crushed residue, mixing and adding monosodium glutamate waste, granulating the mixture to 8-30 meshes using drum granulator, adding dinotefuran and tebuconazole, mixing, adding water, and spray-drying the mixture.
NOVELTY - Organic-inorganic fertilizer comprises 30-40 pts. wt. of monosodium glutamate, 15-30 pts. wt. of macronutrient fertilizers, 30-40 pts. wt. of boric sludge slag, 10-15 pts. wt. of humic acid, 0.3-0.5 pts. wt. of carbosulfan, 1-1.5 pts. wt. of photosynthetic bacteria and 2-3 pts. wt. of bacterial enzymes.    USE - Organic-inorganic fertilizer.    ADVANTAGE - The organic-inorganic fertilizer is eco-friendly, and has comprehensive nutrition, increased soil ventilation property, loose soil plate structure and reduced chemical fertilizer adjuvant residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic-inorganic fertilizer comprising uniformly mixing monosodium glutamate, macronutrient fertilizers, and humic acid, then adding photosynthetic bacteria and bacterial enzymes, fermenting at 50-70 degrees C for 10-15 days, then adding boric sludge slag, uniformly mixing, granulating, dissolving carbosulfan with water, diluting, then uniformly spraying, and sieving to obtain organic-inorganic biological compound fertilizer granule having a particle diameter of 2-4 mm.
NOVELTY - Nelarabine (I) is prepared by dissolving furan derivative (II) in inert solvent A, reacting with nucleophilic reagent, deprotecting using alkali B in inert solvent B, adding deprotecting reagent, and reacting.    USE - Method for preparing nelarabine (claimed).    ADVANTAGE - The method has simple operation, easy purification, high yield, low cost, and environment-friendly reaction.    DETAILED DESCRIPTION - Nelarabine of formula (I) is prepared by dissolving furan derivative of formula (II) in inert solvent A, adding nucleophilic reagent, carrying out nucleophilic substitution, deprotecting using alkali B in inert solvent B, adding deprotecting reagent, and reacting.
NOVELTY - This utility new type relates to a one energy-saving type tea saponin extraction device. The traditional tea saponin extraction operation link multi-period long, extraction agent consumption. This utility new type of target provide a one energy-saving type tea saponin extraction device, simple structure, convenient use, easy operation and control, and high extraction rate. The extraction device, include extraction liquid, foam-separating tower, a foam collector, provide compressed air of air supply system and supplying extraction liquid of fluid infusion system, air supply system and the foam separating tower and a extraction liquor storage device connecting the upper foam separation tower is provided with a feeding port, foam-separating tower is set at the bottom of gas distributor, upper end of gas distributor of glass fibre bag is equipped with a tea seed cake. This utility new type has simple structure, easy operation, easy control, extraction time is short, the energy consumption and high extraction rate, simplifies the traditional tea saponin extraction process.
NOVELTY - This utility new type aims to provide one of a compost turning machine, include a base and a main body, said main body through support frame is set on the upper part of the base, the left end of said main body is provided with a stirring device, in part of main body is set with a cylinder, one end of the cylinder connecting the upper main body, and the other end connecting the base up, used for lifting main body. Through mounting cylinder, drives the upper main body, and lower pulling cylinder and allixiary reinforcing plate is added, the rising and falling of the main body is more stable and is provided with a handle, a manually lifting body, and is added, the safety hidden trouble and improves the working efficiency, prolong device use lifetime.
NOVELTY - Cultivating bamboo shoots in sawdust fermentation material, involves collecting Ganoderma powder, reacting the powder, stacking pre-processed material with e.g. wheat bran, regulating C/N ratio, maintaining water content, mixing e.g. fermentation material and water, culturing the bamboo shoots, covering the shoots with soil, covering cultivated material using plastic film, performing fruiting management, and harvesting bamboo.    USE - The method is useful for cultivating bamboo shoots in sawdust fermentation material (claimed).    ADVANTAGE - The method reduces pollution, improves production efficiency, and is cost-effective.    DETAILED DESCRIPTION - Method for cultivating bamboo shoots in sawdust fermentation material, involves collecting Ganoderma powder without mildew, using lime water of mass concentration 2%, reacting the powder for 24-48 hours, stacking pre-processed material with 13 pts. wt. wheat bran, 5 pts. wt. urea and 0.5 pts. wt. gypsum powder, regulating C/N ratio to 30-40:1, maintaining water content of 60-65%, ventilating and fermenting the materials at 60 degrees C, mixing 96 pts. wt. fermentation material, 2 pts. wt. soybean powder, 1 pt. wt. saw powder, 0.9 pts. wt. gypsum powder, 0.1 pts. wt. white sugar and 60-65 pts. wt. water, culturing the bamboo shoots in the above-mentioned mixture, covering the shoots with soil, covering cultivated material using plastic film for 3-5 days, uniformly spraying 0.5% formaldehyde solution for 3-5 days, performing fruiting management at 24-26 degrees C under natural light for 30 minutes for 15-20 days, and harvesting bamboo.
NOVELTY - This new type utility claims a purifying water by microbes one sewage treatment device, it include sandwich-type glass steel of upper filtering tank body is set with water inlet tube and water outlet tube, a filter tank body at least set with three between each two adjacent baffle plate set with one of, for each upper transverse for at least set with one of sun-shading net-type microorganism culture net, upper filtering tank body upper part set with viewing port, a viewing port set with cover, the upper of each baffle plate is uniformly set with one for , upper oxygen pipe in the upper filter tank body is further set with air vent and upper sludge discharging pipe, a sludge discharging tube set with filth, a filter tank body set with set with oxygen of Meat and oxygen-supplying port, the oxygen pipe is set on the sludge pipe. This utility new type has simple structure, low cost, mechanical filter at the same time, it can by microorganism adsorbing a sewage multi-element process of purified water.
NOVELTY - The stirrer has a transmission shaft (7) fixed with an upper bearing base (6) and an output belt wheel (5). A transmission belt (4) is connected with a lower input belt wheel (2) and the output belt wheel. The transmission shaft is fixed with a stirring shaft (11) by a shaft joint (10). A lower end of the stirring shaft is fixed with a self-suction stirring impeller (12). The impeller includes an upper flange and a lower flange. The transmission shaft is fixed with a screw thread connector. A first flow channel is matched with a second flow channel that is matched with a third flow channel.    USE - Municipal oxygen supplying domestic rubbish fermentation stirrer.    ADVANTAGE - The stirrer satisfies oxygen supplying domestic rubbish fermentation stirring processing requirements.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a municipal oxygen supplying domestic rubbish fermentation stirrer in partial section.    Lower input belt wheel (2)    Transmission belt (4)    Output belt wheel (5)    Upper bearing base (6)    Transmission shaft (7)    Shaft joint (10)    Stirring shaft (11)    Self-suction stirring impeller (12)
NOVELTY - Preparation of aluminum oxide/calcium magnesium oxide composite solid base catalyst comprises adding alumina powder into nitrate solution, mixing, adding sodium carbonate and sodium hydroxide, adjusting pH to 8-9, forming colloidal precipitation, stirring at 60 degrees C, aging for 24 hours, filtering, washing spent ion with water, drying at 120 degrees C, placing dried precipitate in muffle furnace, calcining at 800 degrees C for 6 hours, cooling to room temperature, triturating, sieving and obtaining 140-200 mu m composite catalyst particles.    USE - Method for preparing aluminum oxide/calcium magnesium oxide composite solid base catalyst (claimed) used for biodiesel production.    ADVANTAGE - The method has up to 97% biodiesel yield using waste vegetable oil and ethanol catalyzed transesterification under mild conditions.    DETAILED DESCRIPTION - Preparation of aluminum oxide/calcium magnesium oxide composite solid base catalyst comprises adding alumina powder into nitrate solution comprising calcium nitrate tetrahydrate and magnesium nitrate hexahydrate, mixing, adding sodium carbonate and sodium hydroxide, adjusting pH to 8-9, forming colloidal precipitation, stirring vigorously at 60 degrees C, aging for 24 hours, filtering precipitate, washing spent ion with water repeatedly, drying at 120 degrees C, placing dried precipitate in muffle furnace, calcining at 800 degrees C for 6 hours, cooling to room temperature, triturating, sieving and obtaining 140-200 mu m composite catalyst particles.
NOVELTY - Preparation of earthworm biofilter comprises setting 40-50 cm height bottom layer with coarse quartz sand and zeolite particles, 30-40 cm height intermediate layer with fine quartz sand and zeolite particles and 30-40 cm height top layer comprising organic media and inorganic filter, and adding earthworms.    USE - Method for preparing earthworm biofilter used for treating sewage (claimed).
NOVELTY - Natural resource diversified integrated life support system comprises water treatment unit, sedimentation tank, seawater pool, water retention pond, natural sink, dirt collecting tank, heat exchanger, solar evaporator, wind powder drain pump, steam turbine generator, filter, water storage tank, solar energy guiding unit, light source, purifier, sewage treatment unit, fresh water reservoir, waste recovery unit, fermentation tank, organic soil culture plant and internal combustion generator.    USE - Natural resource diversified integrated life support system.    ADVANTAGE - The system is safe, self-sufficient, environment-friendly, reduces labor cost by 80% and reduces material transportation cost.
NOVELTY - Method for preparing organic fertilizer, involves adding biogas slurry into sedimentation tank, adding the obtained product to hydrolysis-acidification tank, adding the resulting product to flocculation device, fine filtration device and fermentation tanks, and packing the obtained product.    USE - The method is useful for preparing organic fertilizer, preferably root or foliar fertilizer (claimed).    ADVANTAGE - The method avoids clogging problems (removes suspended particles).
NOVELTY - Method for processing organic fertilizer, involves treating bean curd using enzyme and lactic acid bacteria, and treating the obtained product.    USE - The method is useful for processing organic fertilizer (claimed).    ADVANTAGE - The method is simple, and suitable for industrialization. The organic fertilizer processed by the method does not require high temperature (for sterilization).
NOVELTY - Method of fermenting and composting organic waste involves (a) collecting dry organic waste e.g. dry straw and wet organic waste e.g. brewery lees; (b) mixing and drying the organic waste collected in step(a) to have moisture content of 60% or less; (c) adding microbial inoculum to the obtained organic waste in weight ratio of 3000-5000 and carrying out anaerobic fermentation of mixed materials; (d) casting the fermentation product using machine or hand and mixing uniformly; (e) performing stacking of obtained mixture at low temperature to obtain product.    USE - The method is useful for fermenting and composting organic waste for preparing organic fertilizer (claimed).    ADVANTAGE - The method is simple, less time-consuming and hence suitable for industrial application.    DETAILED DESCRIPTION - Method of fermenting and composting organic waste involves (a) collecting dry organic waste chosen from dry straw, mushroom residue, peanut shell and other agricultural waste having moisture content of 40% or less and wet organic waste chosen from brewery lees, monosodium glutamate factory residue, industrial fermentation residue and urban sewage treatment plant residue having moisture content of 40-95%; (b) mixing and drying the organic waste collected in step(a) to have moisture content of 60% or less; (c) adding microbial inoculum to the obtained organic waste in weight ratio of 3000-5000 and carrying out anaerobic fermentation of mixed materials; (d) casting the fermentation product using machine or hand and mixing uniformly; (e) performing stacking of obtained mixture at low temperature to obtain product.
NOVELTY - Method for preparing organic fertilizer using AT-18 enzyme composition involves (a) crushing organic waste, (b) adjusting carbon and nitrogen ratio of organic waste to 20-30:1, adding the 50-65% organic waste into fermentor, stirring mechanically and turning continuously, (c) maintaining 35-80 degrees C for 1 hour, maintaining 80 degrees C for 3 hours, and maintaining 55 degrees C for 15 hours, (d) adding 1-5 %mass AT-18 enzyme composition, and (e) stopping fermentation, stirring mechanically, turning continuously, and supplying oxygen for 18 hours.    USE - The method is useful for preparing organic fertilizer using AT-18 enzyme composition (claimed).    ADVANTAGE - The method enables preparation of organic fertilizer at high speed and converts 50-70% organic waste into fertilizer.
NOVELTY - Biological organic fertilizer comprises 30-70 pts. wt. aquatic plant, 20-50 pts. wt. livestock and poultry manure, 5-25 pts. wt. soybean meal, 3-12 pts. wt. coal ash, 1-5 pts. wt. trace element and 0.1-1.5 pts. wt. active strain.    USE - Biological organic fertilizer for aquatic plants (claimed).    ADVANTAGE - The biological organic fertilizer has high viable count, multi-nutrient content and decomposition rate, improves useful microorganism flora in soil, provides growth nutrients to crops and improves yield upon continuous long-term use, and is prepared using waste products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves crushing the raw materials, adding suitable quantity of water, fermenting, granulating, drying, cooling and sieving product.
NOVELTY - Environmentally-friendly edible fungus culture medium comprises 70-80% corn stalk, 70-80% straw, 20-25% rice bran, 3-5% gypsum powder, 3-5% calcium oxide, 3-5% calcium superphosphate, 3-5% white sugar, 3-5% urea, and 0.7% water-absorbing resin.    USE - As edible fungus culture medium.    ADVANTAGE - The edible fungus culture medium is environmentally-friendly, and is rich in nutrient content.
NOVELTY - Composite fertilizer comprises organic fertilizer component, inorganic fertilizer component, Lactobacillus plantarum additive, and traditional Chinese medicinal additive.    USE - As composite fertilizer.    ADVANTAGE - The composite fertilizer improves the fertilizer utilization rate, increases soil organic material, causes no pollution, improves the quality of crop, increases crop yield, protects soil, and reduces usage of chemical fertilizer and pesticide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited composite fertilizer, which involves (a) activating L.plantarum at 32-36 degrees C in enrichment culture liquid, and culturing for 24 hours at low temperature and 220-250 revolutions per minute (rpm), (b) inoculating 2-5% strain in aerobic fermentation medium, and culturing at 32-36 degrees C and 170-200 rpm for 20-24 hours, and (c) filtering using 0.45 mu m filter, sterilizing, naturally air drying or drying at 30 degrees C, and obtaining solid microbial fertilizer having 10 IU/g bacteria amount.
NOVELTY - Organic fertilizer comprises 40-60 pts. wt. poultry manure, 40-60 pts. wt. traditional Chinese medicinal waste, 40-60 pts. wt. edible mushroom waste, 40-60 pts. wt. mineral substances, 20-30 pts. wt. vitamin composition, and 1-10 pts. wt. microbial inoculum.    USE - As organic fertilizer in the form of granule (claimed).    ADVANTAGE - The organic fertilizer provides organic minerals and vitamins to crops, and saves social and natural resources.    DETAILED DESCRIPTION - Organic fertilizer comprises 40-60 pts. wt. poultry manure, 40-60 pts. wt. traditional Chinese medicinal waste, 40-60 pts. wt. edible mushroom waste, 40-60 pts. wt. mineral substances, 20-30 pts. wt. vitamin composition, and 1-10 pts. wt. microbial inoculum. The mineral substance comprises 40-60 pts. wt. sludge, 40-60 pts. wt. coal gangue, 20-30 pts. wt. urea, 20-30 pts. wt. phosphorus, 20-30 pts. wt. potassium, 1-3 pts. wt. silicon, 1-3 pts. wt. sodium selenite, 1-3 pts. wt. zinc sulfate, 1-3 pts. wt. copper sulfate, 1-3 pts. wt. manganese sulfate, 1-3 pts. wt. boric acid, 1-3 pts. wt. sodium molybdate, and 5-10 pts. wt. zeolite powder. The vitamin composition comprises 1-2 pts. wt. vitamin B1, 1-2 pts. wt. vitamin B2, 1-2 pts. wt. vitamin B6, 1-2 pts. wt. vitamin B12, and 1-2 pts. wt. vitamin C. The microbial inoculum comprises 1-2 pts. wt. photosynthetic bacteria, 1-2 pts. wt. nitrifying bacteria, 1-2 pts. wt. lactic acid bacteria, 1-2 pts. wt. Saccharomycetes, 1-2 pts. wt. nitrogen fixing bacteria, 1-2 pts. wt. Actinomycetes, 1-2 pts. wt. phosphate solubilizing bacteria, 1-2 pts. wt. Bacillus subtilis, and 1-2 pts. wt. plant growth promoting bacteria. An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned raw materials, crushing the mixture to 20-80 meshes, fermenting the mixture at less than 65 degrees C for 12-36 hours, granulating the fermented product, packaging the granules and storing the product.
NOVELTY - Fertilizer comprises 8-12 parts mass corn powder, 1 parts mass dipotassium phosphate, 3 parts mass yeast powder, 3 parts mass peptone, 1 parts mass honey and 80 parts mass distilled water.    USE - The fertilizer is useful for stimulating growth of foliage (claimed) in vegetables chosen from rape, spinach, celery and lettuce.    ADVANTAGE - The fertilizer is cost-effective and prepared by simple method and hence suitable for large scale production.
NOVELTY - Bio-fertilizer comprises 15-20 pts. wt. broad bean straw powder, 5-10 pts. wt. conch shell powder, 5-9 pts. wt. clamshell powder, 9-14 pts. wt. calcium monohydrogen phosphate, 3-6 pts. wt. calcium superphosphate, 3-6 pts. wt. potassium nitrate, 2-6 pts. wt. ammonium nitrate, 1-2 pts. wt. rice bran, 10-15 pts. wt. rapeseed cake, 15-20 pts. wt. grass powder, 68 pts. wt. chicken manure, 25-35 soybean cake, 15-30 pts. wt.Phellodendron, and 1-2 pts. wt.Bacillus.    USE - The bio-fertilizer is useful for tea (claimed).    ADVANTAGE - The bio-fertilizer is rich in organic and inorganic nutrients, and multi-nutrients, and nontoxic, and causes no side effects, and does not leave any residues. The fertilizer causes no pollution, and has no drug resistance, and provides necessary nutrients to tea, and improves quality of tea and soil conditions.
NOVELTY - Biological fertilizer comprises raw materials comprising ammonium nitrate, Bacillus subtilis, calcium biphosphate, diammonium phosphate, plant activating enzymes, calcium nitrate, B.thuringiensis powder, dipotassium hydrogen phosphate, sodium pyrophosphate, sodium dihydrogen phosphate, disodium hydrogen phosphate, chicken manure, potassium chloride, rice hull powder, grass carbon, chicken manure, flax straw pole powder and potassium sulfate.    USE - The biological fertilizer is useful for planting tea tree (claimed).    ADVANTAGE - The biological fertilizer improves quality of tea, increases yield of tea, reduces plant diseases and insect pests, and artificial labor intensity, and is convenient to use, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Biological fertilizer comprises raw materials comprising 15-20 pts. wt. ammonium nitrate, 0.003 pts. wt. Bacillus subtilis, 8-14 pts. wt. calcium biphosphate, 9-11 pts. wt. diammonium phosphate, 0.0001 pts. wt. plant activating enzymes, 3-5 pts. wt. calcium nitrate, 0.001-0.003 pts. wt. B.thuringiensis powder, 3-9 pts. wt. dipotassium hydrogen phosphate, 1-2 pts. wt. sodium pyrophosphate, 3-9 pts. wt. sodium dihydrogen phosphate, 11-16 pts. wt. disodium hydrogen phosphate, 25-30 pts. wt. chicken manure, 15-20 pts. wt. potassium chloride, 12-15 pts. wt. rice hull powder, 68 pts. wt. grass carbon, 25-35 pts. wt. chicken manure, 25-30 pts. wt. flax straw pole powder and 11-16 pts. wt. potassium sulfate.
NOVELTY - Method of recycling crystallization mother liquor of divalproex sodium, involves concentrating divalproex crystallization mother liquor, mixing obtained solid mixture containing divalproex, with alkali solution, dissolving, obtaining mixed solution, mixing with an inorganic salt, producing valproate precipitate, mixing obtained valproate precipitate with an acid, obtaining an organic layer, fractionating organic layer, and obtaining valproic acid.    USE - Method of recycling crystallization mother liquor of divalproex sodium (claimed).    ADVANTAGE - The method efficiently and economically recycles crystallization mother liquor of divalproex sodium and provides valproic acid having yield of 93% and purity of 99.6% or more, by simple method.
NOVELTY - Acid is added to reaction container, and acetic anhydride and concentrated sulfuric acid are added and mixed uniformly. Distilled water is added to reaction container, agitated, set in cold water bath and filtered to obtain crude acetyl salicylic acid. Crude acetyl salicylic acid is transferred to a beaker, and 10% sodium bicarbonate is added and stirred. The high polymer solid is filtered out, and 18% concentrated hydrochloric acid is added to the obtained filtrate. The container is then placed in cold water bath for 5-30 minutes, filtered and dried to obtain acetylsalicylic acid.    USE - Preparation of acetylsalicylic acid (claimed).    ADVANTAGE - The method efficiently provides acetylsalicylic acid by simple method, without affecting the environment.    DETAILED DESCRIPTION - An acid is added to a reaction container, and acetic anhydride and concentrated sulfuric acid having concentration of 98% are added and mixed uniformly into glass beads. The reaction container is shaked until the crystals are separated, such that mass ratio of salicylic acid, acetic anhydride and concentrated sulfuric acid is 2 g:3-6 ml:0.15-0.6 ml. Distilled water is added to reaction container, and the obtained solution is added. The mixture is then agitated with glass rod, such that crystals are not deposited in the reaction container. The reaction container is set in a cold water bath for 5-30 minutes, and filtered to obtain crude acetyl salicylic acid. The crude acetyl salicylic acid is transferred to a beaker, and 10% sodium bicarbonate is added and stirred. The high polymer solid is filtered out, and 18% concentrated hydrochloric acid is added to the obtained filtrate. The container is then placed in cold water bath for 5-30 minutes, filtered and dried to obtain acetylsalicylic acid.
NOVELTY - Terbutaline sulfate (I) is obtained by adding bambuterol hydrochloride (II) to sodium hydroxide aqueous solution, stirring for 5-10 minutes, reacting under heat-reflux conditions for 3-20 hours, and detecting reaction by thin-layer chromatography.    USE - Synthesis of terbutaline sulfate for use in pharmaceutical field.    ADVANTAGE - The method enables convenient and environmentally-friendly industrial synthesis of terbutaline sulfate with high purity and high yield (50%), under mild conditions. The obtained compound meets European 7.8 edition pharmacopoeia standards and American 36 edition pharmacopoeia standards.    DETAILED DESCRIPTION - Terbutaline sulfate of formula (I) is obtained by adding bambuterol hydrochloride of formula (II) to sodium hydroxide aqueous solution, stirring for 5-10 minutes, reacting under heat-reflux conditions for 3-20 hours, and detecting reaction by thin-layer chromatography.
NOVELTY - 3-Hydroxy-2-butanone, 95% ethanol and ammonium acetate in a ratio of 1:1:1-2 are used as raw materials, and absolute ethyl alcohol, methanol, acetone, butanone and dimethylformamide are used as solvent, to prepare pyrazine compound (I), or its salt (II) or (III).    USE - Preparation of pyrazine compound used as spices, food additive, photosensitizer, pharmaceutical and pesticide.    ADVANTAGE - The method enables environmentally-friendly and economical preparation of pyrazine compound by a simple process with high yield and reduced energy consumption.    DETAILED DESCRIPTION - 3-Hydroxy-2-butanone, 95% ethanol and ammonium acetate in a ratio of 1:1:1-2 are used as raw materials, and absolute ethyl alcohol, methanol, acetone, butanone and dimethylformamide are used as solvent, to prepare pyrazine compound of formula (I), or its salt of formula (II) or (III).
NOVELTY - Preparation of acipimox involves reacting 5-methylpyrazine-2,3-dicarboxylic acid, water, acid, sodium tungstate and hydrogen peroxide as raw material, using water as solvent, hydrogen peroxide as oxidant, acid and sodium tungstate as catalyst. The molar ratio of 5-methylpyrazine-2,3-dicarboxylic acid, hydrogen peroxide and sodium tungstate is 1:0.05-5:1-10:0.04-0.2.    USE - Preparation of acipimox (claimed).    ADVANTAGE - The acipimox having favorable purity of more than 99.5% is economically prepared by simple and environmentally-friendly method in short time, with yield of more than 80%.
NOVELTY - The device has feed conveyor (3), vertical type airtight heat processing device (1), ash slag machine, and hydrocarbon oil collecting and utilizing device that are connected in turn. The feed conveyor is connected with vertical type airtight heat processing device. Upper portion of housing (2) is provided with a feed inlet, and intermittent feeding bin (36) is comprised with cylindrical casing. Bottom portion of case provided with discharge valve (6).    USE - Domestic garbage or organic waste reduction device.    ADVANTAGE - The device is featured with simple structure, convenient operation, low manufacturing cost and high raw material utilization rate. Sterilization effect can be efficiently achieved, consumption of energy can be reduced, and environmental protection can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the domestic garbage or organic waste reduction device.    Vertical type airtight heat processing device (1)    Housing (2)    Feed conveyor (3)    Discharge valve (6)    Intermittent feeding bin (36)
NOVELTY - The method involves crushing biomass material into powder granule and, drying the powder granule. The dried material is sent to a spiral-conveying machine and is sent to a microwave pyrolysis reactor. A cyclone separator is provided for performing gas-solid separation for removing the carbon particles and sand. The biomass oil is collected. The uncondensed gas is cooled for three times, and the low-boiling-point oil is collected. The collected non-condensing gas is recycled.    USE - Method for preparing biomass oil.    ADVANTAGE - The particle size of raw material can be reduced, so as to reduce the preprocessing cost. The pyrolysis temperature can be controlled accurately. The energy consumption can be reduced. The quality of the biomass oil can be improved.
NOVELTY - A bamboo charcoal comprises carbon block of square honeycomb structure having length of 10 cm, width of 10 cm and height of 10 cm.    USE - Bamboo charcoal used in roasting food or for warming in winter.    ADVANTAGE - The bamboo charcoal is small in structure, convenient to use, smokeless and odorless, and is not easy to break, and has high hardness, high carbon content, high heat productivity, long combustion time, and low ash content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the bamboo charcoal, comprising:    (A) sun drying bamboo product residual slag for 1-2 days to water content of 10-15%, and air drying until the water content is less than 5% to obtain dry raw material;    (B) fine grinding the dry raw material by ball milling into 20-90 mesh powder;    (C) drying the powder to water content of 2-3% at 160 degrees C, and then putting into a block making machine to form into 10 cmx 10 cmx 10 cm block at 160-450 degrees C to obtain bamboo charcoal block semi-finished product;    (D) drilling the semi-finished product to obtain honeycomb structure semi-finished bamboo charcoal block; and    (E) sending the charcoal block into a carbonizing furnace in anoxic condition, heating furnace to 150-220 degrees C, controlling temperature of charcoal block to 140-200 degrees C, then continuously heating furnace to 500-800 degrees C and carbonizing and smoldering to form the bamboo charcoal block finished product.
NOVELTY - A bio-fertilizer for water hyacinth comprises 4-40% microbial inoculum, 4-30% nutrient content, 10-80% soluble carrier and 2-20% microelement chelate.    USE - As bio-fertilizer for water hyacinth (claimed).    ADVANTAGE - The bio-fertilizer is stable; has high efficiency and wide applicability; is prepared by simple and low cost preparation process; can inhibit propagation and eggs of insect pathogenic microorganism; and can prevent the occurrence of plant diseases and insect pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation bio-fertilizer involving a) preparation culture medium having the pH value of 5-7; b) inoculating microbial inoculum comprising Bacillus subtilis, Trichoderma, Nocardia and/or small Aeromonas into culture medium obtained in step a); c) preparation nutrient content, soluble carrier and microelement chelate; and d) then adding the microbial inoculum obtained in step b), and nutrient content, soluble carrier and microelement obtained in step c) chelate to obtain bio-fertilizer.