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280results about How to "Maintain catalytic activity" patented technology

Preparation method for functionalized graphene loaded noble metal nano-crystalline composite catalyst

The invention discloses a preparation method for a functionalized graphene loaded noble metal nano-crystalline composite catalyst, which synchronously realizes reduction of a noble metal precursor and graphite oxide to obtain the composite catalyst in a structure that grapheme with surface modified by sulfonic acid is uniformly loaded with noble metal nano-crystalline. The method comprises the following steps: 1, preparing the graphite oxide; 2, carrying out covalent modification on the graphite oxide by benzenesulfonic acid; and 3, synchronously reducing the noble metal precursor and the graphite oxide and stabilizing noble metal nano particles by utilizing a coordination effect between a sulfonic acid group and the noble metal. Meanwhile, the surface sulfonic acid group has the hydrophilcity so that the catalyst can be uniformly dispersed in a water solution. A result shows that the noble metal nano particles with narrow size distribution can be uniformly distributed on the surface of graphene to form the efficient catalyst which has good dispersion in the water solution. Catalytic reduction reaction of p-nitrophenol proves that the catalyst has a very excellent catalysis performance; the catalyst still keeps the previous activity after being recycled and reutilized for five times.
Owner:HENAN AGRICULTURAL UNIVERSITY

Method for regenerating and maintaining activity of ionic liquid catalyst and method for producing alkylate

The invention discloses a method for regenerating and maintaining the activity of an ionic liquid catalyst, and the method comprises the following step of adding hydrogen halide or halohydrocarbon in an acidic ionic liquid catalyst or alkylation reaction raw material during the alkylation reaction process, and the ionic liquid catalyst is used for catalyzing alkylation of C4 alkene and alkane. And the invention also provides a method for producing alkylate by using alkylation reaction, and the method comprises the following step of adding the hydrogen halide or the halohydrocarbon in the acidic ionic liquid catalyst or the alkylation reaction raw material during the alkylation reaction process, and the regeneration of the ionic liquid catalyst and the continuous production of the alkylateare realized by adding B acid lost during the alkylation reaction process of the ionic liquid catalyst. The invention can effectively prolong the service life of the acidic ionic liquid catalyst, andthe treatment capacity of the raw materials can reach more than 1000 times of consumption of the ionic liquid; and the method has no influence to the quality of the alkylate, is simple and convenientin operation, and has higher industrial practicability.
Owner:北京中实奥杰石油科技有限公司

Preparation method of catalyst for continuous production of succinic anhydride from hydrogenation of maleic anhydride

The invention provides a catalyst for continuously producing butanedioic anhydride by maleic anhydride hydrogenation. The catalyst is a nickel loaded catalyst prepared by an equivalent-volume impregnation method, wherein in the catalyst, the content of nickel is 13 to 20 weight percent, the content of accelerating agent is 1 to 7 weight percent, and a carrier is a composite oxide of SiO2 and Al2O3 or SiO2-Al2O3. A preparation method for the catalyst comprises the following steps: impregnating impregnation solution blended by ammonia water and active metal salt solution on a carrier subjected to baking pretreatment at a temperature between 400 and 800 DEG C by the equivalent-volume impregnation method to form the catalyst through drying, baking and reducing treatment. The catalyst is applied to continuously preparing the butanedioic anhydride by maleic anhydride hydrogenation on a fixed bed reactor, the conversion rate of maleic anhydride is more than or equal to 99.98 percent, and theselectivity of the butanedioic anhydride is more than or equal to 98.85 percent. The catalyst achieves the technical-scale continuous production of the butanedioic anhydride, and has the advantages of high activity, good selectivity, high yield (more than or equal to 98.83 percent) and long service life.
Owner:SHANXI UNIV

Synthetic process for amino aromatic hydrocarbon compound

The invention discloses a synthetic process for an amino aromatic hydrocarbon compound. The process comprises the following steps: pre-preparing reaction solutions -1 and -2 by using an aromatic hydrocarbon compound (I), concentrated sulphuric acid and concentrated nitric acid, respectively pumping the solutions in a micro reactor, heating to react, cooling the reaction liquid, and pos-treating to obtain a nitryl aromatic hydrocarbon compound (II); mixing the nitryl aromatic hydrocarbon compound (II), a catalyst and a solvent as a reaction solution -3; respectively pumping the reaction solution -3 and hydrogen into the micro reactor, heating to react, cooling the reaction liquid and post-treating to obtain the amino aromatic hydrocarbon compound (III). The process disclosed by the invention is less in use level of nitric acid, convenient to concentrate and apply waste acid; in the nitrification reaction process, the heat release is little, and the nitration product nitryl aromatic hydrocarbon compound (II) is quickly transferred. The reaction phenomenon is stable without intense heat release and even material punching of a common kettle nitration reaction, so that the safety of nitration reaction is improved; the process is easy to realize industrialization, simple to operate and high in industrial safety degree and meets the environmental requirements.
Owner:ANHUI SHENGYUAN CHEM

Method for treating chrome-containing wastewater by catalytic reduction of petaloid magnetic iron oxide/molybdenum sulfide composite

The invention relates to a method for treating chrome-containing wastewater by catalytic reduction of a petaloid magnetic iron oxide/molybdenum sulfide composite. The method comprises the following steps: weighing ferrous sulfate heptahydrate and sodium chlorate, dissolving in deionized water, stirring until the solution becomes light yellow, reacting in a high-pressure reaction kettle, carrying out centrifugal separation to obtain ferric oxide, drying, and pulverizing into powder; weighing the ferric oxide powder, molybdenum trisulphate dihydrate and thiocarbamide, dissolving in deionized water, stirring uniformly, transferring the mixture into a high-pressure reaction kettle, reacting, and carrying out centrifugal separation; cleaning with ethanol and deionized water; and drying to obtain the ferric oxide/molybdenum sulfide composite finished product, adding the finished product into hexavalent-chrome-containing wastewater with the initial concentration of 5-20 mg/L, stirring uniformly, irradiating with a metal halide lamp for more than 30 minutes, determining the hexavalent chrome concentration after treatment, and calculating the removal rate. The ferric oxide/molybdenum sulfide composite for treating hexavalent-chrome wastewater has the advantages of high removal rate and low treatment cost.
Owner:YANGZHOU UNIV

Synthesis process of dimido dipheny compound

The invention discloses a synthesis process of a dimido dipheny compound. The synthesis process disclosed by the invention comprises the following steps: by taking benzene(I) as a raw material, carrying out continuous nitration on a micro reactor platform to obtain a mixed nitrobenzene compound (II); then obtaining a mixed diaminobenzene compound (III) by carrying out catalytic hydrogenation reduction under a mild condition with temperature of 50~70 DEG C and hydrogen gas pressure not higher than 1.0MPa; and purifying to obtain o-phenylenediamine, p-phenylenediamine and m-phenylenediamine. The synthesis process disclosed by the invention has the benefits that: the use level of nitric acid is low, so that the waste acid is easy to concentrate and apply mechanically; the heat release is less, the product dinitrobenzene compound (II) is quickly transferred, the reaction phenomenon is stable without intense heat release and even punch of a common autoclave nitration reaction, so that the safety of nitration reaction is improved; the rate in nitrification reaction is fast, and the energy consumption is reduced; the reaction phenomenon is stable, so that the safety of catalytic hydrogenation reduction reaction is improved; the synthesis process is a new technique which is high in safety, easy to industrialize and less in environment protection.
Owner:ANHUI SHENGYUAN CHEM

Method for preparing polycarbonate catalyzed by ionic liquid

The invention relates to a method for preparing polycarbonate catalyzed by ionic liquid. The method is characterized in that heterocyclic nitrogen-containing ionic liquid is used as a catalyst, the amount of the catalyst is 5*10<-3>-5% of the mass of a dihydroxy compound, the dihydroxy compound and bis(trichloromethyl) carbonate are taken as raw materials, a feeding mol ratio of the dihydroxy compound to the bis(trichloromethyl) carbonate is 1:0.8-1:10, and the corresponding polycarbonate is obtained by melt polymerization. A synthesis process of the polycarbonate includes two stages of transesterification and polycondensation. In the transesterification stage, a prepolymer is obtained under conditions of a reaction temperature of 90-180 DEG C, an atmospheric pressure and reaction time of0.05-6 h. In the polycondensation stage, the polycarbonate is obtained by synthesizing prepolymer at 200-270 DEG C, a vacuum degree of 4.0*10<-3> MPa-1.0*10<-5> MPa, and reaction time of 0.05-7 h. Thesynthetic method has the advantages of simple catalyst components and molecular structure that can be designed. Moreover, the catalyst is strong in alkalinity and high in activity. By-products can berecycled, which reduces the cost. The synthetic method does not use highly toxic phosgene, dose not require a solvent, is very little in three wastes generation, and conforms to the concept of cleanproduction.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Polyacid-based metal organic framework crystal material and preparation method thereof

The invention provides a polyacid-based metal organic framework crystal material and a preparation method thereof and relates to a polyacid-based metal organic framework crystal material with nano porous channels. The invention aims at solving the problems that the polyacid-based metal organic framework material synthesized by adopting the prior art generally has a single porous channel, the finally obtained material does not have the porous channels after a polyacid molecule is immobilized, and therefore, the catalytic activity of the material is low. A chemical formula of the designed and developed flexible ligand assembled polyacid-based metal organic framework material with the nano porous channels is {[CuI(btpe)2][CuII2(H2O)2(btpe)2][BW12]40}}.2H2O. The preparation method comprises the following steps: dissolving borotungstic acid, copper acetate and 1,5-bis(triazole)-pentane into deionized water, regulating pH value, and then carrying out reaction for 3 days at the temperature of160 DEG C. By carrying out the preparation method provided by the invention, the flexible ligand assembled polyacid-based metal organic framework crystal material with the nano porous channels can beobtained.
Owner:HARBIN UNIV OF SCI & TECH

Amorphous non-precious metal hydroxide modified perovskite composite catalyst used for oxygen evolution reaction and preparation method thereof

The invention discloses an amorphous non-precious metal hydroxide modified perovskite composite catalyst used for oxygen evolution reaction and a preparation method thereof. The composite catalyst is composed of a main body material and a modification material, wherein the main body material is perovskite oxide and the modification material is amorphous non-precious metal hydroxide. The chemical composition of the amorphous non-precious metal hydroxide modification material is MxA1-x(OH)y, wherein M and A are selected from transition metal elements, x is no less than 0 and no more than 1, and y is no less than 2 and no more than 3. The main body material A-position ordered double perovskite oxide and has a molecular formula of Ln0.5Ba0.5CoO3-delta. The hydroxide modification material and the perovskite main body in the composite catalyst produce cooperative effect; the catalytic activity of the composite catalyst is greatly improved compared with catalytic activity of a main body catalyst; and after long-time electrochemical performance test, the composite catalyst can maintain catalytic activity and morphological stability.
Owner:NANJING UNIV OF AERONAUTICS & ASTRONAUTICS
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