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49results about How to "Reaction process cleaning" patented technology

Method for preparing benzaldehyde by catalytically oxidizing phenylcarbinol through Pt/BiOCl-metal oxide serving as catalyst

ActiveCN107042108AThe type of carrier can be controlledHigh selectivityCatalyst carriersOrganic compound preparationBenzaldehydeManganese
The invention discloses a method for preparing benzaldehyde by catalytically oxidizing phenylcarbinol through Pt/BiOCl-metal oxide serving as a catalyst. The method comprises the following steps: by taking a noble metal Pt/BiOCl-metal oxide compound system as the catalyst, dispersing phenylcarbinol and the catalyst into water, and continuously stirring under a relatively low-temperature dark condition for 3 to 10 hours, wherein the generation selectivity of the benzaldehyde can be 99 percent or above, and the yield of the benzaldehyde is retained within a range of 80 to 100 percent according to different types of carriers. The method has the following active effects that 1, the reaction can be carried out at relatively low temperature, such as room temperature of 25 DEG C; 2, low-cost air is used as an oxidant, so that the problem of environmental pollution caused by the fact that a high-cost metal such as chromium and manganese is used as the oxidant is solved; 3, no alkaline substances serving as an auxiliary catalyst are added into a reaction system; 4, basically no side effect is caused in a reaction process, and the generation selectivity of the benzaldehyde is retained at 99 percent or above; 5, equipment devices for reaction and an operation process are simple.
Owner:广西鲁桥新材料有限公司

Electrochemical preparation method of uniform and compact cuprous iodide semiconductor film

The invention discloses an electrochemical preparation method of a uniform and compact cuprous iodide semiconductor film, which comprises the following steps: 1) washing ITO conductive glass or silicon wafers with acetone 2 to 3 times, cleaning the ITO conductive glass or the silicon wafers in an ultrasonic cleaning machine with deionized water, then activating the ITO conductive glass or the silicon wafers in 10% of nitric acid solution, and finally washing with deionized water repeatedly; 2) mixing 0.002-2mol/L of Cu (NO3) 2, 0.002-2mol/L of KI, 3.4 x 10<-6>-1.7 x 10<-3>mol/L of K30 polyvinylpyrrolidone, and adjusting the pH value to 1 to 5 with 2mol/L of HNO3 or 0.1mol/L of NaOH solution to obtain electrolyte; and 3) taking the ITO conductive glass or the silicon wafers as a working electrode, taking a platinum sheet electrode as a counter electrode, and taking a saturated calomel electrode as a reference electrode to obtain the compact cuprous iodide semiconductor film by eletrodeposition, wherein the eletrodeposition voltage of the relative saturated calomel electrode is 0.1-0.4V, the eletrodeposition time is 1-30 minutes, and the electrodeposition temperature is 25-80 DEG C. The invention has the advantages of simple equipment, low cost, low reaction condition requirements and the like.
Owner:ZHEJIANG UNIV

Method for efficiently preparing benzaldehyde by using air as oxidation agent to catalyze benzyl alcohol in alkali-free water phase system at room temperature

The invention discloses a method for efficiently preparing benzaldehyde by using air as an oxidation agent to catalyze benzyl alcohol in an alkali-free water phase system at room temperature. According to the method, a precious metal Pt / metal oxide (zinc oxide, titanium oxide or reduced bismuth oxide) composite system is used as a catalyst, and the benzyl alcohol and the catalyst are dispersed into water and are then continuously stirred for 5-10h at low temperature in a dark place; the generation selectivity of the benzaldehyde can reach 99% or above, and the yield of the benzaldehyde is maintained within a range of 75-100% with the different types of carriers. The method has the positive effects that 1, a reaction can be carried out at the lower temperature such as room temperature 25 DEG C; 2, the cheap air is taken as the oxidation agent, so that the problem of environmental pollution caused by high valence metal such as chromium and manganese which are used as oxidation agents can be solved; 3, alkaline substances are not added into the reaction system as catalyst promoters; 4, the reaction process is basically free from a side reaction, and the generation selectivity of the benzaldehyde is maintained to be 99% or above; 5, equipment and operation technology of the reaction are simple.
Owner:浙江知多多网络科技有限公司

Process for one-step synthesis of methyl ethyl carbonate and co-production of ethylene glycol by using ethylene oxide

The invention discloses a process for one-step synthesis of methyl ethyl carbonate and co-production of ethylene glycol by using ethylene oxide, and relates to the process of synthesizing the methyl ethyl carbonate. According to the process, azeotropic separation is carried out while reaction rectification is carried out, and extraction and separation are carried out on a product without a solvent, so that the technological process of a conventional synthesis process of the methyl ethyl carbonate is greatly simplified, meanwhile multiple components can be separated at one time, and the separation purity is high. The selectivity of the methyl ethyl carbonate in the crude product obtained by the reaction can be up to 70%. The by-products, dimethyl carbonate and diethyl carbonate, can be directly separated out as products, and can be recycled for continued reaction for generating the methyl ethyl carbonate; and the by-product ethylene glycol can be separated out through simple distillation as a bulk raw material. The whole reaction process is clean, efficient and free of pollution, and no waste is generated. The optimal temperature for separating ethylene glycol by using a T4 ethyleneglycol batch rectifying tower is 140-155 DEG C, and the ethylene glycol content can reach 96% or above under the condition.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Method for synthesizing para aminophenylmethylether by catalytic hydrogenation of paranitroanisole

The invention provides a method for synthesizing para aminophenylmethylether by catalytic hydrogenation paranitroanisole. In the method, the paranitroanisole is subjected to catalytic reduction reaction with hydrogen to generate the para aminophenylmethylether in the presence of a load type palladium catalyst in a supercritical carbon dioxide reaction medium under mild conditions. Compared with the traditional processes, such as a nitrobenzene method, a sodium sulfide or ferrum reduction method, a method for synthesizing the para aminophenylmethylether by reducing the paranitroanisole by activated carbon load type palladium catalyst hydrazine hydrate, and the like, the invention has the advantages of mild reaction condition, fast reaction, clean reaction process and easy product separation, achieving the product yield more than 99 percent, and the like; in addition, in the invention, reaction temperature is reduced from 75-125 DEG C in the nitrobenzene method to 50-80 DEG C, and reaction time is reduced from 130 minutes in the method for synthesizing the para aminophenylmethylether by reducing the paranitroanisole by the activated carbon load type palladium catalyst hydrazine hydrate to 10-30 minutes without adding any organic solvent and additive or generating any side products in the reaction process.
Owner:CHANGCHUN UNIV OF TECH

Method for synthesis of symmetrical carbonate and co-production of 1,2-propylene glycol

The invention discloses a method for synthesis of symmetrical carbonate and co-production of 1,2-propylene glycol, and relates to the method for synthesizing the symmetrical carbonate. According to the method provided by the invention, a high-efficiency basic catalyst with a composite pore structure is used for one-step synthesis of the symmetrical carbonate by using propylene carbonate and various alcohols (ROH, wherein the R can be selected from various alcohols such as straight-chain alcohols, iso-alcohols, aromatic alcohols, phenols, diols such as ethylene glycol and diethylene glycol, polyols, and the like). The obtained crude product obtained by a reaction only contains the symmetrical carbonate and the 1,2-propylene glycol, wherein the conversion rate of the propylene carbonate canbe up to 95%. The by-product 1,2-propylene glycol can be separated out through simple distillation as a bulk raw material. The whole reaction process is clean, efficient and free of pollution, and nowaste is generated. When the molar ratio of the propylene carbonate to the various alcohols is 1:3, the reaction pressure is 5 MPa, the reaction temperature is 100 DEG C, and the space velocity is 5 h<-1>, the catalyst is not deactivated and has good stability after being used for 5000 hours.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Method for synthesizing ethyl methyl carbonate in one-step and co-producing ethylene glycol from ethylene oxide

The invention discloses a method for synthesizing ethyl methyl carbonate in one step and co-producing ethylene glycol from ethylene oxide, and relates to methods for synthesizing ethyl methyl carbonate. The method is characterized in that a high-efficiency alkaline catalyst with a composite pore structure is used for one-step synthesis of ethyl methyl carbonate from ethylene oxide, carbon dioxide,methanol and ethanol. The obtained crude product of the reation contains dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate and ethylene glycol, wherein the selectivity of methyl ethyl carbonate can reach up to 70% at maximum, byproducts of dimethyl carbonate and diethyl carbonate can be directly isolated as products, or can be recycled to react continuously to form ethyl methyl carbonate, and the byproduct ethylene glycol as a bulk raw material can be separated through simple distillation. The entire reaction process is clean, efficient, non-polluting and free of generating any waste. When the molar ratio of ethylene oxide: carbon dioxide: methanol: ethanol is 1:1:3:2, the reaction pressure is 5 MPa, the reaction temperature is 100 DEG C, and the space velocity is 5 h<-1>, thecatalyst does not lose activity after being used for 5000 h, and the stability is better.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Process for synthesizing ethyl methyl carbonate in one step and co-producing ethylene glycol

The invention discloses a process for synthesizing ethyl methyl carbonate in one step and co-producing ethylene glycol, and relates to manufacturing processes of preparing ethyl methyl carbonate. Theprocess is characterized in that ethyl methyl carbonate, diethyl carbonate and ethylene glycol are directly synthesized in one step under the catalysis of a multifunctional composite alkaline materialcatalyst; when reactive distillation is carried out, azeotropic separation is carried out simultaneously, and no solvent is needed to perform extraction separation on the products, so that technicalprocess of conventional ethyl methyl carbonate synthesis is greatly simplified, meanwhile, multiple components can be separated at one time, and the separation purity is high. The selectivity of methyl ethyl carbonate in the obtained crude product of the reaction can reach up to 70% at maximum, byproducts of dimethyl carbonate and diethyl carbonate can be directly isolated as products, or can be recycled to react continuously to form ethyl methyl carbonate, and the byproduct ethylene glycol as a bulk raw material can be separated through simple distillation. The entire reaction process is clean, efficient, non-polluting and free of generating any waste.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Method for one-step synthesis of ethyl methyl carbonate from propylene oxide and co-production of 1,2-propanediol

The invention relates to a method for synthesizing ethyl methyl carbonate, and concretely relates to a method for one-step synthesis of ethyl methyl carbonate from propylene oxide and co-production of1,2-propanediol. An efficient alkaline catalyst having a compopsite pore structure is used in the one-step reaction of the propylene oxide, carbon dioxide, methanol and ethanol for synthesizing the ethyl methyl carbonate. A crude product obtained through the reaction contains dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate and 1,2-propanediol, wherein the ethyl methyl carbonate selectivity reaches up to 70%. Byproducts dimethyl carbonate and diethyl carbonate can be directly separated as products, also can be recycled, and are continuously reacted to generate the ethyl methyl carbonate, and the product 1,2-propanediol can be separated through simple distillation as a popular raw material. The method has the advantages of cleanness, high efficiency, no pollution and no wastesin the whole reaction process. The catalyst is not inactive after being used at a molar ratio of the propylene oxide to the carbon dioxide to the methanol to the ethanol of 1:1:3:2 under a reaction pressure of 5 MPa at a reaction temperature of 100 DEG C under an air speed of 5 h<-1> for 5000 h, and has a good stability.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Pt/biocl-metal oxide is used as catalyst to prepare the method of benzaldehyde by catalytic oxidation of benzyl alcohol

The invention discloses a method for preparing benzaldehyde by catalytically oxidizing phenylcarbinol through Pt / BiOCl-metal oxide serving as a catalyst. The method comprises the following steps: by taking a noble metal Pt / BiOCl-metal oxide compound system as the catalyst, dispersing phenylcarbinol and the catalyst into water, and continuously stirring under a relatively low-temperature dark condition for 3 to 10 hours, wherein the generation selectivity of the benzaldehyde can be 99 percent or above, and the yield of the benzaldehyde is retained within a range of 80 to 100 percent according to different types of carriers. The method has the following active effects that 1, the reaction can be carried out at relatively low temperature, such as room temperature of 25 DEG C; 2, low-cost air is used as an oxidant, so that the problem of environmental pollution caused by the fact that a high-cost metal such as chromium and manganese is used as the oxidant is solved; 3, no alkaline substances serving as an auxiliary catalyst are added into a reaction system; 4, basically no side effect is caused in a reaction process, and the generation selectivity of the benzaldehyde is retained at 99 percent or above; 5, equipment devices for reaction and an operation process are simple.
Owner:广西鲁桥新材料有限公司

Method for one-step synthesis of carbonic acid symmetric ester and co-production of 1,2-propanediol through propylene oxide

The invention relates to a method for one-step synthesis of a carbonic acid symmetric ester and co-production of 1,2-propanediol through propylene oxide, and relates to a method for synthesizing a carbonic acid symmetric ester. According to the present invention, the method is used for one-step synthesis of carbonic acid symmetric esters through propylene oxide, carbon dioxide and various alcohols(ROH can be a linear alcohol, an isomeric alcohol, an aromatic alcohol, a phenol, a diol such as 1,2-propylene glycol and diethylene glycol, polyol and various alcohols), the crude products obtainedthrough the reaction contain only the carbonic acid symmetric ester and the 1,2-propanediol, the selectivity of the carbonic acid symmetric ester can be up to 95%, and the by-product 1,2-propanediol as the bulk material can be separated through simple distillation, such that the whole reaction process is clean, efficient and non-polluting, and does not produce any waste; and the catalyst is not deactivated for 5000 h at the reaction temperature of 100 DEG C under the reaction pressure of 5 MPa at the space velocity of 5 h<-1> according to the molar ratio of propylene oxide to carbon dioxide tovarious alcohols of 1:1:3 so as to achieve good stability.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

Method of one-step synthesis of asymmetric carbonate and co-production of 1,2-propylene glycol by using propylene oxide

The invention discloses a method of one-step synthesis of asymmetric carbonate and co-production of 1,2-propylene glycol by using propylene oxide, and relates to the method for synthesizing the asymmetric carbonate. A high-efficiency neutral catalyst with a composite pore structure is used for the one-step synthesis of the asymmetric carbonate by using the propylene oxide, carbon dioxide, methanoland various alcohols. The selectivity of the asymmetric carbonate in the crude product obtained by a reaction can be up to 70%. The by-products, dimethyl carbonate and dialkyl carbonates can be directly separated out as products, and can be recycled for continued reaction for generating the asymmetric carbonate; and the by-product 1,2-propylene glycol can be separated out through simple distillation as a bulk raw material. When the molar ratio of the propylene oxide to the carbon dioxide to the methanol to the other alcohols is 1:1:3:2, the reaction pressure is 5 MPa, the reaction temperatureis 100 DEG C, and the space velocity is 5 hours<-1>, the catalyst is not deactivated and has good stability after being used for 5000 hours. The whole reaction process is clean, efficient and free ofpollution, and no waste is generated.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY

One-step technology for synthesis of ethyl methyl carbonate and co-production of 1,2-propanediol

The invention provides a one-step technology for synthesis of ethyl methyl carbonate and co-production of 1,2-propanediol and relates to a technology for synthesizing ethyl methyl carbonate. Accordingto the technology, ethyl methyl carbonate, diethyl carbonate and 1,2-propanediol are directly synthesized in one step by catalysis of a multifunctional composite alkaline material catalyst. Azeotropic separation is performed synchronously while reactive distillation is performed, a solvent is not needed for extraction and separation of a product, and accordingly, the conventional technological process of synthesis of ethyl methyl carbonate is greatly simplified; meanwhile, multiple components are separated at a time, and the separation purity is high. The maximum selectivity of ethyl methyl carbonate in a crude product obtained by the reaction can reach 70%, and dimethyl carbonate and diethyl carbonate as byproducts can be taken as products to be separated directly and can also be recycled to be reacted continuously for generation of ethyl methyl carbonate, and the byproduct 1,2-propanediol can be taken as a bulk raw material to be separated by simple distillation. The whole reactionprocess is clean, efficient and pollution-free, and no waste is generated.
Owner:SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY
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