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723results about How to "Reduce the discharge of three wastes" patented technology

Method for producing caprolactam by taking high-purity benzene as raw material

The invention provides a method for producing caprolactam by taking high-purity benzene as a raw material, and the method comprises the following steps of: A. preparing cyclohexene from the raw material benzene through hydrogenation; B. separating and purifying cyclohexene; C. carrying out hydration on the cyclohexene for preparing cyclohexanol; D. separating and purifying cyclohexanol; E. carrying out dehydrogenation on cyclohexanol for preparaing cyclohexanone; F. refining cyclohexanone; G. carrying out oximation on cyclohexanone so as to prepare cyclohexanone-oxime; H. refining cyclohexanone-oxime; I. carrying out rearrangement on refined cyclohexanone-oxime so as to prepare caprolactam; and J. refining caprolactam, wherein the high-purity benzene is adopted as a raw material, so that the purity of benzene is more than 99.95%, the sulphur content is less than 5ppm, and the methylbenzene is not more than 100ppm. The method has the beneficial effects that the high-purity benzene is adopted as a raw material, so that the impurity is less, and the product quality is high; the raw material is high in comprehensive utilization rate and low in hydrogen consumption; and the mass of the raw material and intermediate products generated in all the steps of reaction can be strictly controlled, so that the direct commercial value of the intermediate products is fully exerted, and the optimal quality of the product caprolactam can be reached.
Owner:CHINA TIANCHEN ENG +3

Novel continuous nitrification denitrating, abstraction, hydrogenation reduction production process for H acid

The present invention relates to a novel technology of continuous nitration and denitration, extraction, hydrogenation and reduction of H acid, and belongs to the technical field of H acid production. In the novel technology, H acid is prepared with liquid naphthalene through sulfonation, continuous nitration and denitration, extraction, hydrogenation and reduction, concentration, alkali fusion and separation of the H acid. The present invention not only solves the problems in the traditional technological process that the steps are more, the process is complex, the labor intensity of workers is high, the yield rate of the H acid is low and the pollution of wastewater is serious, but also eliminates the factors that the slightly inaccurate control over the reaction temperature and time of nitration and denitration can easily cause explosive polynitro compounds and thus hidden danger of security. The present invention has the advantages that the process is shortened, the byproducts are fewer, and the labor intensity is reduced. The continuous nitration and denitration has the advantages that the occupied area is small, the production capacity is high, the energy consumption is low, the yield rate is improved by 8 percent compared with the traditional process, about 1 ton of sulphuric acid is saves in production of one ton of the product, and the wastewater discharge is reduced. No iron ions are contained in the materials, the product quality of the H acid is improved, and the workshop production environment is obviously better.
Owner:CHUYUAN HIGH NEW TECH GRP

Method for comprehensively recovering copper and indium from lead matte

The invention discloses a method for comprehensively recovering copper and indium from lead matte. The method comprises the following steps: A, crushing lead matte block materials and then ball-milling to obtain lead matte powder; B, leaching the lead matte powder obtained by ball-milling in an autoclave by using sulfuric acid and continuously introducing oxygen in the leaching process; C, after leaching, carrying out solid-liquid separation to obtain leaching residues and leachates containing copper ions and indium ions; D, selectively extracting the copper ions in the leachates by using ZJ988, obtaining copper sulfate enrichment liquid by using a sulfuric acid-copper sulfate solution to perform reverse extraction on loaded organic phase, taking the copper sulfate enrichment liquid as an electrolyte of electro-deposit copper and obtaining cathode copper through a copper sulfate electro-deposition process; E, selectively extracting the indium ions by using P204, then obtaining indium chloride enrichment liquid by using a hydrochloric acid solution to perform reverse extraction on the loaded organic phase and replacing the indium chloride enrichment liquid by using a zinc plate or an aluminum plate to obtain sponge indium. The method has the benefits that the complete separation of the copper from the indium in the lead matte is realized, recovery rate of the valuable metal is high, and the environmental friendliness is realized.
Owner:YUNNAN COPPER CO LTD +1

Method for preparing pure acrylate copolymer coating emulsion for building external wall elastic coating

The invention discloses a method for preparing a pure acrylate copolymer coating emulsion for a building external wall elastic coating, including a preparation method of a seed emulsion, a pure acrylate type elastic emulsion prepared from the seed emulsion and a preparation method thereof, as well as an elastic coating prepared from the elastic emulsion added with auxiliaries, a filler and the like, wherein the ratio (by wt) of comonomers St:MMA:BMA:BA of the copolymer of the seed emulsion is (32-42):(18-27):(18-27):(12-22); the hansch constant of the polymer of the seed emulsion is 3.00-3.81 pKa; and the elastic emulsion is obtained through seed polymerization of a monomer mixture which is composed of acrylic acid (AA), acrylamide (AM), butyl acrylate (BA), methyl methacrylate (MMA) and n-butyl methacrylate (BMA) in a monomer ratio (wt) of (0.8-5):(0.8-5):(25-45):(7-33):(7-33). As the elastic coating prepared from the pure acrylate type elastic emulsion prepared by the method provided by the invention is obviously improved in properties such as stain resistance, weather fastness, low-temperature elasticity, adhesiveness, water tolerance and the like, the elastic coating can be used as an external wall decorative coating high in requirement for durability and thus can be widely applied to the field of building coating.
Owner:HENGSHUI XINGUANG CHEM

Method for preparing polyol by using bio-oil and application

The invention discloses a method for preparing polyol by using bio-oil. The method comprises the following steps: firstly performing methyl esterification, namely, performing ester exchange on biolipid and methanol under the catalysis of potassium fluoride loaded magnesium oxide solid alkali, converting the obtained product into fatty acid methyl ester with small molecular weight and byproduct glycerol, filtering to recycle the catalyst, and separating lower-layer glycerol; performing epoxidation on upper-layer fatty acid methyl ester in 30% of hydrogen peroxide under the catalysis of ionic liquid so as to form epoxidized fatty acid methyl ester.; then adding the glycerol in the methyl esterification process, continuously performing alkoxide ring-opening under the catalysis of ionic liquid, introducing hydroxyl, and finally separating liquid to recycle the ionic liquid catalyst, reducing pressure and distilling the upper-layer to remove water so as to obtain low-viscosity bio-oil-based polyol. The raw material is easily available, recyclable and good in biodegradability, the preparation process is environmental friendly, the industrial three-waste emission is small, the product structure and a hydroxyl value are adjustable, the application range is wide, and the environment influence level is low.
Owner:ZHEJIANG HENGFENG NEW MATERIAL

Chemical recovery method for waste polycarbonate material in ionic liquid surrounding

The invention relates to a novel method for generating bisphenol A and dialkyl carbonate by chemical degradation of waste polycarbonate (PC) to realize chemical recycling of the bisphenol A and the dialkyl carbonate. The method is characterized in that reusable ionic liquid such as chloridized 1-allyl-3-methylimidazole and bromized 1-butyl-3-methylimidazole is taken as a reaction medium and catalyst, and subjected to hydrolysis reaction or alcoholysis reaction at a temperature of between 60 and 170 DEG C; after reaction is over, bisphenol A products are obtained after extraction, distillation and other operations (as for alcoholysis reaction, the dialkyl carbonate is obtained simultaneously); reclaimed ionic liquid is directly reused without any treatment; and the yield of the bisphenol A is more than 93 percent. Compared with the prior art, the method has the characteristics that: firstly, the method overcomes the defects in the prior art that high-concentration inorganic strong acid/strong alkali is applied and can not be recycled; and secondly, due to adoption of the ionic liquid which has certain solubility on the PC as the reaction medium and the catalyst, the method relieves the reaction conditions on one hand and can realize reutilization of the ionic liquid on the other hand, and obviously solves the problems of equipment corrosion and environmental pollution.
Owner:QINGDAO UNIV OF SCI & TECH

Method and device for treating dichlorosilane waste by utilizing reactive distillation

The invention relates to a method and a device for treating dichlorosilane waste by utilizing reactive distillation. A reactive distillation tower is divided to three segments, namely a distillation segment, a reaction segment and a stripping segment, wherein a tower top condenser is arranged on the top of the reactive distillation tower; a tower bottom reboiler is arranged at the bottom of the reactive distillation tower; a cooler is arranged at the bottom of the reactive distillation tower; an inlet of the cooler is connected with a tower bottom material outlet through a pipeline; an outlet of the cooler is connected with an inlet of a low-temperature cooler; and an outlet of the low-temperature cooler is connected to the reactive distillation tower through a pipeline. Raw materials silicon tetrachloride and dichlorosilane respectively enter the reactive distillation tower from the top and the bottom of the reaction segment to generate a disproportionated reaction in the reaction segment so as to produce trichlorosilane, and the trichlorosilane is continuously moved out of the reaction segment under the action of distillation separation; and the silicon tetrachloride in the materials of the tower returns back to the reactive distillation tower through external circulation from the top of the reaction segment so as to further react, and therefore the conversion rate of the reaction can be improved. The conversion rate of the dichlorosilane can achieve 98.50% and the purity of the trichlorosilane in the materials on the top of the tower can achieve 98.48%.
Owner:TIANJIN UNIV

Method and equipment for producing C4-C6 diacid low-carbon alcohol ester

The invention belongs to the chemical field, in particular to method and equipment for producing C1-C2 low-carbon alcohol ester of C4-C6 diacid. The method is characterized by comprising the following steps of: adding a catalytic agent, C4-C6 diacid and C1-C2 alcohol to a dispensing kettle, stirring and heating to enable the solid diacid to be dissolved; and then continuously delivering feed liquid to an esterification reactor to carry out esterification reaction under the conditions of a certain pressure, a certain reaction temperature and the like; continuously delivering an obtained esterification reaction mixture to a flash evaporator for flash evaporation; separating out unreacted alcohol and generated water from the upper part of the flash evaporator; discharging the product ester and unreacted raw material acid from the lower part of the flash evaporator; and then rectifying to obtain the C1-C2 alcohol ester of the C4-C6 diacid. The invention has the characteristics of low energy consumption and continuous esterification production, and aims to solve the problems existing in the aspects of long time, high energy consumption and the like in the esterification reaction for traditionally producing the C1-C2 low-carbon alcohol ester.
Owner:SHENYANG POLYTECHNIC UNIV

Co-production method for methyl benzoic acid and phthalic acid

The invention discloses a co-production method for methyl benzoic acid and phthalic acid. The co-production method comprises the following steps: (1) continuously introducing fresh dimethylbenzene, a catalyst and oxygen-containing gas into a primary oxidation reactor for a reaction to obtain a primary oxidation reaction solution containing methyl benzoic acid and an eight-carbon oxygen-contained compound; (2) carrying out continuous cooling, crystallization and filtration on the primary oxidation reaction solution to obtain filter liquor and filter cake, circulating 1-98% of the filter liquor back the primary oxidation reactor continuously, and continuous rectifying the filter cake continuously, to obtain a low-boiling point front cut fraction, distillation raffinate and a methyl benzoic acid product separately; (3) adding the remaining filter liquor in the step (2) and the obtained front cut fraction and distillation raffinate in the step (2) into a secondary oxidation reactor continuously, and meanwhile continuously introducing a Co/Mn/Br catalyst, acetic acid and oxygen-containing gas into the secondary oxidation reactor for an oxidation reaction to obtain a secondary oxidation reaction mixture; and (4) continuously cooling, crystallizing and filtrating the secondary oxidation reaction mixture to obtain a filter liquor and a phthalic acid product. The co-production method has advantages of a simple process, a low cost, a high yield, good selectivity, good economic benefits, and environmental protection.
Owner:山东友道化学有限公司

Novel method for preparing battery grade lithium carbonate by using tantalum niobium tailings lithium mica

The invention provides a novel method for preparing battery grade lithium carbonate by using tantalum niobium tailings lithium mica. The method is characterized by comprising the following steps of: crushing lithium mica powder until granularity is 100 to 200 meshes, adding the crushed lithium mica powder and 30 to 70 percent sulfuric acid solution in a solid and liquid mass ratio of 1:(2-8) into a reaction device, reacting at the temperature of between 60 and 200 DEG C for 3 to 10 hours to obtain the sulfuric acid solution which contains Li<+>, and separating to remove fluorine-containing solution; performing filtering separation on the sulfuric acid solution which contains the Li<+>, and fully washing the filter residue with water to remove the filter residue and obtain filtrate which serves as mother liquor 1; changing the temperature of the mother liquor to be between 10 and 100 DEG C with stirring, separating solids, namely rubidium, caesium and alum, performing filtering separation, washing the filter residue, and recovering the filtrate as mother liquor 2; adding calcium hydroxide into the mother liquor 2, and controlling the pH value of the solution to between 2 and 7 to obtain solid and liquid mixed solution of neutralization reaction; performing filtering separation on the solid and liquid mixed solution, washing and filtering the filter residue, and recovering the filtrate as mother liquor 3; performing evaporation concentration on the mother liquor 3, controlling the concentration of the Li<+> in the solution to be between 40 and 65g/l, and filtering to obtain the filtrate serving as mother liquor 4; and blowing carbon dioxide into the mother liquor 4 at the temperature of between 95 and 105 DEG C under 2 atmospheres and performing lithium-sinking reaction for 40 to 100 minutes, filtering and mechanically separating to obtain lithium carbonate, washing with water, and drying to obtain the battery grade lithium carbonate product.
Owner:宜春银锂新能源有限责任公司

Production method of N-phosphono methyliminodiacetic acid

The invention discloses a method for manufacturing N-phosphonomethyliminodiacetic acid (PMIDA). The method comprises the following steps: (1) IDA disodium salt source is reacted with sulphuric acid to obtain IDA monosodium salt solution; (2) the IDA monosodium salt solution is then reacted with sulphuric acid to separate out iminodiacetic acid (IDA), and reaction mother liquor is treated by liquid alkali to obtain Na2SO4 after evaporated dehydration; moreover, the mother liquor is treated as the raw material of the step (2); (3) the IDA is mixed with phosphorous acid and formaldehyde to generate PMIDA through reaction under the condition of sulphuric acid, wherein the PMIDA is obtained through cooling crystallization and filtration after formaldehyde-containing waste water is separated through evaporation; the mother liquor is treated as the raw material of PMIDA; the formaldehyde-containing waste water separates concentrated and reclaimed concentrated formaldehyde through a pervaporation membrane separating device, and the separated concentrated formaldehyde is treated as formaldehyde raw material; and discharged water is used for reclaimed water recovery after resin treatment. The invention reclaims the byproduct of Na2SO4 and makes effective use of resources such as PMIDA, IDA, formaldehyde, sulphuric acid and water in the production waste water of PMIDA.
Owner:捷马化工股份有限公司

Enzyme engineering method for producing gamma-aminobutyric acid

The invention discloses an enzyme engineering method for producing gamma-aminobutyric acid, belonging to the technical field of a fermentation method for producing enzymes. The method disclosed by the invention comprises the following steps of: inducing by using lactose as an inducer for producing enzymes, filtering through a ceramic film for collecting thalli, and washing the thalli instantly; then, adding an acetic acid-sodium acetate buffer solution into the thalli, and adding a small amount of substrate glutamic acid many times to enable the glutamic acid to be converted into gamma-aminobutyric acid; then, filtering and removing the thalli instantly by adopting the ceramic film, and decoloring by adopting a rolled organic film; and finally, carrying out triple-effect concentration, stopping concentrating until the content of the concentrated product reaches 550-600g / L, pouring the concentrated solution into a vacuum concentration crystallizing tank, continuing to concentrate, stopping heating until the content of the product reaches 700-900g / L, and naturally cooling and growing the grain for 1-1.5 hours under the normal pressure to obtain a columnar or powdered crystal. The purity of the crystal obtained by primary crystallization is greater than or equal to 99.0%, and the yield of the crystal is greater than or equal to 85%. The method disclosed by the invention is a clean production process and has low emission of the three wastes, and the residues of the thalli can be used as feed proteins.
Owner:山东恩贝生物工程有限公司
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