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361 results about "Trichloroethane" patented technology

Trichloroethane can refer to either of two isomeric chemical compounds: 1,1,1-Trichloroethane 1,1,2-Trichloroethane

Diffusion method for solace cell with polycrystalline silicon selective emitter

The invention discloses a diffusion method for a solar cell with a polycrystalline silicon selective emitter. The diffusion method includes the following steps: firstly, placing a silicon chip on which a doping agent grows into a diffusion furnace and raising the temperature to 750-800DEG C, wherein the environment in the furnace is N2 with the flow being 10-30slm; secondly, after the temperature is stabilized, uniformly raising the temperature in each temperature zone in the furnace to 850-900DEG C, introducing 0.2-2slm of N2 carrying trichloroethane, 1-5slm of O2 and 10-30slm of N2 while raising the temperature so as to realize heavy doping and controlling the heavily-doped sheet resistance between 30 and 60 omega/m<2>; thirdly, reducing the temperature of each temperature zone to the diffusion temperature of 820-840DEG C and introducing N2 carrying POCl3 for diffusing; fourthly, reducing the temperature of each temperature zone to 780-800DEG C, stopping introducing the N2 carrying the POCl3 so as to realize shallow doping, wherein the propulsion time is 10-25minutes and controlling the shallow-doped sheet resistance between 70-120 omega/m<2>; and fifthly, cooling the silicon chip, taking out the silicon chip and finishing the diffusion process. According to the diffusion method disclosed by the invention, the diffusion of a doping agent is realized at high temperature and the heavy doping and shallow doping of the selective emitter are realized; and meanwhile, the gettering of a polycrystalline silicon is realized, so that the conversion efficiency is greatly increased.
Owner:CSI CELLS CO LTD +1

Recovery method and recovery device for sulfur dioxide in sucralose chlorination reaction

The invention relates to a recovery method for sulfur dioxide in sucralose chlorination reaction. The method includes steps: 1, adding concentrated sulfuric acid into a drying tower, removing moisturefrom tail gas of a gas-liquid separator, and allowing dried sulfur dioxide and trichloroethane tail gas to enter a primary condenser; 2, allowing residual tail gas and condensate flowing through theprimary condenser to enter a trichloroethane separation tank, allowing sulfur dioxide and trichloroethane condensate to enter a collection tank, and enabling tail gas sulfur dioxide to enter a secondary condenser; 3, enabling tail gas and sulfur dioxide condensate flowing through the secondary condenser to enter a tertiary condenser at a temperature ranging from -25 DEG C to -30 DEG C, condensinggaseous sulfur dioxide into liquid sulfur dioxide, and sending into a recovery storage tank. The recovery method has advantages that hydrogen chloride in the tail gas is subjected to three-stage waterabsorption to obtain high-concentration hydrochloric acid while sulfur dioxide and trichloroethane in the tail gas are separated out, and accordingly the product conversion rate is increased, raw material and energy consumption is reduced, and cost is saved to the maximum extent.
Owner:ANHUI JINGHE IND

A kind of method that takes dichloroethane as raw material to produce trichloroethylene and tetrachloroethylene

The invention relates to a method for preparing trichloroethylene and perchloroethylene from dichloroethane as a raw material. The existing method has the defects of difficult realization and large amount of investment. The method of the invention comprises the following steps that dichloroethane undergoes chlorination to produce a mixture of dichloroethane, trichloroethane, tetrachloroethane, pentachloroethane and hexachloroethane, and hydrogen chloride gas under a dichloroethane gaseous or liquid phase; the mixture is transferred into a rectifying tower to be rectified; a tetrachloroethane / pentachloroethane mixture fraction with a top temperature of 147 to 162 DEG C is collected; the collected tetrachloroethane / pentachloroethane mixture fraction is vaporized and then is fed into a fixedbed reactor to form a trichloroethylene / perchloroethylene gas mixture; the trichloroethylene / perchloroethylene gas mixture is condensed into a liquid mixture; the liquid mixture and hydroquinone are fed into a rectifying tower to be rectified; a fraction with a top temperature of 86 to 87.5 DEG C is collected to obtain trichloroethylene finished products; and a fraction with a top temperature of 120 to 121.5 DEG C is collected to obtain perchloroethylene finished products. The method has the advantages of simple process, good controllability, easy acquirement of raw materials, low cost and little or no process wastewater or waste residue.
Owner:内蒙古磐迅科技有限责任公司

Fiber/fabric/paper finishing liquid with effects of resisting mildew and repelling and killing mosquitoes as well as use method and product of fiber/fabric/paper finishing liquid

The invention relates to fiber/fabric/paper finishing liquid with the effects of resisting mildew and repelling and killing mosquitoes as well as a use method and a product of the fiber/fabric/paper finishing liquid. In the fiber/fabric/paper finishing liquid, an insecticide is water insecticide with the effective content of 0.1 to 99 percent or dichlorodiphenyl trichloroethane with various dosageforms and the effective content of 1 to 99 percent; a repellent is a water repellent with the effective content of 0.1 to 99.9 percent; an antibacterial agent is an inorganic, organic or natural antibacterial agent with various dosage forms and the effective content of 1 to 100 percent; an adhesive is a water adhesive with the solid content of 30 to 50 percent; a cross-linking agent is an epoxy polymer cross-linking agent, a methyl-etherified hexahydroxy methylmelamine resin early-shrinkage body cross-linking agent or the like. The use method of the fiber/fabric/paper finishing liquid, disclosed by the invention, can select one of a padding method, a spraying method or an impregnating method according to the difference of fabric/fiber materials. The fiber/fabric/paper finishing liquid andthe product thereof have the advantages of high efficacy, high adhesive force, washing resistance, low cost, good applicability, convenience in use and popularization and the like; the fiber/fabric/paper finishing liquid and the product thereof can reach the WTO standard.
Owner:张裕

Anaerobic biodegradation of unsaturated, saturated, aromatic and halogenated hydrocarbons

An apparatus and method for anaerobic biodegradation, bioremediation or bioprocessing of hydrocarbons dissolved in an aqueous matrix, such as wastewater, groundwater, or slurry. Dissolved alkanes (saturated hydrocarbons), alkenes (unsaturated hydrocarbons), aromatic hydrocarbons and/or halogenated hydrocarbons are metabolized or cometabolized. In one form, the invention involves introducing an aqueous stream comprising at least one dissolved aromatic hydrocarbon (such as benzene, toluene, ethylbenzene, o-xylene, m-xylene, p-xylene, phenol, o-cresol, m-cresol, or p-cresol) and a dissolved oxide of nitrogen [such as nitrate (NO3-), nitrite (NO2-), nitric oxide (NO) and nitrous oxide (N2O)] to a reactor, and operating said reactor under conditions that support denitrification of the aromatic hydrocarbon. Alternatively, the aqueous stream may comprise at least one alkane (such as ethane) and/or at least one alkene (such as ethene or ethylene) and biodegradation of these compounds is accomplished. In a preferred form, the aqueous stream also comprises at least one dissolved halogenated hydrocarbon (such as tetrachloroethylene, trichloroethylene, or 1,1,1-trichloroethane) and dehalogenation of the halogenated hydrocarbon is accomplished. The reactor may be a continuous stirred tank reactor, a batch (or sequencing batch) reactor, a plug-flow reactor, a fixed-film reactor, or a pore space in an underground aquifer in situ. The reactor is operated in such a way that molecular oxygen is excluded from the space or zone in which the biodegradation is occurring and the other requirements of denitrifying bacteria are met. In some implementations, kinetic control (control of mean cell residence time) is used to enrich a denitrifying culture in the reactor.
Owner:YESTECH

Preparation method of environment-friendly light-resistant and waterproof polyurethane coating and adhesive

The invention discloses a preparation method of an environment-friendly light-resistant and waterproof polyurethane coating and adhesive. The preparation method comprises the steps of mixing polytetramethylene ether glycol and isophorone diisocyanate in the existence of a dibutyltin dilaurate catalyst according to the NCO to OH molar ratio of 1.5:1 to 4.5:1, reacting at the temperature of 80-100 DEG C for 1-4h, adding lipidosome, and reacting at the temperature of 80 DEG C for 1h to obtain a polyurethane prepolymer A; adding a chain extender accounting for 1.2-3.2% of the weight of the prepolymer A and 1, 1, 2-trifluorotrichloroethane accounting for 12-25% of the weight of the prepolymer A into the prepolymer A, reacting at the temperature of 65-85 DEG C for 1.5-3.5h, adding a fluorine compound accounting for 0.5-1.2% of the weight of the prepolymer A, reacting at the temperature of 75-85 DEG C for 1-2h, adding triethylamine accounting for 10-15% of the weight of the prepolymer A to carry out neutral reaction for 30-50min, adding water to emulsify to obtain the environment-friendly light-resistant and waterproof polyurethane coating and adhesive. The prepared light-resistant polyurethane coating and adhesive is environment-friendly and low in price, can be widely applied to the surfaces of a wall, furniture and metal ware, and can be used as an adhesive for plastics, glass, papermaking and textiles.
Owner:广州富思德化工科技有限公司

Electrical equipment cleaning agent and preparation method thereof

The invention relates to an electrical equipment cleaning agent and a preparation method thereof. The electrical equipment cleaning agent comprises 1 to 5% of one or more alcohol ether solvents, 5 to 10% of dichloromethane, 30 to 50% of tetrachloroethylene, 0 to 10% of limonene and the balance one or more hydrocarbon solvents. The preparation method comprises the following steps of standing the one or more hydrocarbon solvents in a storage tank having the cone-shaped bottom for more than 24 hours, adding the one or more hydrocarbon solvents into a stainless steel reactor according to a certain ratio, orderly adding the one or more alcohol ether solvents, dichloromethane, tetrachloroethylene and limonene into the stainless steel reactor, stirring for 20 to 30 minutes, drying by a dryer and filtering by a filter to obtain the electrical equipment cleaning agent. The electrical equipment cleaning agent does not contain ozone depleting substance (ODS) raw materials of trifluorotrichloroethane (F-113), 1,1,1-trichloroethane, trichloroethylene and carbon tetrachloride, is safe and environmentally friendly, has an ozone destruction coefficient of 0.00, strong detergency of 99.9% and a strong capacity of removing mineral oil stains, soldering and dust, allows on-line cleaning, has withstand voltage more than 25KV and stable chemical properties, does not produce corrosion on circuit boards and metal materials, and can be volatilized fully without residual.
Owner:华阳新兴科技(天津)集团有限公司

Method for separating solvents after chlorination and neutralization reaction of sucralose

The invention relates to a method for separating solvents after a chlorination and neutralization reaction of sucralose. The method comprises the following steps: filtering a neutralized solution obtained after chlorination and neutralization, pumping the filtered neutralized solution into an extraction kettle, adding 10# industrial oil used as an extractant to extract the solvent trichloroethaneand DMF and make the solvents enter a supernatant, carrying out secondary reduced-pressure rectification on the supernatant, respectively separating the trichloroethane and DMF by using a boiling point difference, decolorizing high-boiling point industrial oil obtained after the secondary rectification with activated carbon to make the decolorized high-boiling point industrial oil directly reused,and directly reusing the trichloroethane and DMF obtained after the two-stage rectification in chlorination; and directly adding water to obtained lower oil to dissolve the lower oil, decolorizing and filtering the obtained solution, adding ethyl acetate, and performing freezing crystallization to obtain crude sucralose-6-acetate. The method has the advantages of simplicity, avoiding of the process of adding water to carry away the solvents during solvent recovery in traditional processes, reduction of the solvent recovery difficulty, improvement of the solvent recovery efficiency, energy consumption saving, great reduction of the production cost, and reduction of pollution.
Owner:ANHUI JINGHE IND

Catalyst for catalytic hydrodechlorination, and preparation method and application thereof

The invention discloses a catalyst for catalytic hydrodechlorination, and a preparation method and an application thereof. The catalyst for catalytic hydrodechlorination comprises an alloy catalyst, an auxiliary agent and a carrier, the alloy catalyst takes element Ru as a main body, and any one or more of specified alloy elements Re, Ti, Cr, Ni, Al, Co, Cu, Nb, Ta, Ru, Pt and Ag are selected to form an alloy with Ru; and the auxiliary agent is alkali metal or rare earth metal, and the carrier is an activated carbon carrier. The catalyst is simple in preparation method and convenient to operate, and has the advantages of low cost, high activity, high selectivity, good stability, mild reaction conditions and the like; the catalyst is applied to a reaction for preparing chlorotrifluoroethylene through catalytic hydrodechlorination of trichlorotrifluoroethane; and the catalyst is good in catalytic hydrodechlorination reaction temperature, instant in reaction at the temperature of 200-550DEG C, high in activity and high in chlorotrifluoroethylene selectivity, the activity of the catalyst reaches 85% or above, the maximum conversion rate of the catalyst reaches 95.7%, and the maximum selectivity of the catalyst reaches 95.6%.
Owner:ZHEJIANG UNIV OF TECH

Method for preparing vinyl chloride and coproducing dichloroethylene and 1,1,2-trichloroethane by acetylene-dichloromethane coupled reaction

ActiveCN104672054ASolve pollutionReaction process with low energy consumptionPreparation by halogen halide addition1,1,2-TrichloroethaneReaction temperature
The invention relates to a method for preparing vinyl chloride and coproducing dichloroethylene and 1,1,2-trichloroethane by acetylene-dichloromethane coupled reaction, which is characterized by comprising the following steps: mixing acetylene and dichloromethane, and simultaneously carrying out dichloromethane coupled reaction and acetylene hydrochlorination on the acetylene and dichloromethane in a catalyst-filled reactor under the action of the catalyst, wherein the mole ratio of the acetylene to the dichloromethane is 0.5-2.5, the reaction temperature is 200-400 DEG C, the volumetric space velocity of the acetylene-dichloromethane gas mixture is 10-500 h<-1>, and the dichloromethane coupled reaction generates dichloroethylene, 1,1,2-trichloroethane and chlorine hydride; and further carrying out acetylene hydrochlorination on the generated chlorine hydride and acetylene to generate vinyl chloride. The method can simultaneously coproduce the dichloroethylene, 1,1,2-trichloroethane and other high-added-value products while producing vinyl chloride, and the process is more economical and has wider industrialization prospects.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI +1

Headspace-gas chromatography/mass spectrometry (HS-GC/MS) measurement method of eleven types of volatile harmful substances in student supplies

The invention relates to a headspace-gas chromatography/mass spectrometry (HS-GC/MS) measurement method of eleven types of volatile harmful substances in student supplies, and belongs to the technicalfield of detection and risk assessment of the harmful substances in the student supplies. The HSGC-MS selection ion quantitative measurement method is established so as to measure the eleven types ofvolatile harmful substances such as 1,1-dichloroethane, trichloromethane, 1,1,1-trichloroethane, cyclohexane, carbon tetrachloride, benzene, methyl cyclohexane, toluene and xylene in the student supplies. After a sample is subjected to headspace at 70 DEG C for 30 min, toluene -d8 serves as the internal standard, then gas in a headspace sample injector is directly injected to a GC/MS system, andthe volatile harmful substances in the student supplies are qualitatively and quantitatively analyzed through the headspace sample injector and a gas chromatography-mass spectrometer. According to themethod, the detection limit is 0.02-0.18 mg/kg, the quantitative limit is 0.07-0.60 mg/kg, the standard recovery rate is 93.33-105.8%, and the relative standard deviation is smaller than 10%. The tedious step of solvent extraction is avoided, by selecting ion detection quantification, interference factors are few, operation is easy, and sensitivity and repeatability are good.
Owner:SHANDONG INST FOR PROD QUALITY INSPECTION

Method for removing pesticide residue and heavy metal residue out of lentinan by using resin adsorption method

The invention relates to the technical field of environmental protection, and particularly relates to a method for removing pesticide residue and heavy metal residue out of lentinan by using a resin adsorption method. The method is characterized in that a process route is as follows: mushroom selection, cleaning, extraction, passing through a resin column, filtration, concentration, alcohol precipitation, recovery of ethanol, spray drying of precipitate, mixing and sub-packaging; the technical data of final products are as follows: moisture is less than or equal to 5.0%, polysaccharide content is more than or equal to 50.0%, lead is less than or equal to 0.1ppm, cadmium is less than or equal to 0.1ppm, and mercury is less than or equal to 0.1ppm; pesticide residues: hexachloro-cyclohexane soprocide is less than or equal to 0.01ppm, quintozene is less than or equal to 0.01ppm, Dichlorodiphenyl Trichloroethane is less than or equal to 0.01ppm, ash content is less than or equal to 4.0%, and mesh number is more than or equal to 100; microbiological indicators: total bacterial count is less than or equal to 1000/g, saccharomycetes are less than or equal to 50/g, mildew is less than or equal to 50/g, and pathogenic bacteria cannot be detected. The resin column uses HPD500 type adsorption resin. The spray drying temperatures are as follows: the inlet temperature is 205 DEG C, and the outlet temperature is 80 DEG C. By adopting the adsorption resin for removing harmful ingredients out of mushroom, the polysaccharide content is increased, the color, aroma and taste of the mushroom cannot be destroyed, and the product quality of polysaccharides is improved.
Owner:FUSHUN HAOYUAN BIOLOGICAL SCI & TECH CO LTD
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